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  • regression/Fluid/funnel_comp/AixLib.Fluid.MassExchangers.MembraneBasedEnthalpyExchangers.Examples.Test_EnthalpyExchanger.mat_senTemColOut.T/upperBound.csv

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  • regression/Fluid/funnel_comp/AixLib.Fluid.MassExchangers.MembraneBasedEnthalpyExchangers.Examples.Test_EnthalpyExchanger.mat_senTemColOut.T/test.csv

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  • regression/Fluid/funnel_comp/AixLib.Fluid.MassExchangers.MembraneBasedEnthalpyExchangers.Examples.Test_EnthalpyExchanger.mat_senTemColOut.T/reference.csv

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+155520,346.0928039550781 +157248,345.9334716796875 +158976,345.8753967285156 +160704,345.6378479003906 +162432,345.578369140625 +164160,345.2607116699219 +165888,345.2107849121094 +167616,344.8332214355469 +169344,344.791259765625 +171072,344.3934326171875 +172800,344.3473510742188 diff --git a/docs/correct_HTML_issue1147_GenericBoiler/regression/Fluid/funnel_comp/AixLib.Fluid.Storage.Examples.StorageSolarCollector.mat_temperatureSensor.T/upperBound.csv b/docs/correct_HTML_issue1147_GenericBoiler/regression/Fluid/funnel_comp/AixLib.Fluid.Storage.Examples.StorageSolarCollector.mat_temperatureSensor.T/upperBound.csv new file mode 100644 index 0000000000..693be47577 --- /dev/null +++ b/docs/correct_HTML_issue1147_GenericBoiler/regression/Fluid/funnel_comp/AixLib.Fluid.Storage.Examples.StorageSolarCollector.mat_temperatureSensor.T/upperBound.csv @@ -0,0 +1,106 @@ +x,y +-0.001,293.4431438903808 +1727.999,298.7451630249024 +3455.999,298.7684101257324 +5183.999,298.7904353027344 +6911.999,298.8108414306641 +8639.999,298.8301172790527 +10367.999,298.8478351745605 +12095.999,298.8646060791016 +13823.999,298.8798801269531 +15551.999,298.8943904724121 +17279.999,298.9076483459473 +19007.999,299.112962097168 +20735.999,299.8313311157226 +22463.999,301.0465954589844 +24191.999,302.7776643981933 +25919.999,304.9922180480957 +27647.999,307.6736687927246 +29375.999,310.7850534362793 +31103.999,314.2820772399903 +32831.999,318.1226754760743 +34559.999,322.2277591247558 +36287.999,326.5440828552246 +38015.999,330.9847678833007 +39743.999,335.4898177490234 +41471.999,339.9765082092285 +43199.999,344.400086303711 +44927.999,347.9580230102538 +44928.001,347.9580230102538 +46656.001,346.9651793518066 +48384.001,344.5362391662597 +50112.001,343.3686604003906 +51840.00083726279,342.7223544004665 +53567.999,342.7796014709473 +55295.999,343.0304013366699 +57023.999,343.2535551757812 +57024.001,343.2535551757812 +58752.001,343.1878156738281 +60480.00099999999,342.887466796875 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+114048.001,343.8691604003906 +115776.0004379446,342.5817418738286 +117503.999,343.0849602355957 +119231.999,344.4039353637694 +120959.999,345.1422522888184 +122687.999,345.8186482238769 +124415.999,346.5927675170899 +126143.999,347.7306840820312 +127871.999,348.5637917480469 +129599.999,349.5606372070313 +131327.999,350.1030491943359 +133055.999,350.6834630126953 +134783.999,350.7896481933594 +136511.999,350.8916788330078 +136512.001,350.8916788330078 +138240.001,350.5618510437012 +139968.001,350.2140609741211 +141696.001,349.4990522460938 +143424.001,348.7608575134277 +145152.001,347.9006842346191 +146880.001,347.4127700500488 +148608.001,347.0139341125488 +150336.001,346.8023885498047 +152064.001,346.6401781616211 +153792.001,346.5120594482422 +155520.001,346.4388967590332 +157248.001,346.2794051513672 +158976.001,346.2212721252441 +160704.001,345.983485748291 +162432.001,345.9239475097656 +164160.001,345.6059723815918 +165888.001,345.5559956970215 +167616.001,345.1780546569824 +169344.001,345.1360510253906 +171072.001,344.7378260498047 +172800.001,344.691698425293 diff --git a/docs/correct_HTML_issue1147_GenericBoiler/regression/Fluid/simulator-dymola.log b/docs/correct_HTML_issue1147_GenericBoiler/regression/Fluid/simulator-dymola.log new file mode 100644 index 0000000000..accbfaf4ef --- /dev/null +++ b/docs/correct_HTML_issue1147_GenericBoiler/regression/Fluid/simulator-dymola.log @@ -0,0 +1,4156 @@ + = true + + +rCheck = checkModel("AixLib.Fluid.Movers.PumpsPolynomialBased.Examples.PumpSpeedControlled"); +Check of AixLib.Fluid.Movers.PumpsPolynomialBased.Examples.PumpSpeedControlled +The model has the same number of unknowns and equations: 156 +The model could not be deduced to be symbolically well-posed. +The model has + 144+2*(size(pump.maxMinTable.columns, 1)+pump.deMultiplex2.n1+pump.deMultiplex2.n2) +pump.criticalDamping.n+pump.vol.dynBal.nPorts +scalar unknowns and + 134+2*size(pump.maxMinTable.columns, 1)+pump.deMultiplex2.n1+pump.deMultiplex2.n2 +pump.criticalDamping.n+(if vessle.use_Xi_in then 1 else (if vessle.use_X_in then 0 else 1))+(if not vessle.use_p_in then 1 else 0)+2*vessle.nPorts+(if not vessle.use_T_in then 1 else 0)+(if not pump.vol.dynBal.use_mWat_flow then 1 else 0)+3*pump.vol.dynBal.nPorts +scalar equations. +However, exploiting the given numerical settings of parameters gives the same number of unknowns and equations: + 156 +Check of AixLib.Fluid.Movers.PumpsPolynomialBased.Examples.PumpSpeedControlled successful. +Declaring variable: Boolean rCheck ; + +Modelica.Utilities.Streams.print(" { \"file\" : \"AixLib/Resources/Scripts/Dymola/Fluid/Movers/PumpsPolynomialBased/Examples/PumpSpeedControlled.mos\",", "AixLib.Fluid.Movers.PumpsPolynomialBased.Examples.PumpSpeedControlled.statistics.log"); +Modelica.Utilities.Streams.print(" \"model\" : \"AixLib.Fluid.Movers.PumpsPolynomialBased.Examples.PumpSpeedControlled\",", "AixLib.Fluid.Movers.PumpsPolynomialBased.Examples.PumpSpeedControlled.statistics.log"); +Modelica.Utilities.Streams.print(" \"check\" : {", "AixLib.Fluid.Movers.PumpsPolynomialBased.Examples.PumpSpeedControlled.statistics.log"); +Modelica.Utilities.Streams.print(" \"command\" : \"checkModel(\\\"AixLib.Fluid.Movers.PumpsPolynomialBased.Examples.PumpSpeedControlled\\\");\",", "AixLib.Fluid.Movers.PumpsPolynomialBased.Examples.PumpSpeedControlled.statistics.log"); +Modelica.Utilities.Streams.print(" \"result\" : " + String(rCheck), "AixLib.Fluid.Movers.PumpsPolynomialBased.Examples.PumpSpeedControlled.statistics.log"); +Modelica.Utilities.Streams.print(" },", "AixLib.Fluid.Movers.PumpsPolynomialBased.Examples.PumpSpeedControlled.statistics.log"); + + +rScript=RunScript("modelica://AixLib/Resources/Scripts/Dymola/Fluid/Movers/PumpsPolynomialBased/Examples/PumpSpeedControlled.mos"); +simulateModel("AixLib.Fluid.Movers.PumpsPolynomialBased.Examples.PumpSpeedControlled", tolerance=1e-6, stopTime=600.0, method="dassl", resultFile="AixLib.Fluid.Movers.PumpsPolynomialBased.Examples.PumpSpeedControlled"); +Translation of AixLib.Fluid.Movers.PumpsPolynomialBased.Examples.PumpSpeedControlled +The DAE has 156 scalar unknowns and 156 scalar equations. + +Statistics + +Original Model + Number of components: 35 + Variables: 388 + Constants: 15 (15 scalars) + Parameters: 177 (374 scalars) + Unknowns: 196 (160 scalars) + Differentiated variables: 6 scalars + Equations: 163 + Nontrivial: 137 +Translated Model + Constants: 131 scalars + Free parameters: 190 scalars + Parameter depending: 94 scalars + Outputs: 7 scalars + Continuous time states: 4 scalars + Time-varying variables: 37 scalars + Alias variables: 97 scalars + Number of mixed real/discrete systems of equations: 0 + Sizes of linear systems of equations: { } + Sizes after manipulation of the linear systems: { } + Sizes of nonlinear systems of equations: {1} + Sizes after manipulation of the nonlinear systems: {0} + Number of numerical Jacobians: 0 + Initialization problem + Sizes of nonlinear systems of equations: {1} + Sizes after manipulation of the nonlinear systems: {1} + Number of numerical Jacobians: 0 + +Selected continuous time states +Statically selected continuous time states +pump.criticalDamping.x[1] +pump.criticalDamping.x[2] +simpleValve.filter.s[1] +simpleValve.filter.s[2] +Finished +Finished + = true + +Declaring variable: Boolean rScript ; + +savelog("AixLib.Fluid.Movers.PumpsPolynomialBased.Examples.PumpSpeedControlled.translation.log"); = true + + +rCheck = checkModel("AixLib.Fluid.DistrictHeatingCooling.Demands.Examples.OpenLoopVarTSupplyDp"); +Check of AixLib.Fluid.DistrictHeatingCooling.Demands.Examples.OpenLoopVarTSupplyDp +The model has the same number of unknowns and equations: 522 +The model could not be deduced to be symbolically well-posed. +The model has + 514+pipeSupply.vol_b.dynBal.nPorts+pipeSupply.vol_a.dynBal.nPorts+ pipeReturn.vol_b.dynBal.nPorts+pipeReturn.vol_a.dynBal.nPorts +scalar unknowns and + 479+(if sourceIdeal.source.use_Xi_in then 1 else (if sourceIdeal.source.use_X_in then 0 else 1))+(if not sourceIdeal.source.use_p_in then 1 else 0)+2* sourceIdeal.source.nPorts+(if not sourceIdeal.source.use_T_in then 1 else 0)+ (if sourceIdeal.sink.use_Xi_in then 1 else (if sourceIdeal.sink.use_X_in then 0 else 1))+(if not sourceIdeal.sink.use_p_in then 1 else 0)+2*sourceIdeal.sink.nPorts +(if not sourceIdeal.sink.use_T_in then 1 else 0)+(if demand.sink.use_Xi_in then 1 else (if demand.sink.use_X_in then 0 else 1))+(if not demand.sink.use_m_flow_in then 1 else 0)+2*demand.sink.nPorts+(if not demand.sink.use_T_in then 1 else 0)+(if demand.source.use_Xi_in then 1 else ( if demand.source.use_X_in then 0 else 1))+(if not demand.source.use_m_flow_in then 1 else 0)+2*demand.source.nPorts+(if not demand.source.use_T_in then 1 else 0)+(if not pipeSupply.vol_b.dynBal.use_mWat_flow then 1 else 0)+3* pipeSupply.vol_b.dynBal.nPorts+(if not pipeSupply.vol_a.dynBal.use_mWat_flow then 1 else 0)+3*pipeSupply.vol_a.dynBal.nPorts+(if not pipeReturn.vol_b.dynBal.use_mWat_flow then 1 else 0)+3*pipeReturn.vol_b.dynBal.nPorts+(if not pipeReturn.vol_a.dynBal.use_mWat_flow then 1 else 0)+3*pipeReturn.vol_a.dynBal.nPorts +scalar equations. +However, exploiting the given numerical settings of parameters gives the same number of unknowns and equations: + 522 +Check of AixLib.Fluid.DistrictHeatingCooling.Demands.Examples.OpenLoopVarTSupplyDp successful. +Declaring variable: Boolean rCheck ; + +Modelica.Utilities.Streams.print(" { \"file\" : \"AixLib/Resources/Scripts/Dymola/Fluid/DistrictHeatingCooling/Demands/Examples/OpenLoopVarTSupplyDp.mos\",", "AixLib.Fluid.DistrictHeatingCooling.Demands.Examples.OpenLoopVarTSupplyDp.statistics.log"); +Modelica.Utilities.Streams.print(" \"model\" : \"AixLib.Fluid.DistrictHeatingCooling.Demands.Examples.OpenLoopVarTSupplyDp\",", "AixLib.Fluid.DistrictHeatingCooling.Demands.Examples.OpenLoopVarTSupplyDp.statistics.log"); +Modelica.Utilities.Streams.print(" \"check\" : {", "AixLib.Fluid.DistrictHeatingCooling.Demands.Examples.OpenLoopVarTSupplyDp.statistics.log"); +Modelica.Utilities.Streams.print(" \"command\" : \"checkModel(\\\"AixLib.Fluid.DistrictHeatingCooling.Demands.Examples.OpenLoopVarTSupplyDp\\\");\",", "AixLib.Fluid.DistrictHeatingCooling.Demands.Examples.OpenLoopVarTSupplyDp.statistics.log"); +Modelica.Utilities.Streams.print(" \"result\" : " + String(rCheck), "AixLib.Fluid.DistrictHeatingCooling.Demands.Examples.OpenLoopVarTSupplyDp.statistics.log"); +Modelica.Utilities.Streams.print(" },", "AixLib.Fluid.DistrictHeatingCooling.Demands.Examples.OpenLoopVarTSupplyDp.statistics.log"); + + +rScript=RunScript("modelica://AixLib/Resources/Scripts/Dymola/Fluid/DistrictHeatingCooling/Demands/Examples/OpenLoopVarTSupplyDp.mos"); +translateModel("AixLib.Fluid.DistrictHeatingCooling.Demands.Examples.OpenLoopVarTSupplyDp"); +Translation of AixLib.Fluid.DistrictHeatingCooling.Demands.Examples.OpenLoopVarTSupplyDp +The DAE has 522 scalar unknowns and 522 scalar equations. + +Statistics + +Original Model + Number of components: 105 + Variables: 1376 + Constants: 25 (25 scalars) + Parameters: 625 (601 scalars) + Unknowns: 726 (538 scalars) + Differentiated variables: 15 scalars + Equations: 623 + Nontrivial: 504 +Translated Model + Constants: 457 scalars + Free parameters: 119 scalars + Parameter depending: 129 scalars + Continuous time states: 11 scalars + Time-varying variables: 123 scalars + Alias variables: 336 scalars + Number of mixed real/discrete systems of equations: 0 + Sizes of linear systems of equations: { } + Sizes after manipulation of the linear systems: { } + Sizes of nonlinear systems of equations: {8} + Sizes after manipulation of the nonlinear systems: {1} + Number of numerical Jacobians: 0 + Initialization problem + Sizes of nonlinear systems of equations: {8} + Sizes after manipulation of the nonlinear systems: {1} + Number of numerical Jacobians: 0 + +Selected continuous time states +Statically selected continuous time states +demand.senT_return.T +demand.senT_supply.T +pControl.I.y +pipeReturn.del.x +pipeReturn.timDel.x +pipeReturn.vol_a.dynBal.U +pipeReturn.vol_b.dynBal.U +pipeSupply.del.x +pipeSupply.timDel.x +pipeSupply.vol_a.dynBal.U +pipeSupply.vol_b.dynBal.U +Finished + = true +simulateModel("AixLib.Fluid.DistrictHeatingCooling.Demands.Examples.OpenLoopVarTSupplyDp", stopTime=100000, method="dassl", tolerance=1e-006, resultFile="AixLib.Fluid.DistrictHeatingCooling.Demands.Examples.OpenLoopVarTSupplyDp"); +Finished +Finished + = true + +Declaring variable: Boolean rScript ; + +savelog("AixLib.Fluid.DistrictHeatingCooling.Demands.Examples.OpenLoopVarTSupplyDp.translation.log"); = true + + +rCheck = checkModel("AixLib.Fluid.HeatPumps.ModularReversible.Examples.TableData3D_OneRoomRadiator"); +Check of AixLib.Fluid.HeatPumps.ModularReversible.Examples.TableData3D_OneRoomRadiator +The model has the same number of unknowns and equations: 1647 +The model could not be deduced to be symbolically well-posed. +The model has + 1604+2*(rad.nEle+vol.dynBal.nPorts)+max([size(timTab.columns, 1); size( timTab.offset, 1)])+rad.vol[1].dynBal.nPorts+rad.vol[2].dynBal.nPorts+ rad.vol[3].dynBal.nPorts+rad.vol[4].dynBal.nPorts+rad.vol[5].dynBal.nPorts+ rad.sumCon.nin+rad.sumRad.nin+heaPum.con.vol.dynBal.nPorts+heaPum.eva.vol.dynBal.nPorts +size(heaPum.safCtr.opeEnv.bouMapHea.tabBou.columns, 1)+heaPum.safCtr.opeEnv.bouMapHea.nor.nu +size(heaPum.safCtr.opeEnv.bouMapCoo.tabBou.columns, 1)+heaPum.safCtr.opeEnv.bouMapCoo.nor.nu +scalar unknowns and + 1564+max([size(timTab.columns, 1); size(timTab.offset, 1)])+(if weaDat.pAtmSou == AixLib.BoundaryConditions.Types.DataSource.Parameter then 1 else 0)+(if weaDat.TDewPoiSou == AixLib.BoundaryConditions.Types.DataSource.Parameter then 1 else 0)+(if weaDat.TDryBulSou == AixLib.BoundaryConditions.Types.DataSource. Parameter then 1 else 0)+(if weaDat.TBlaSkySou == AixLib.BoundaryConditions.Types.DataSource. Parameter then 1 else 0)+(if weaDat.relHumSou == AixLib.BoundaryConditions.Types.DataSource. Parameter then 1 else 0)+(if weaDat.opaSkyCovSou == AixLib.BoundaryConditions.Types.DataSource. Parameter then 1 else 0)+(if weaDat.ceiHeiSou == AixLib.BoundaryConditions.Types.DataSource. Parameter then 1 else 0)+(if weaDat.totSkyCovSou == AixLib.BoundaryConditions.Types.DataSource. Parameter then 1 else 0)+(if weaDat.winSpeSou == AixLib.BoundaryConditions.Types.DataSource. Parameter then 1 else 0)+(if weaDat.winDirSou == AixLib.BoundaryConditions.Types.DataSource. Parameter then 1 else 0)+(if weaDat.HInfHorSou == AixLib.BoundaryConditions.Types.DataSource. Parameter then 1 else 0)+(if weaDat.HSou == AixLib.BoundaryConditions.Types.RadiationDataSource. Input_HDirNor_HDifHor then 2 else 1)+(if weaDat.HSou == AixLib.BoundaryConditions.Types.RadiationDataSource. Input_HDirNor_HGloHor then 2 else 1)+(if weaDat.HSou == AixLib.BoundaryConditions.Types.RadiationDataSource. Input_HGloHor_HDifHor then 2 else 1)+(if sou.use_Xi_in then 1 else (if sou.use_X_in then 0 else 1))+(if not sou.use_p_in then 1 else 0)+2*sou.nPorts +(if not sou.use_T_in then 1 else 0)+(if sin.use_Xi_in then 1 else (if sin.use_X_in then 0 else 1))+(if not sin.use_p_in then 1 else 0)+2*sin.nPorts +(if not sin.use_T_in then 1 else 0)+(if preSou.use_Xi_in then 1 else (if preSou.use_X_in then 0 else 1))+(if not preSou.use_p_in then 1 else 0)+2* preSou.nPorts+(if not preSou.use_T_in then 1 else 0)+(if not vol.dynBal.use_mWat_flow then 1 else 0)+5*vol.dynBal.nPorts+(if not rad.vol[1].dynBal.use_mWat_flow then 1 else 0)+3*rad.vol[1].dynBal.nPorts+(if not rad.vol[2].dynBal.use_mWat_flow then 1 else 0)+3*rad.vol[2].dynBal.nPorts +(if not rad.vol[3].dynBal.use_mWat_flow then 1 else 0)+3*rad.vol[3].dynBal.nPorts +(if not rad.vol[4].dynBal.use_mWat_flow then 1 else 0)+3*rad.vol[4].dynBal.nPorts +(if not rad.vol[5].dynBal.use_mWat_flow then 1 else 0)+3*rad.vol[5].dynBal.nPorts +(if not pumHeaPum.vol.steBal.use_mWat_flow then 1 else 0)+(if not pumHeaPumSou.vol.steBal.use_mWat_flow then 1 else 0)+(if not heaPum.con.vol.dynBal.use_mWat_flow then 1 else 0)+3*heaPum.con.vol.dynBal.nPorts+(if not heaPum.eva.vol.dynBal.use_mWat_flow then 1 else 0)+3*heaPum.eva.vol.dynBal.nPorts+size(heaPum.safCtr.opeEnv.bouMapHea.tabBou.columns, 1)+size(heaPum.safCtr.opeEnv.bouMapCoo.tabBou.columns, 1)+2*rad.nEle +scalar equations. +However, exploiting the given numerical settings of parameters gives the same number of unknowns and equations: + 1647 +Check of AixLib.Fluid.HeatPumps.ModularReversible.Examples.TableData3D_OneRoomRadiator successful. +Declaring variable: Boolean rCheck ; + +Modelica.Utilities.Streams.print(" { \"file\" : \"AixLib/Resources/Scripts/Dymola/Fluid/HeatPumps/ModularReversible/Examples/TableData3D_OneRoomRadiator.mos\",", "AixLib.Fluid.HeatPumps.ModularReversible.Examples.TableData3D_OneRoomRadiator.statistics.log"); +Modelica.Utilities.Streams.print(" \"model\" : \"AixLib.Fluid.HeatPumps.ModularReversible.Examples.TableData3D_OneRoomRadiator\",", "AixLib.Fluid.HeatPumps.ModularReversible.Examples.TableData3D_OneRoomRadiator.statistics.log"); +Modelica.Utilities.Streams.print(" \"check\" : {", "AixLib.Fluid.HeatPumps.ModularReversible.Examples.TableData3D_OneRoomRadiator.statistics.log"); +Modelica.Utilities.Streams.print(" \"command\" : \"checkModel(\\\"AixLib.Fluid.HeatPumps.ModularReversible.Examples.TableData3D_OneRoomRadiator\\\");\",", "AixLib.Fluid.HeatPumps.ModularReversible.Examples.TableData3D_OneRoomRadiator.statistics.log"); +Modelica.Utilities.Streams.print(" \"result\" : " + String(rCheck), "AixLib.Fluid.HeatPumps.ModularReversible.Examples.TableData3D_OneRoomRadiator.statistics.log"); +Modelica.Utilities.Streams.print(" },", "AixLib.Fluid.HeatPumps.ModularReversible.Examples.TableData3D_OneRoomRadiator.statistics.log"); + + +rScript=RunScript("modelica://AixLib/Resources/Scripts/Dymola/Fluid/HeatPumps/ModularReversible/Examples/TableData3D_OneRoomRadiator.mos"); +simulateModel("AixLib.Fluid.HeatPumps.ModularReversible.Examples.TableData3D_OneRoomRadiator", stopTime=86400, method="CVode", tolerance=1e-08, resultFile="AixLib.Fluid.HeatPumps.ModularReversible.Examples.TableData3D_OneRoomRadiator"); +Translation of AixLib.Fluid.HeatPumps.ModularReversible.Examples.TableData3D_OneRoomRadiator +The DAE has 1647 scalar unknowns and 1647 scalar equations. + +Statistics + +Original Model + Number of components: 446 + Variables: 3567 + Constants: 78 (78 scalars) + Parameters: 1711 (2047 scalars) + Unknowns: 1778 (1690 scalars) + Differentiated variables: 22 scalars + Equations: 1659 + Nontrivial: 1384 +Translated Model + Constants: 1463 scalars + Free parameters: 250 scalars + Parameter depending: 757 scalars + Outputs: 24 scalars + Continuous time states: 14 scalars + Time-varying variables: 359 scalars + Alias variables: 986 scalars + Number of mixed real/discrete systems of equations: 0 + Sizes of linear systems of equations: {2, 2, 2, 2, 2, 4} + Sizes after manipulation of the linear systems: {0, 0, 0, 0, 0, 0} + Sizes of nonlinear systems of equations: {3} + Sizes after manipulation of the nonlinear systems: {1} + Number of numerical Jacobians: 0 + Initialization problem + Sizes of nonlinear systems of equations: {11, 1, 1, 2} + Sizes after manipulation of the nonlinear systems: {5, 1, 1, 1} + Sizes of simplified homotopy nonlinear systems of equations: {2} + Sizes after manipulation of the simplified homotopy nonlinear systems: {1} + Number of numerical Jacobians: 0 + +Selected continuous time states +Statically selected continuous time states +heaPum.con.vol.dynBal.U +heaPum.eva.vol.dynBal.U +oneRooRadHeaPumCtr.PIDCoo.I.y +oneRooRadHeaPumCtr.PIDHea.I.y +rad.vol[1].dynBal.U +rad.vol[2].dynBal.U +rad.vol[3].dynBal.U +rad.vol[4].dynBal.U +rad.vol[5].dynBal.U +temRet.T +temSup.T +vol.dynBal.m +vol.dynBal.medium.Xi[1] +vol.hOut_internal +Finished +Finished + = true + +Declaring variable: Boolean rScript ; + +savelog("AixLib.Fluid.HeatPumps.ModularReversible.Examples.TableData3D_OneRoomRadiator.translation.log"); = true + + +rCheck = checkModel("AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.StaticPipe"); +Check of AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.StaticPipe +Warning: Local "m_flow_small" conflict with inherited. Should be identical +Warning: Component m_flow_small(min = << Empty >>), + but previously m_flow_small(min = 0). + The components are not identical. + + For element m_flow_small found at + + File: /tmp/tmp-AixLib-0-u7dmbvv4/AixLib/Fluid/DistrictHeatingCooling/Pipes/StaticPipe.mo, line 36 + Conflict with element from + File: /tmp/tmp-AixLib-0-u7dmbvv4/AixLib/Fluid/Interfaces/PartialTwoPortInterface.mo, line 10 + Component context: pip + Component declared as StaticPipe pip in AixLib.Fluid.DistrictHeatingCooling.Pipes + File: /tmp/tmp-AixLib-0-u7dmbvv4/AixLib/Fluid/DistrictHeatingCooling/Pipes/Examples/StaticPipe.mo, line 18 +The model has the same number of unknowns and equations: 175 +The model could not be deduced to be symbolically well-posed. +The model has + 173+pip.vol.dynBal.nPorts +scalar unknowns and + 159+(if sin.use_Xi_in then 1 else (if sin.use_X_in then 0 else 1))+(if not sin.use_p_in then 1 else 0)+2*sin.nPorts+(if not sin.use_T_in then 1 else 0)+ (if sou.use_Xi_in then 1 else (if sou.use_X_in then 0 else 1))+(if not sou.use_m_flow_in then 1 else 0)+2*sou.nPorts+(if not sou.use_T_in then 1 else 0)+(if not pip.vol.dynBal.use_mWat_flow then 1 else 0)+3* pip.vol.dynBal.nPorts +scalar equations. +However, exploiting the given numerical settings of parameters gives the same number of unknowns and equations: + 175 +Check of AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.StaticPipe successful. +Declaring variable: Boolean rCheck ; + +Modelica.Utilities.Streams.print(" { \"file\" : \"AixLib/Resources/Scripts/Dymola/Fluid/DistrictHeatingCooling/Pipes/Examples/StaticPipe.mos\",", "AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.StaticPipe.statistics.log"); +Modelica.Utilities.Streams.print(" \"model\" : \"AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.StaticPipe\",", "AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.StaticPipe.statistics.log"); +Modelica.Utilities.Streams.print(" \"check\" : {", "AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.StaticPipe.statistics.log"); +Modelica.Utilities.Streams.print(" \"command\" : \"checkModel(\\\"AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.StaticPipe\\\");\",", "AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.StaticPipe.statistics.log"); +Modelica.Utilities.Streams.print(" \"result\" : " + String(rCheck), "AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.StaticPipe.statistics.log"); +Modelica.Utilities.Streams.print(" },", "AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.StaticPipe.statistics.log"); + + +rScript=RunScript("modelica://AixLib/Resources/Scripts/Dymola/Fluid/DistrictHeatingCooling/Pipes/Examples/StaticPipe.mos"); +translateModel("AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.StaticPipe"); +Translation of AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.StaticPipe +Warning: Local "m_flow_small" conflict with inherited. Should be identical +Warning: Component m_flow_small(min = << Empty >>), + but previously m_flow_small(min = 0). + The components are not identical. + + For element m_flow_small found at + + File: /tmp/tmp-AixLib-0-u7dmbvv4/AixLib/Fluid/DistrictHeatingCooling/Pipes/StaticPipe.mo, line 36 + Conflict with element from + File: /tmp/tmp-AixLib-0-u7dmbvv4/AixLib/Fluid/Interfaces/PartialTwoPortInterface.mo, line 10 + Component context: pip + Component declared as StaticPipe pip in AixLib.Fluid.DistrictHeatingCooling.Pipes + File: /tmp/tmp-AixLib-0-u7dmbvv4/AixLib/Fluid/DistrictHeatingCooling/Pipes/Examples/StaticPipe.mo, line 18 +The DAE has 175 scalar unknowns and 175 scalar equations. + +Statistics + +Original Model + Number of components: 33 + Variables: 506 + Constants: 10 (10 scalars) + Parameters: 251 (244 scalars) + Unknowns: 245 (181 scalars) + Differentiated variables: 4 scalars + Equations: 205 + Nontrivial: 171 +Translated Model + Constants: 185 scalars + Free parameters: 45 scalars + Parameter depending: 61 scalars + Continuous time states: 3 scalars + Time-varying variables: 31 scalars + Alias variables: 113 scalars + Number of mixed real/discrete systems of equations: 0 + Sizes of linear systems of equations: { } + Sizes after manipulation of the linear systems: { } + Sizes of nonlinear systems of equations: { } + Sizes after manipulation of the nonlinear systems: { } + Number of numerical Jacobians: 0 + +Selected continuous time states +Statically selected continuous time states +pip.vol.dynBal.U +senTemIn.T +senTemOut.T +Finished +Warning: WARNINGS have been issued. + = true +simulateModel("AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.StaticPipe", stopTime=1000, method="dassl", tolerance=1e-006, resultFile="AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.StaticPipe"); +Finished + = true + +Declaring variable: Boolean rScript ; + +savelog("AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.StaticPipe.translation.log"); = true + + +rCheck = checkModel("AixLib.Fluid.Storage.Examples.StorageDetailedExample"); +Check of AixLib.Fluid.Storage.Examples.StorageDetailedExample +The model has the same number of unknowns and equations: 2714 +Check of AixLib.Fluid.Storage.Examples.StorageDetailedExample successful. +Declaring variable: Boolean rCheck ; + +Modelica.Utilities.Streams.print(" { \"file\" : \"AixLib/Resources/Scripts/Dymola/Fluid/Storage/Examples/StorageDetailedExample.mos\",", "AixLib.Fluid.Storage.Examples.StorageDetailedExample.statistics.log"); +Modelica.Utilities.Streams.print(" \"model\" : \"AixLib.Fluid.Storage.Examples.StorageDetailedExample\",", "AixLib.Fluid.Storage.Examples.StorageDetailedExample.statistics.log"); +Modelica.Utilities.Streams.print(" \"check\" : {", "AixLib.Fluid.Storage.Examples.StorageDetailedExample.statistics.log"); +Modelica.Utilities.Streams.print(" \"command\" : \"checkModel(\\\"AixLib.Fluid.Storage.Examples.StorageDetailedExample\\\");\",", "AixLib.Fluid.Storage.Examples.StorageDetailedExample.statistics.log"); +Modelica.Utilities.Streams.print(" \"result\" : " + String(rCheck), "AixLib.Fluid.Storage.Examples.StorageDetailedExample.statistics.log"); +Modelica.Utilities.Streams.print(" },", "AixLib.Fluid.Storage.Examples.StorageDetailedExample.statistics.log"); + + +rScript=RunScript("modelica://AixLib/Resources/Scripts/Dymola/Fluid/Storage/Examples/StorageDetailedExample.mos"); +simulateModel("AixLib.Fluid.Storage.Examples.StorageDetailedExample", tolerance=1e-6, stopTime=86400, method="dassl", resultFile="AixLib.Fluid.Storage.Examples.StorageDetailedExample"); +Translation of AixLib.Fluid.Storage.Examples.StorageDetailedExample +The DAE has 2714 scalar unknowns and 2714 scalar equations. + +Statistics + +Original Model + Number of components: 532 + Variables: 7113 + Constants: 124 (124 scalars) + Parameters: 3345 (3234 scalars) + Unknowns: 3644 (2792 scalars) + Differentiated variables: 92 scalars + Equations: 2756 + Nontrivial: 2117 +Translated Model + Constants: 2427 scalars + Free parameters: 221 scalars + Parameter depending: 1324 scalars + Continuous time states: 66 scalars + Time-varying variables: 623 scalars + Alias variables: 1555 scalars + Number of mixed real/discrete systems of equations: 0 + Sizes of linear systems of equations: {2, 2, 4, 3, 3, 2, 2, 2, 2, 2, 2, 2, 2, 2, 4, 3, 3, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2} + Sizes after manipulation of the linear systems: {0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0} + Sizes of nonlinear systems of equations: {6, 6, 6, 6, 6, 6, 6, 6} + Sizes after manipulation of the nonlinear systems: {1, 1, 1, 1, 1, 1, 1, 1} + Number of numerical Jacobians: 0 + +Selected continuous time states +Statically selected continuous time states +bufferStorage.bottomCover.loadIns.T +bufferStorage.bottomCover.loadWall.T +bufferStorage.heatingCoil1.pipe[1].del.x +bufferStorage.heatingCoil1.pipe[1].timDel.x +bufferStorage.heatingCoil1.pipe[1].vol_a.dynBal.U +bufferStorage.heatingCoil1.pipe[1].vol_b.dynBal.U +bufferStorage.heatingCoil1.pipe[2].del.x +bufferStorage.heatingCoil1.pipe[2].timDel.x +bufferStorage.heatingCoil1.pipe[2].vol_a.dynBal.U +bufferStorage.heatingCoil1.pipe[2].vol_b.dynBal.U +bufferStorage.heatingCoil1.pipe[3].del.x +bufferStorage.heatingCoil1.pipe[3].timDel.x +bufferStorage.heatingCoil1.pipe[3].vol_a.dynBal.U +bufferStorage.heatingCoil1.pipe[3].vol_b.dynBal.U +bufferStorage.heatingCoil1.pipe[4].del.x +bufferStorage.heatingCoil1.pipe[4].timDel.x +bufferStorage.heatingCoil1.pipe[4].vol_a.dynBal.U +bufferStorage.heatingCoil1.pipe[4].vol_b.dynBal.U +bufferStorage.heatingCoil1.pipe[5].del.x +bufferStorage.heatingCoil1.pipe[5].timDel.x +bufferStorage.heatingCoil1.pipe[5].vol_a.dynBal.U +bufferStorage.heatingCoil1.pipe[5].vol_b.dynBal.U +bufferStorage.heatingCoil1.pipe[6].del.x +bufferStorage.heatingCoil1.pipe[6].timDel.x +bufferStorage.heatingCoil1.pipe[6].vol_a.dynBal.U +bufferStorage.heatingCoil1.pipe[6].vol_b.dynBal.U +bufferStorage.heatingCoil1.pipe[7].del.x +bufferStorage.heatingCoil1.pipe[7].timDel.x +bufferStorage.heatingCoil1.pipe[7].vol_a.dynBal.U +bufferStorage.heatingCoil1.pipe[7].vol_b.dynBal.U +bufferStorage.heatingCoil1.pipe[8].del.x +bufferStorage.heatingCoil1.pipe[8].timDel.x +bufferStorage.heatingCoil1.pipe[8].vol_a.dynBal.U +bufferStorage.heatingCoil1.pipe[8].vol_b.dynBal.U +bufferStorage.layer[1].dynBal.U +bufferStorage.layer[2].dynBal.U +bufferStorage.layer[3].dynBal.U +bufferStorage.layer[4].dynBal.U +bufferStorage.layer[5].dynBal.U +bufferStorage.layer[6].dynBal.U +bufferStorage.layer[7].dynBal.U +bufferStorage.layer[8].dynBal.U +bufferStorage.layer[9].dynBal.U +bufferStorage.layer[10].dynBal.U +bufferStorage.storageMantle[1].Insulation.CylindricLoad1.heatCapacitor.T +bufferStorage.storageMantle[1].Wall.CylindricLoad1.heatCapacitor.T +bufferStorage.storageMantle[2].Insulation.CylindricLoad1.heatCapacitor.T +bufferStorage.storageMantle[2].Wall.CylindricLoad1.heatCapacitor.T +bufferStorage.storageMantle[3].Insulation.CylindricLoad1.heatCapacitor.T +bufferStorage.storageMantle[3].Wall.CylindricLoad1.heatCapacitor.T +bufferStorage.storageMantle[4].Insulation.CylindricLoad1.heatCapacitor.T +bufferStorage.storageMantle[4].Wall.CylindricLoad1.heatCapacitor.T +bufferStorage.storageMantle[5].Insulation.CylindricLoad1.heatCapacitor.T +bufferStorage.storageMantle[5].Wall.CylindricLoad1.heatCapacitor.T +bufferStorage.storageMantle[6].Insulation.CylindricLoad1.heatCapacitor.T +bufferStorage.storageMantle[6].Wall.CylindricLoad1.heatCapacitor.T +bufferStorage.storageMantle[7].Insulation.CylindricLoad1.heatCapacitor.T +bufferStorage.storageMantle[7].Wall.CylindricLoad1.heatCapacitor.T +bufferStorage.storageMantle[8].Insulation.CylindricLoad1.heatCapacitor.T +bufferStorage.storageMantle[8].Wall.CylindricLoad1.heatCapacitor.T +bufferStorage.storageMantle[9].Insulation.CylindricLoad1.heatCapacitor.T +bufferStorage.storageMantle[9].Wall.CylindricLoad1.heatCapacitor.T +bufferStorage.storageMantle[10].Insulation.CylindricLoad1.heatCapacitor.T +bufferStorage.storageMantle[10].Wall.CylindricLoad1.heatCapacitor.T +bufferStorage.topCover.loadIns.T +bufferStorage.topCover.loadWall.T +Finished +Finished + = true + +Declaring variable: Boolean rScript ; + +savelog("AixLib.Fluid.Storage.Examples.StorageDetailedExample.translation.log"); = true + + +rCheck = checkModel("AixLib.Fluid.MassExchangers.MembraneBasedEnthalpyExchangers.Validation.StaticValidation"); +Check of AixLib.Fluid.MassExchangers.MembraneBasedEnthalpyExchangers.Validation.StaticValidation +The model has the same number of unknowns and equations: 5511 +The model could not be deduced to be symbolically well-posed. +The model has + 3783+32*enthalpyExchanger.n+16*enthalpyExchanger.airDuct2.heatTransfer.n+18* enthalpyExchanger.airDuct2.massTransfer.n+16*enthalpyExchanger.airDuct1.heatTransfer.n +18*enthalpyExchanger.airDuct1.massTransfer.n+5*enthalpyExchanger.membrane.heatTransfer.n +enthalpyExchanger.membrane.massTransfer.n+2*enthalpyExchanger.airDuct2.vol[1].dynBal.nPorts +2*enthalpyExchanger.airDuct2.vol[2].dynBal.nPorts+2*enthalpyExchanger.airDuct2.vol[3].dynBal.nPorts +2*enthalpyExchanger.airDuct2.vol[4].dynBal.nPorts+2*enthalpyExchanger.airDuct2.vol[5].dynBal.nPorts +2*enthalpyExchanger.airDuct2.vol[6].dynBal.nPorts+2*enthalpyExchanger.airDuct2.vol[7].dynBal.nPorts +2*enthalpyExchanger.airDuct2.vol[8].dynBal.nPorts+2*enthalpyExchanger.airDuct2.vol[9].dynBal.nPorts +2*enthalpyExchanger.airDuct2.vol[10].dynBal.nPorts+2*enthalpyExchanger.airDuct2.vol[11].dynBal.nPorts +2*enthalpyExchanger.airDuct2.vol[12].dynBal.nPorts+2*enthalpyExchanger.airDuct2.vol[13].dynBal.nPorts +2*enthalpyExchanger.airDuct2.vol[14].dynBal.nPorts+2*enthalpyExchanger.airDuct2.vol[15].dynBal.nPorts +2*enthalpyExchanger.airDuct1.vol[1].dynBal.nPorts+2*enthalpyExchanger.airDuct1.vol[2].dynBal.nPorts +2*enthalpyExchanger.airDuct1.vol[3].dynBal.nPorts+2*enthalpyExchanger.airDuct1.vol[4].dynBal.nPorts +2*enthalpyExchanger.airDuct1.vol[5].dynBal.nPorts+2*enthalpyExchanger.airDuct1.vol[6].dynBal.nPorts +2*enthalpyExchanger.airDuct1.vol[7].dynBal.nPorts+2*enthalpyExchanger.airDuct1.vol[8].dynBal.nPorts +2*enthalpyExchanger.airDuct1.vol[9].dynBal.nPorts+2*enthalpyExchanger.airDuct1.vol[10].dynBal.nPorts +2*enthalpyExchanger.airDuct1.vol[11].dynBal.nPorts+2*enthalpyExchanger.airDuct1.vol[12].dynBal.nPorts +2*enthalpyExchanger.airDuct1.vol[13].dynBal.nPorts+2*enthalpyExchanger.airDuct1.vol[14].dynBal.nPorts +2*enthalpyExchanger.airDuct1.vol[15].dynBal.nPorts+max([size(bondaryEta.columns, 1); size(bondaryEta.offset, 1)])+max([size(bondaryOda.columns, 1); size( bondaryOda.offset, 1)])+max([size(Results.columns, 1); size(Results.offset, 1)]) +2*fan.vol.dynBal.nPorts+2*fan1.vol.dynBal.nPorts +scalar unknowns and + 3435+17*enthalpyExchanger.airDuct2.heatTransfer.n+19*enthalpyExchanger.airDuct2.massTransfer.n +3*(if enthalpyExchanger.couFloArr then 2*enthalpyExchanger.n else 0)+17* enthalpyExchanger.airDuct1.heatTransfer.n+19*enthalpyExchanger.airDuct1.massTransfer.n +7*enthalpyExchanger.membrane.heatTransfer.n+3*enthalpyExchanger.membrane.massTransfer.n +2*(if enthalpyExchanger.useConPer then 1 else 0)+32*enthalpyExchanger.n+(if souEta.use_Xi_in then 2 else (if souEta.use_X_in then 1 else 3))+3* souEta.nPorts+(if not souEta.use_p_in then 1 else 0)+(if not souEta.use_T_in then 1 else 0)+(if sinEha.use_Xi_in then 2 else (if sinEha.use_X_in then 1 else 3))+3*sinEha.nPorts+(if not sinEha.use_p_in then 1 else 0)+(if not sinEha.use_T_in then 1 else 0)+(if souOda.use_Xi_in then 2 else (if souOda.use_X_in then 1 else 3))+3*souOda.nPorts+(if not souOda.use_p_in then 1 else 0)+(if not souOda.use_T_in then 1 else 0)+(if sinSup.use_Xi_in then 2 else (if sinSup.use_X_in then 1 else 3))+3*sinSup.nPorts+(if not sinSup.use_p_in then 1 else 0)+(if not sinSup.use_T_in then 1 else 0)+max([ size(bondaryEta.columns, 1); size(bondaryEta.offset, 1)])+max([size( bondaryOda.columns, 1); size(bondaryOda.offset, 1)])+max([size(Results.columns, 1); size(Results.offset, 1)])+(if conPID.reset <> AixLib.Types.Reset.Input then 1 else 0)+(if conPID1.reset <> AixLib.Types.Reset.Input then 1 else 0)+5 *enthalpyExchanger.airDuct2.vol[1].dynBal.nPorts+5*enthalpyExchanger.airDuct2.vol[2].dynBal.nPorts +5*enthalpyExchanger.airDuct2.vol[3].dynBal.nPorts+5*enthalpyExchanger.airDuct2.vol[4].dynBal.nPorts +5*enthalpyExchanger.airDuct2.vol[5].dynBal.nPorts+5*enthalpyExchanger.airDuct2.vol[6].dynBal.nPorts +5*enthalpyExchanger.airDuct2.vol[7].dynBal.nPorts+5*enthalpyExchanger.airDuct2.vol[8].dynBal.nPorts +5*enthalpyExchanger.airDuct2.vol[9].dynBal.nPorts+5*enthalpyExchanger.airDuct2.vol[10].dynBal.nPorts +5*enthalpyExchanger.airDuct2.vol[11].dynBal.nPorts+5*enthalpyExchanger.airDuct2.vol[12].dynBal.nPorts +5*enthalpyExchanger.airDuct2.vol[13].dynBal.nPorts+5*enthalpyExchanger.airDuct2.vol[14].dynBal.nPorts +5*enthalpyExchanger.airDuct2.vol[15].dynBal.nPorts+5*enthalpyExchanger.airDuct1.vol[1].dynBal.nPorts +5*enthalpyExchanger.airDuct1.vol[2].dynBal.nPorts+5*enthalpyExchanger.airDuct1.vol[3].dynBal.nPorts +5*enthalpyExchanger.airDuct1.vol[4].dynBal.nPorts+5*enthalpyExchanger.airDuct1.vol[5].dynBal.nPorts +5*enthalpyExchanger.airDuct1.vol[6].dynBal.nPorts+5*enthalpyExchanger.airDuct1.vol[7].dynBal.nPorts +5*enthalpyExchanger.airDuct1.vol[8].dynBal.nPorts+5*enthalpyExchanger.airDuct1.vol[9].dynBal.nPorts +5*enthalpyExchanger.airDuct1.vol[10].dynBal.nPorts+5*enthalpyExchanger.airDuct1.vol[11].dynBal.nPorts +5*enthalpyExchanger.airDuct1.vol[12].dynBal.nPorts+5*enthalpyExchanger.airDuct1.vol[13].dynBal.nPorts +5*enthalpyExchanger.airDuct1.vol[14].dynBal.nPorts+5*enthalpyExchanger.airDuct1.vol[15].dynBal.nPorts +(if not fan.vol.dynBal.use_mWat_flow then 1 else 0)+5*fan.vol.dynBal.nPorts+ (if (if conPID.reset == AixLib.Types.Reset.Disabled then conPID.reset else AixLib.Types.Reset.Input) <> AixLib.Types.Reset.Input then 1 else 0)+(if (if conPID.reset == AixLib.Types.Reset.Disabled then conPID.reset else AixLib.Types.Reset.Input) == AixLib.Types.Reset.Disabled then 1 else 0)+(if not fan1.vol.dynBal.use_mWat_flow then 1 else 0)+5*fan1.vol.dynBal.nPorts+( if (if conPID1.reset == AixLib.Types.Reset.Disabled then conPID1.reset else AixLib.Types.Reset.Input) <> AixLib.Types.Reset.Input then 1 else 0)+(if (if conPID1.reset == AixLib.Types.Reset.Disabled then conPID1.reset else AixLib.Types.Reset.Input) == AixLib.Types.Reset.Disabled then 1 else 0) +scalar equations. +However, exploiting the given numerical settings of parameters gives the same number of unknowns and equations: + 5511 +Check of AixLib.Fluid.MassExchangers.MembraneBasedEnthalpyExchangers.Validation.StaticValidation successful. +Declaring variable: Boolean rCheck ; + +Modelica.Utilities.Streams.print(" { \"file\" : \"AixLib/Resources/Scripts/Dymola/Fluid/MassExchangers/MembraneBasedEnthalpyExchangers/Validation/StaticValidation.mos\",", "AixLib.Fluid.MassExchangers.MembraneBasedEnthalpyExchangers.Validation.StaticValidation.statistics.log"); +Modelica.Utilities.Streams.print(" \"model\" : \"AixLib.Fluid.MassExchangers.MembraneBasedEnthalpyExchangers.Validation.StaticValidation\",", "AixLib.Fluid.MassExchangers.MembraneBasedEnthalpyExchangers.Validation.StaticValidation.statistics.log"); +Modelica.Utilities.Streams.print(" \"check\" : {", "AixLib.Fluid.MassExchangers.MembraneBasedEnthalpyExchangers.Validation.StaticValidation.statistics.log"); +Modelica.Utilities.Streams.print(" \"command\" : \"checkModel(\\\"AixLib.Fluid.MassExchangers.MembraneBasedEnthalpyExchangers.Validation.StaticValidation\\\");\",", "AixLib.Fluid.MassExchangers.MembraneBasedEnthalpyExchangers.Validation.StaticValidation.statistics.log"); +Modelica.Utilities.Streams.print(" \"result\" : " + String(rCheck), "AixLib.Fluid.MassExchangers.MembraneBasedEnthalpyExchangers.Validation.StaticValidation.statistics.log"); +Modelica.Utilities.Streams.print(" },", "AixLib.Fluid.MassExchangers.MembraneBasedEnthalpyExchangers.Validation.StaticValidation.statistics.log"); + + +rScript=RunScript("modelica://AixLib/Resources/Scripts/Dymola/Fluid/MassExchangers/MembraneBasedEnthalpyExchangers/Validation/StaticValidation.mos"); +simulateModel("AixLib.Fluid.MassExchangers.MembraneBasedEnthalpyExchangers.Validation.StaticValidation", stopTime=29600, numberOfIntervals=0, outputInterval=1, method="dassl",tolerance=1E-6, resultFile="AixLib.Fluid.MassExchangers.MembraneBasedEnthalpyExchangers.Validation.StaticValidation"); +Translation of AixLib.Fluid.MassExchangers.MembraneBasedEnthalpyExchangers.Validation.StaticValidation +The DAE has 5511 scalar unknowns and 5511 scalar equations. +Redundant consistent initial conditions. +Removed the following equations which are redundant and consistent: + fan1.vol.p_start = fan1.p_start; + if (enthalpyExchanger.airDuct2.vol[1].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (enthalpyExchanger.airDuct2.vol[1].dynBal.initialize_p) then + enthalpyExchanger.airDuct2.vol[1].dynBal.medium.p = enthalpyExchanger.airDuct2.vol[1].dynBal.p_start; + end if; + else + if (enthalpyExchanger.airDuct2.vol[1].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then + if (enthalpyExchanger.airDuct2.vol[1].dynBal.initialize_p) then + der(enthalpyExchanger.airDuct2.vol[1].dynBal.medium.p) = 0; + end if; + end if; + end if; + if (enthalpyExchanger.airDuct2.vol[2].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (enthalpyExchanger.airDuct2.vol[2].dynBal.initialize_p) then + enthalpyExchanger.airDuct2.vol[2].dynBal.medium.p = enthalpyExchanger.airDuct2.vol[2].dynBal.p_start; + end if; + else + if (enthalpyExchanger.airDuct2.vol[2].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then + if (enthalpyExchanger.airDuct2.vol[2].dynBal.initialize_p) then + der(enthalpyExchanger.airDuct2.vol[2].dynBal.medium.p) = 0; + end if; + end if; + end if; + if (enthalpyExchanger.airDuct2.vol[3].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (enthalpyExchanger.airDuct2.vol[3].dynBal.initialize_p) then + enthalpyExchanger.airDuct2.vol[3].dynBal.medium.p = enthalpyExchanger.airDuct2.vol[3].dynBal.p_start; + end if; + else + if (enthalpyExchanger.airDuct2.vol[3].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then + if (enthalpyExchanger.airDuct2.vol[3].dynBal.initialize_p) then + der(enthalpyExchanger.airDuct2.vol[3].dynBal.medium.p) = 0; + end if; + end if; + end if; + if (enthalpyExchanger.airDuct2.vol[4].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (enthalpyExchanger.airDuct2.vol[4].dynBal.initialize_p) then + enthalpyExchanger.airDuct2.vol[4].dynBal.medium.p = enthalpyExchanger.airDuct2.vol[4].dynBal.p_start; + end if; + else + if (enthalpyExchanger.airDuct2.vol[4].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then + if (enthalpyExchanger.airDuct2.vol[4].dynBal.initialize_p) then + der(enthalpyExchanger.airDuct2.vol[4].dynBal.medium.p) = 0; + end if; + end if; + end if; + if (enthalpyExchanger.airDuct2.vol[5].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (enthalpyExchanger.airDuct2.vol[5].dynBal.initialize_p) then + enthalpyExchanger.airDuct2.vol[5].dynBal.medium.p = enthalpyExchanger.airDuct2.vol[5].dynBal.p_start; + end if; + else + if (enthalpyExchanger.airDuct2.vol[5].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then + if (enthalpyExchanger.airDuct2.vol[5].dynBal.initialize_p) then + der(enthalpyExchanger.airDuct2.vol[5].dynBal.medium.p) = 0; + end if; + end if; + end if; + if (enthalpyExchanger.airDuct2.vol[6].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (enthalpyExchanger.airDuct2.vol[6].dynBal.initialize_p) then + enthalpyExchanger.airDuct2.vol[6].dynBal.medium.p = enthalpyExchanger.airDuct2.vol[6].dynBal.p_start; + end if; + else + if (enthalpyExchanger.airDuct2.vol[6].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then + if (enthalpyExchanger.airDuct2.vol[6].dynBal.initialize_p) then + der(enthalpyExchanger.airDuct2.vol[6].dynBal.medium.p) = 0; + end if; + end if; + end if; + if (enthalpyExchanger.airDuct2.vol[7].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (enthalpyExchanger.airDuct2.vol[7].dynBal.initialize_p) then + enthalpyExchanger.airDuct2.vol[7].dynBal.medium.p = enthalpyExchanger.airDuct2.vol[7].dynBal.p_start; + end if; + else + if (enthalpyExchanger.airDuct2.vol[7].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then + if (enthalpyExchanger.airDuct2.vol[7].dynBal.initialize_p) then + der(enthalpyExchanger.airDuct2.vol[7].dynBal.medium.p) = 0; + end if; + end if; + end if; + if (enthalpyExchanger.airDuct2.vol[8].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (enthalpyExchanger.airDuct2.vol[8].dynBal.initialize_p) then + enthalpyExchanger.airDuct2.vol[8].dynBal.medium.p = enthalpyExchanger.airDuct2.vol[8].dynBal.p_start; + end if; + else + if (enthalpyExchanger.airDuct2.vol[8].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then + if (enthalpyExchanger.airDuct2.vol[8].dynBal.initialize_p) then + der(enthalpyExchanger.airDuct2.vol[8].dynBal.medium.p) = 0; + end if; + end if; + end if; + if (enthalpyExchanger.airDuct2.vol[9].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (enthalpyExchanger.airDuct2.vol[9].dynBal.initialize_p) then + enthalpyExchanger.airDuct2.vol[9].dynBal.medium.p = enthalpyExchanger.airDuct2.vol[9].dynBal.p_start; + end if; + else + if (enthalpyExchanger.airDuct2.vol[9].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then + if (enthalpyExchanger.airDuct2.vol[9].dynBal.initialize_p) then + der(enthalpyExchanger.airDuct2.vol[9].dynBal.medium.p) = 0; + end if; + end if; + end if; + if (enthalpyExchanger.airDuct2.vol[10].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (enthalpyExchanger.airDuct2.vol[10].dynBal.initialize_p) then + enthalpyExchanger.airDuct2.vol[10].dynBal.medium.p = enthalpyExchanger.airDuct2.vol[10].dynBal.p_start; + end if; + else + if (enthalpyExchanger.airDuct2.vol[10].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then + if (enthalpyExchanger.airDuct2.vol[10].dynBal.initialize_p) then + der(enthalpyExchanger.airDuct2.vol[10].dynBal.medium.p) = 0; + end if; + end if; + end if; + if (enthalpyExchanger.airDuct2.vol[11].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (enthalpyExchanger.airDuct2.vol[11].dynBal.initialize_p) then + enthalpyExchanger.airDuct2.vol[11].dynBal.medium.p = enthalpyExchanger.airDuct2.vol[11].dynBal.p_start; + end if; + else + if (enthalpyExchanger.airDuct2.vol[11].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then + if (enthalpyExchanger.airDuct2.vol[11].dynBal.initialize_p) then + der(enthalpyExchanger.airDuct2.vol[11].dynBal.medium.p) = 0; + end if; + end if; + end if; + if (enthalpyExchanger.airDuct2.vol[12].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (enthalpyExchanger.airDuct2.vol[12].dynBal.initialize_p) then + enthalpyExchanger.airDuct2.vol[12].dynBal.medium.p = enthalpyExchanger.airDuct2.vol[12].dynBal.p_start; + end if; + else + if (enthalpyExchanger.airDuct2.vol[12].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then + if (enthalpyExchanger.airDuct2.vol[12].dynBal.initialize_p) then + der(enthalpyExchanger.airDuct2.vol[12].dynBal.medium.p) = 0; + end if; + end if; + end if; + if (enthalpyExchanger.airDuct2.vol[13].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (enthalpyExchanger.airDuct2.vol[13].dynBal.initialize_p) then + enthalpyExchanger.airDuct2.vol[13].dynBal.medium.p = enthalpyExchanger.airDuct2.vol[13].dynBal.p_start; + end if; + else + if (enthalpyExchanger.airDuct2.vol[13].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then + if (enthalpyExchanger.airDuct2.vol[13].dynBal.initialize_p) then + der(enthalpyExchanger.airDuct2.vol[13].dynBal.medium.p) = 0; + end if; + end if; + end if; + if (enthalpyExchanger.airDuct2.vol[14].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (enthalpyExchanger.airDuct2.vol[14].dynBal.initialize_p) then + enthalpyExchanger.airDuct2.vol[14].dynBal.medium.p = enthalpyExchanger.airDuct2.vol[14].dynBal.p_start; + end if; + else + if (enthalpyExchanger.airDuct2.vol[14].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then + if (enthalpyExchanger.airDuct2.vol[14].dynBal.initialize_p) then + der(enthalpyExchanger.airDuct2.vol[14].dynBal.medium.p) = 0; + end if; + end if; + end if; + if (enthalpyExchanger.airDuct2.vol[15].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (enthalpyExchanger.airDuct2.vol[15].dynBal.initialize_p) then + enthalpyExchanger.airDuct2.vol[15].dynBal.medium.p = enthalpyExchanger.airDuct2.vol[15].dynBal.p_start; + end if; + else + if (enthalpyExchanger.airDuct2.vol[15].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then + if (enthalpyExchanger.airDuct2.vol[15].dynBal.initialize_p) then + der(enthalpyExchanger.airDuct2.vol[15].dynBal.medium.p) = 0; + end if; + end if; + end if; + if (enthalpyExchanger.airDuct1.vol[1].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (enthalpyExchanger.airDuct1.vol[1].dynBal.initialize_p) then + enthalpyExchanger.airDuct1.vol[1].dynBal.medium.p = enthalpyExchanger.airDuct1.vol[1].dynBal.p_start; + end if; + else + if (enthalpyExchanger.airDuct1.vol[1].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then + if (enthalpyExchanger.airDuct1.vol[1].dynBal.initialize_p) then + der(enthalpyExchanger.airDuct1.vol[1].dynBal.medium.p) = 0; + end if; + end if; + end if; + if (enthalpyExchanger.airDuct1.vol[2].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (enthalpyExchanger.airDuct1.vol[2].dynBal.initialize_p) then + enthalpyExchanger.airDuct1.vol[2].dynBal.medium.p = enthalpyExchanger.airDuct1.vol[2].dynBal.p_start; + end if; + else + if (enthalpyExchanger.airDuct1.vol[2].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then + if (enthalpyExchanger.airDuct1.vol[2].dynBal.initialize_p) then + der(enthalpyExchanger.airDuct1.vol[2].dynBal.medium.p) = 0; + end if; + end if; + end if; + if (enthalpyExchanger.airDuct1.vol[3].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (enthalpyExchanger.airDuct1.vol[3].dynBal.initialize_p) then + enthalpyExchanger.airDuct1.vol[3].dynBal.medium.p = enthalpyExchanger.airDuct1.vol[3].dynBal.p_start; + end if; + else + if (enthalpyExchanger.airDuct1.vol[3].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then + if (enthalpyExchanger.airDuct1.vol[3].dynBal.initialize_p) then + der(enthalpyExchanger.airDuct1.vol[3].dynBal.medium.p) = 0; + end if; + end if; + end if; + if (enthalpyExchanger.airDuct1.vol[4].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (enthalpyExchanger.airDuct1.vol[4].dynBal.initialize_p) then + enthalpyExchanger.airDuct1.vol[4].dynBal.medium.p = enthalpyExchanger.airDuct1.vol[4].dynBal.p_start; + end if; + else + if (enthalpyExchanger.airDuct1.vol[4].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then + if (enthalpyExchanger.airDuct1.vol[4].dynBal.initialize_p) then + der(enthalpyExchanger.airDuct1.vol[4].dynBal.medium.p) = 0; + end if; + end if; + end if; + if (enthalpyExchanger.airDuct1.vol[5].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (enthalpyExchanger.airDuct1.vol[5].dynBal.initialize_p) then + enthalpyExchanger.airDuct1.vol[5].dynBal.medium.p = enthalpyExchanger.airDuct1.vol[5].dynBal.p_start; + end if; + else + if (enthalpyExchanger.airDuct1.vol[5].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then + if (enthalpyExchanger.airDuct1.vol[5].dynBal.initialize_p) then + der(enthalpyExchanger.airDuct1.vol[5].dynBal.medium.p) = 0; + end if; + end if; + end if; + if (enthalpyExchanger.airDuct1.vol[6].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (enthalpyExchanger.airDuct1.vol[6].dynBal.initialize_p) then + enthalpyExchanger.airDuct1.vol[6].dynBal.medium.p = enthalpyExchanger.airDuct1.vol[6].dynBal.p_start; + end if; + else + if (enthalpyExchanger.airDuct1.vol[6].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then + if (enthalpyExchanger.airDuct1.vol[6].dynBal.initialize_p) then + der(enthalpyExchanger.airDuct1.vol[6].dynBal.medium.p) = 0; + end if; + end if; + end if; + if (enthalpyExchanger.airDuct1.vol[7].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (enthalpyExchanger.airDuct1.vol[7].dynBal.initialize_p) then + enthalpyExchanger.airDuct1.vol[7].dynBal.medium.p = enthalpyExchanger.airDuct1.vol[7].dynBal.p_start; + end if; + else + if (enthalpyExchanger.airDuct1.vol[7].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then + if (enthalpyExchanger.airDuct1.vol[7].dynBal.initialize_p) then + der(enthalpyExchanger.airDuct1.vol[7].dynBal.medium.p) = 0; + end if; + end if; + end if; + if (enthalpyExchanger.airDuct1.vol[8].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (enthalpyExchanger.airDuct1.vol[8].dynBal.initialize_p) then + enthalpyExchanger.airDuct1.vol[8].dynBal.medium.p = enthalpyExchanger.airDuct1.vol[8].dynBal.p_start; + end if; + else + if (enthalpyExchanger.airDuct1.vol[8].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then + if (enthalpyExchanger.airDuct1.vol[8].dynBal.initialize_p) then + der(enthalpyExchanger.airDuct1.vol[8].dynBal.medium.p) = 0; + end if; + end if; + end if; + if (enthalpyExchanger.airDuct1.vol[9].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (enthalpyExchanger.airDuct1.vol[9].dynBal.initialize_p) then + enthalpyExchanger.airDuct1.vol[9].dynBal.medium.p = enthalpyExchanger.airDuct1.vol[9].dynBal.p_start; + end if; + else + if (enthalpyExchanger.airDuct1.vol[9].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then + if (enthalpyExchanger.airDuct1.vol[9].dynBal.initialize_p) then + der(enthalpyExchanger.airDuct1.vol[9].dynBal.medium.p) = 0; + end if; + end if; + end if; + if (enthalpyExchanger.airDuct1.vol[10].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (enthalpyExchanger.airDuct1.vol[10].dynBal.initialize_p) then + enthalpyExchanger.airDuct1.vol[10].dynBal.medium.p = enthalpyExchanger.airDuct1.vol[10].dynBal.p_start; + end if; + else + if (enthalpyExchanger.airDuct1.vol[10].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then + if (enthalpyExchanger.airDuct1.vol[10].dynBal.initialize_p) then + der(enthalpyExchanger.airDuct1.vol[10].dynBal.medium.p) = 0; + end if; + end if; + end if; + if (enthalpyExchanger.airDuct1.vol[11].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (enthalpyExchanger.airDuct1.vol[11].dynBal.initialize_p) then + enthalpyExchanger.airDuct1.vol[11].dynBal.medium.p = enthalpyExchanger.airDuct1.vol[11].dynBal.p_start; + end if; + else + if (enthalpyExchanger.airDuct1.vol[11].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then + if (enthalpyExchanger.airDuct1.vol[11].dynBal.initialize_p) then + der(enthalpyExchanger.airDuct1.vol[11].dynBal.medium.p) = 0; + end if; + end if; + end if; + if (enthalpyExchanger.airDuct1.vol[12].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (enthalpyExchanger.airDuct1.vol[12].dynBal.initialize_p) then + enthalpyExchanger.airDuct1.vol[12].dynBal.medium.p = enthalpyExchanger.airDuct1.vol[12].dynBal.p_start; + end if; + else + if (enthalpyExchanger.airDuct1.vol[12].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then + if (enthalpyExchanger.airDuct1.vol[12].dynBal.initialize_p) then + der(enthalpyExchanger.airDuct1.vol[12].dynBal.medium.p) = 0; + end if; + end if; + end if; + if (enthalpyExchanger.airDuct1.vol[13].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (enthalpyExchanger.airDuct1.vol[13].dynBal.initialize_p) then + enthalpyExchanger.airDuct1.vol[13].dynBal.medium.p = enthalpyExchanger.airDuct1.vol[13].dynBal.p_start; + end if; + else + if (enthalpyExchanger.airDuct1.vol[13].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then + if (enthalpyExchanger.airDuct1.vol[13].dynBal.initialize_p) then + der(enthalpyExchanger.airDuct1.vol[13].dynBal.medium.p) = 0; + end if; + end if; + end if; + if (enthalpyExchanger.airDuct1.vol[14].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (enthalpyExchanger.airDuct1.vol[14].dynBal.initialize_p) then + enthalpyExchanger.airDuct1.vol[14].dynBal.medium.p = enthalpyExchanger.airDuct1.vol[14].dynBal.p_start; + end if; + else + if (enthalpyExchanger.airDuct1.vol[14].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then + if (enthalpyExchanger.airDuct1.vol[14].dynBal.initialize_p) then + der(enthalpyExchanger.airDuct1.vol[14].dynBal.medium.p) = 0; + end if; + end if; + end if; + if (enthalpyExchanger.airDuct1.vol[15].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (enthalpyExchanger.airDuct1.vol[15].dynBal.initialize_p) then + enthalpyExchanger.airDuct1.vol[15].dynBal.medium.p = enthalpyExchanger.airDuct1.vol[15].dynBal.p_start; + end if; + else + if (enthalpyExchanger.airDuct1.vol[15].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then + if (enthalpyExchanger.airDuct1.vol[15].dynBal.initialize_p) then + der(enthalpyExchanger.airDuct1.vol[15].dynBal.medium.p) = 0; + end if; + end if; + end if; + if (fan.vol.dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.FixedInitial) then + if (fan.vol.dynBal.initialize_p) then + fan.vol.dynBal.medium.p = fan.vol.dynBal.p_start; + end if; + else + if (fan.vol.dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. SteadyStateInitial) then + if (fan.vol.dynBal.initialize_p) then + der(fan.vol.dynBal.medium.p) = 0; + end if; + end if; + end if; + +This required evaluation of +the interactive parameters + fan.p_start(start = 101325) + fan1.p_start(start = 101325) + sinEha.p(start = 101325) + sinSup.p(start = 101325) + souEta.p(start = 101325) + souOda.p(start = 101325) + +The redundancies involve +initial equations: + enthalpyExchanger.airDuct2.vol[1].dynBal.medium.p = 101325.0; + enthalpyExchanger.airDuct2.vol[2].dynBal.medium.p = 101325.0; + enthalpyExchanger.airDuct2.vol[3].dynBal.medium.p = 101325.0; + enthalpyExchanger.airDuct2.vol[4].dynBal.medium.p = 101325.0; + enthalpyExchanger.airDuct2.vol[5].dynBal.medium.p = 101325.0; + enthalpyExchanger.airDuct2.vol[6].dynBal.medium.p = 101325.0; + enthalpyExchanger.airDuct2.vol[7].dynBal.medium.p = 101325.0; + enthalpyExchanger.airDuct2.vol[8].dynBal.medium.p = 101325.0; + enthalpyExchanger.airDuct2.vol[9].dynBal.medium.p = 101325.0; + enthalpyExchanger.airDuct2.vol[10].dynBal.medium.p = 101325.0; + enthalpyExchanger.airDuct2.vol[11].dynBal.medium.p = 101325.0; + enthalpyExchanger.airDuct2.vol[12].dynBal.medium.p = 101325.0; + enthalpyExchanger.airDuct2.vol[13].dynBal.medium.p = 101325.0; + enthalpyExchanger.airDuct2.vol[14].dynBal.medium.p = 101325.0; + enthalpyExchanger.airDuct2.vol[15].dynBal.medium.p = 101325.0; + enthalpyExchanger.airDuct1.vol[1].dynBal.medium.p = 101325.0; + enthalpyExchanger.airDuct1.vol[2].dynBal.medium.p = 101325.0; + enthalpyExchanger.airDuct1.vol[3].dynBal.medium.p = 101325.0; + enthalpyExchanger.airDuct1.vol[4].dynBal.medium.p = 101325.0; + enthalpyExchanger.airDuct1.vol[5].dynBal.medium.p = 101325.0; + enthalpyExchanger.airDuct1.vol[6].dynBal.medium.p = 101325.0; + enthalpyExchanger.airDuct1.vol[7].dynBal.medium.p = 101325.0; + enthalpyExchanger.airDuct1.vol[8].dynBal.medium.p = 101325.0; + enthalpyExchanger.airDuct1.vol[9].dynBal.medium.p = 101325.0; + enthalpyExchanger.airDuct1.vol[10].dynBal.medium.p = 101325.0; + enthalpyExchanger.airDuct1.vol[11].dynBal.medium.p = 101325.0; + enthalpyExchanger.airDuct1.vol[12].dynBal.medium.p = 101325.0; + enthalpyExchanger.airDuct1.vol[13].dynBal.medium.p = 101325.0; + enthalpyExchanger.airDuct1.vol[14].dynBal.medium.p = 101325.0; + enthalpyExchanger.airDuct1.vol[15].dynBal.medium.p = 101325.0; + fan.vol.dynBal.medium.p = fan.vol.dynBal.p_start; + fan1.vol.dynBal.medium.p = fan1.vol.dynBal.p_start; + + +Statistics + +Original Model + Number of components: 676 + Variables: 7282 + Constants: 168 (168 scalars) + Parameters: 2808 (3273 scalars) + Unknowns: 4306 (5679 scalars) + Differentiated variables: 129 scalars + Equations: 2961 + Nontrivial: 2303 +Translated Model + Constants: 2679 scalars + Free parameters: 252 scalars + Parameter depending: 1420 scalars + Continuous time states: 97 scalars + Time-varying variables: 1771 scalars + Alias variables: 2998 scalars + Number of mixed real/discrete systems of equations: 0 + Sizes of linear systems of equations: {2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 3, 3, 3, 3, 3, 3, 3, 3, 3, 3, 3, 3, 3, 3, 3} + Sizes after manipulation of the linear systems: {0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2} + Sizes of nonlinear systems of equations: {1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1} + Sizes after manipulation of the nonlinear systems: {0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0} + Number of numerical Jacobians: 0 + Initialization problem + Sizes of nonlinear systems of equations: {1, 1} + Sizes after manipulation of the nonlinear systems: {0, 0} + Number of numerical Jacobians: 0 + +Selected continuous time states +Statically selected continuous time states +conPID.I.y +conPID1.I.y +enthalpyExchanger.airDuct1.senRelHum.phi +enthalpyExchanger.airDuct1.senTem.T +enthalpyExchanger.airDuct1.vol[1].dynBal.medium.Xi[1] +enthalpyExchanger.airDuct1.vol[1].dynBal.U +enthalpyExchanger.airDuct1.vol[2].dynBal.medium.Xi[1] +enthalpyExchanger.airDuct1.vol[2].dynBal.U +enthalpyExchanger.airDuct1.vol[3].dynBal.medium.Xi[1] +enthalpyExchanger.airDuct1.vol[3].dynBal.U +enthalpyExchanger.airDuct1.vol[4].dynBal.medium.Xi[1] +enthalpyExchanger.airDuct1.vol[4].dynBal.U +enthalpyExchanger.airDuct1.vol[5].dynBal.medium.Xi[1] +enthalpyExchanger.airDuct1.vol[5].dynBal.U +enthalpyExchanger.airDuct1.vol[6].dynBal.medium.Xi[1] +enthalpyExchanger.airDuct1.vol[6].dynBal.U +enthalpyExchanger.airDuct1.vol[7].dynBal.medium.Xi[1] +enthalpyExchanger.airDuct1.vol[7].dynBal.U +enthalpyExchanger.airDuct1.vol[8].dynBal.medium.Xi[1] +enthalpyExchanger.airDuct1.vol[8].dynBal.U +enthalpyExchanger.airDuct1.vol[9].dynBal.medium.Xi[1] +enthalpyExchanger.airDuct1.vol[9].dynBal.U +enthalpyExchanger.airDuct1.vol[10].dynBal.medium.Xi[1] +enthalpyExchanger.airDuct1.vol[10].dynBal.U +enthalpyExchanger.airDuct1.vol[11].dynBal.medium.Xi[1] +enthalpyExchanger.airDuct1.vol[11].dynBal.U +enthalpyExchanger.airDuct1.vol[12].dynBal.medium.Xi[1] +enthalpyExchanger.airDuct1.vol[12].dynBal.U +enthalpyExchanger.airDuct1.vol[13].dynBal.medium.Xi[1] +enthalpyExchanger.airDuct1.vol[13].dynBal.U +enthalpyExchanger.airDuct1.vol[14].dynBal.medium.Xi[1] +enthalpyExchanger.airDuct1.vol[14].dynBal.U +enthalpyExchanger.airDuct1.vol[15].dynBal.medium.Xi[1] +enthalpyExchanger.airDuct1.vol[15].dynBal.U +enthalpyExchanger.airDuct2.senRelHum.phi +enthalpyExchanger.airDuct2.senTem.T +enthalpyExchanger.airDuct2.vol[1].dynBal.medium.Xi[1] +enthalpyExchanger.airDuct2.vol[1].dynBal.U +enthalpyExchanger.airDuct2.vol[2].dynBal.medium.Xi[1] +enthalpyExchanger.airDuct2.vol[2].dynBal.U +enthalpyExchanger.airDuct2.vol[3].dynBal.medium.Xi[1] +enthalpyExchanger.airDuct2.vol[3].dynBal.U +enthalpyExchanger.airDuct2.vol[4].dynBal.medium.Xi[1] +enthalpyExchanger.airDuct2.vol[4].dynBal.U +enthalpyExchanger.airDuct2.vol[5].dynBal.medium.Xi[1] +enthalpyExchanger.airDuct2.vol[5].dynBal.U +enthalpyExchanger.airDuct2.vol[6].dynBal.medium.Xi[1] +enthalpyExchanger.airDuct2.vol[6].dynBal.U +enthalpyExchanger.airDuct2.vol[7].dynBal.medium.Xi[1] +enthalpyExchanger.airDuct2.vol[7].dynBal.U +enthalpyExchanger.airDuct2.vol[8].dynBal.medium.Xi[1] +enthalpyExchanger.airDuct2.vol[8].dynBal.U +enthalpyExchanger.airDuct2.vol[9].dynBal.medium.Xi[1] +enthalpyExchanger.airDuct2.vol[9].dynBal.U +enthalpyExchanger.airDuct2.vol[10].dynBal.medium.Xi[1] +enthalpyExchanger.airDuct2.vol[10].dynBal.U +enthalpyExchanger.airDuct2.vol[11].dynBal.medium.Xi[1] +enthalpyExchanger.airDuct2.vol[11].dynBal.U +enthalpyExchanger.airDuct2.vol[12].dynBal.medium.Xi[1] +enthalpyExchanger.airDuct2.vol[12].dynBal.U +enthalpyExchanger.airDuct2.vol[13].dynBal.medium.Xi[1] +enthalpyExchanger.airDuct2.vol[13].dynBal.U +enthalpyExchanger.airDuct2.vol[14].dynBal.medium.Xi[1] +enthalpyExchanger.airDuct2.vol[14].dynBal.U +enthalpyExchanger.airDuct2.vol[15].dynBal.medium.Xi[1] +enthalpyExchanger.airDuct2.vol[15].dynBal.U +enthalpyExchanger.membrane.heatTransfer.Ts[1] +enthalpyExchanger.membrane.heatTransfer.Ts[2] +enthalpyExchanger.membrane.heatTransfer.Ts[3] +enthalpyExchanger.membrane.heatTransfer.Ts[4] +enthalpyExchanger.membrane.heatTransfer.Ts[5] +enthalpyExchanger.membrane.heatTransfer.Ts[6] +enthalpyExchanger.membrane.heatTransfer.Ts[7] +enthalpyExchanger.membrane.heatTransfer.Ts[8] +enthalpyExchanger.membrane.heatTransfer.Ts[9] +enthalpyExchanger.membrane.heatTransfer.Ts[10] +enthalpyExchanger.membrane.heatTransfer.Ts[11] +enthalpyExchanger.membrane.heatTransfer.Ts[12] +enthalpyExchanger.membrane.heatTransfer.Ts[13] +enthalpyExchanger.membrane.heatTransfer.Ts[14] +enthalpyExchanger.membrane.heatTransfer.Ts[15] +fan.filter.s[1] +fan.filter.s[2] +fan.vol.dynBal.medium.Xi[1] +fan.vol.dynBal.U +fan1.filter.s[1] +fan1.filter.s[2] +fan1.vol.dynBal.medium.Xi[1] +fan1.vol.dynBal.U +senMasFraEha.X +senMasFraEta.X +senMasFraOda.X +senMasFraSup.X +senTemEha.T +senTemEta.T +senTemOda.T +senTemSup.T +Finished +Finished + = true + +Declaring variable: Boolean rScript ; + +savelog("AixLib.Fluid.MassExchangers.MembraneBasedEnthalpyExchangers.Validation.StaticValidation.translation.log"); = true + + +rCheck = checkModel("AixLib.Fluid.BoilerCHP.Examples.BoilerGeneric"); +Check of AixLib.Fluid.BoilerCHP.Examples.BoilerGeneric +The model has the same number of unknowns and equations: 281 +The model could not be deduced to be symbolically well-posed. +The model has + 255+boiGen.vol.dynBal.nPorts+2*boiGen.offDesignOperation.multiplex4.n1+2* boiGen.offDesignOperation.multiplex4.n2+2*boiGen.offDesignOperation.multiplex4.n3 +2*boiGen.offDesignOperation.multiplex4.n4+boiGen.offDesignOperation.boilerEffciency.nin +2*boiGen.designOperation.multiplex4.n1+2*boiGen.designOperation.multiplex4.n2 +2*boiGen.designOperation.multiplex4.n3+2*boiGen.designOperation.multiplex4.n4 +boiGen.designOperation.boilerEffciency.nin +scalar unknowns and + 246+2*(boiGen.offDesignOperation.multiplex4.n1+boiGen.offDesignOperation.multiplex4.n2 +boiGen.offDesignOperation.multiplex4.n3+boiGen.offDesignOperation.multiplex4.n4 +boiGen.designOperation.multiplex4.n1+boiGen.designOperation.multiplex4.n2+ boiGen.designOperation.multiplex4.n3+boiGen.designOperation.multiplex4.n4+ source.nPorts)+(if not source.use_m_flow_in then 1 else 0)+(if not source.use_T_in then 1 else 0)+(if not source.use_X_in then 1 else 0)+2* sink.nPorts+(if not sink.use_p_in then 1 else 0)+(if not sink.use_T_in then 1 else 0)+(if not sink.use_X_in then 1 else 0)+(if conPID.reset <> AixLib.Types.Reset.Input then 1 else 0)+(if not boiGen.vol.dynBal.use_mWat_flow then 1 else 0)+3*boiGen.vol.dynBal.nPorts+(if (if conPID.reset == AixLib.Types.Reset.Disabled then conPID.reset else AixLib.Types.Reset.Input) <> AixLib.Types.Reset.Input then 1 else 0)+(if (if conPID.reset == AixLib.Types.Reset.Disabled then conPID.reset else AixLib.Types.Reset.Input) == AixLib.Types.Reset.Disabled then 1 else 0) +scalar equations. +However, exploiting the given numerical settings of parameters gives the same number of unknowns and equations: + 281 +Check of AixLib.Fluid.BoilerCHP.Examples.BoilerGeneric successful. +Declaring variable: Boolean rCheck ; + +Modelica.Utilities.Streams.print(" { \"file\" : \"AixLib/Resources/Scripts/Dymola/Fluid/BoilerCHP/Examples/BoilerGeneric.mos\",", "AixLib.Fluid.BoilerCHP.Examples.BoilerGeneric.statistics.log"); +Modelica.Utilities.Streams.print(" \"model\" : \"AixLib.Fluid.BoilerCHP.Examples.BoilerGeneric\",", "AixLib.Fluid.BoilerCHP.Examples.BoilerGeneric.statistics.log"); +Modelica.Utilities.Streams.print(" \"check\" : {", "AixLib.Fluid.BoilerCHP.Examples.BoilerGeneric.statistics.log"); +Modelica.Utilities.Streams.print(" \"command\" : \"checkModel(\\\"AixLib.Fluid.BoilerCHP.Examples.BoilerGeneric\\\");\",", "AixLib.Fluid.BoilerCHP.Examples.BoilerGeneric.statistics.log"); +Modelica.Utilities.Streams.print(" \"result\" : " + String(rCheck), "AixLib.Fluid.BoilerCHP.Examples.BoilerGeneric.statistics.log"); +Modelica.Utilities.Streams.print(" },", "AixLib.Fluid.BoilerCHP.Examples.BoilerGeneric.statistics.log"); + + +rScript=RunScript("modelica://AixLib/Resources/Scripts/Dymola/Fluid/BoilerCHP/Examples/BoilerGeneric.mos"); +simulateModel("AixLib.Fluid.BoilerCHP.Examples.BoilerGeneric", tolerance=1e-06, stopTime=1200, method="dassl", resultFile="AixLib.Fluid.BoilerCHP.Examples.BoilerGeneric"); +Translation of AixLib.Fluid.BoilerCHP.Examples.BoilerGeneric +The DAE has 281 scalar unknowns and 281 scalar equations. + +Statistics + +Original Model + Number of components: 69 + Variables: 558 + Constants: 6 (6 scalars) + Parameters: 250 (249 scalars) + Unknowns: 302 (285 scalars) + Differentiated variables: 6 scalars + Equations: 300 + Nontrivial: 247 +Translated Model + Constants: 166 scalars + Free parameters: 59 scalars + Parameter depending: 89 scalars + Outputs: 7 scalars + Continuous time states: 4 scalars + Time-varying variables: 44 scalars + Alias variables: 182 scalars + Number of mixed real/discrete systems of equations: 0 + Sizes of linear systems of equations: {5} + Sizes after manipulation of the linear systems: {0} + Sizes of nonlinear systems of equations: { } + Sizes after manipulation of the nonlinear systems: { } + Number of numerical Jacobians: 0 + +Selected continuous time states +Statically selected continuous time states +boiGen.internalCapacity.T +boiGen.senTRet.T +boiGen.senTSup.T +conPID.I.y +Finished +Finished + = true + +Declaring variable: Boolean rScript ; + +savelog("AixLib.Fluid.BoilerCHP.Examples.BoilerGeneric.translation.log"); = true + + +rCheck = checkModel("AixLib.Fluid.Pools.Examples.IndoorSwimmingPool"); +Check of AixLib.Fluid.Pools.Examples.IndoorSwimmingPool +The model has the same number of unknowns and equations: 677 +The model has the same number of unknowns and equations +for the given numerical settings of parameters: 677 +Check of AixLib.Fluid.Pools.Examples.IndoorSwimmingPool successful. +Declaring variable: Boolean rCheck ; + +Modelica.Utilities.Streams.print(" { \"file\" : \"AixLib/Resources/Scripts/Dymola/Fluid/Pools/Examples/IndoorSwimmingPool.mos\",", "AixLib.Fluid.Pools.Examples.IndoorSwimmingPool.statistics.log"); +Modelica.Utilities.Streams.print(" \"model\" : \"AixLib.Fluid.Pools.Examples.IndoorSwimmingPool\",", "AixLib.Fluid.Pools.Examples.IndoorSwimmingPool.statistics.log"); +Modelica.Utilities.Streams.print(" \"check\" : {", "AixLib.Fluid.Pools.Examples.IndoorSwimmingPool.statistics.log"); +Modelica.Utilities.Streams.print(" \"command\" : \"checkModel(\\\"AixLib.Fluid.Pools.Examples.IndoorSwimmingPool\\\");\",", "AixLib.Fluid.Pools.Examples.IndoorSwimmingPool.statistics.log"); +Modelica.Utilities.Streams.print(" \"result\" : " + String(rCheck), "AixLib.Fluid.Pools.Examples.IndoorSwimmingPool.statistics.log"); +Modelica.Utilities.Streams.print(" },", "AixLib.Fluid.Pools.Examples.IndoorSwimmingPool.statistics.log"); + + +rScript=RunScript("modelica://AixLib/Resources/Scripts/Dymola/Fluid/Pools/Examples/IndoorSwimmingPool.mos"); +simulateModel("AixLib.Fluid.Pools.Examples.IndoorSwimmingPool", tolerance=1e-6, stopTime=604800, numberOfIntervals=0, outputInterval=900, method="CVode", resultFile="AixLib.Fluid.Pools.Examples.IndoorSwimmingPool"); +Translation of AixLib.Fluid.Pools.Examples.IndoorSwimmingPool +The DAE has 677 scalar unknowns and 677 scalar equations. + +Statistics + +Original Model + Number of components: 161 + Variables: 1600 + Constants: 41 (41 scalars) + Parameters: 725 (917 scalars) + Unknowns: 834 (704 scalars) + Differentiated variables: 3 scalars + Equations: 700 + Nontrivial: 575 +Translated Model + Constants: 539 scalars + Free parameters: 126 scalars + Parameter depending: 408 scalars + Continuous time states: 3 scalars + Time-varying variables: 180 scalars + Alias variables: 409 scalars + Number of mixed real/discrete systems of equations: 1 + Sizes of linear systems of equations: {26} + Sizes after manipulation of the linear systems: {13} + Sizes of nonlinear systems of equations: {75, 1, 1} + Sizes after manipulation of the nonlinear systems: {16, 0, 1} + Number of numerical Jacobians: 0 + Initialization problem + Sizes of nonlinear systems of equations: {1, 74, 1} + Sizes after manipulation of the nonlinear systems: {1, 16, 1} + Number of numerical Jacobians: 0 + +Selected continuous time states +Statically selected continuous time states +indoorSwimming.cirPump.filter.s[1] +indoorSwimming.cirPump.filter.s[2] +indoorSwimming.PI.I.y +Finished +Finished + = true + +Declaring variable: Boolean rScript ; + +savelog("AixLib.Fluid.Pools.Examples.IndoorSwimmingPool.translation.log"); = true + + +rCheck = checkModel("AixLib.Fluid.Movers.PumpsPolynomialBased.Examples.PumpHeadControlled"); +Check of AixLib.Fluid.Movers.PumpsPolynomialBased.Examples.PumpHeadControlled +The model has the same number of unknowns and equations: 151 +The model could not be deduced to be symbolically well-posed. +The model has + 140+2*(size(pump.maxMinTable.columns, 1)+pump.deMultiplex3_1.n1+pump.deMultiplex3_1.n2) +pump.criticalDamping.n+pump.vol.dynBal.nPorts +scalar unknowns and + 130+2*size(pump.maxMinTable.columns, 1)+pump.deMultiplex3_1.n1+pump.deMultiplex3_1.n2 +pump.criticalDamping.n+(if vessle.use_Xi_in then 1 else (if vessle.use_X_in then 0 else 1))+(if not vessle.use_p_in then 1 else 0)+2*vessle.nPorts+(if not vessle.use_T_in then 1 else 0)+(if not pump.vol.dynBal.use_mWat_flow then 1 else 0)+3*pump.vol.dynBal.nPorts +scalar equations. +However, exploiting the given numerical settings of parameters gives the same number of unknowns and equations: + 151 +Check of AixLib.Fluid.Movers.PumpsPolynomialBased.Examples.PumpHeadControlled successful. +Declaring variable: Boolean rCheck ; + +Modelica.Utilities.Streams.print(" { \"file\" : \"AixLib/Resources/Scripts/Dymola/Fluid/Movers/PumpsPolynomialBased/Examples/PumpHeadControlled.mos\",", "AixLib.Fluid.Movers.PumpsPolynomialBased.Examples.PumpHeadControlled.statistics.log"); +Modelica.Utilities.Streams.print(" \"model\" : \"AixLib.Fluid.Movers.PumpsPolynomialBased.Examples.PumpHeadControlled\",", "AixLib.Fluid.Movers.PumpsPolynomialBased.Examples.PumpHeadControlled.statistics.log"); +Modelica.Utilities.Streams.print(" \"check\" : {", "AixLib.Fluid.Movers.PumpsPolynomialBased.Examples.PumpHeadControlled.statistics.log"); +Modelica.Utilities.Streams.print(" \"command\" : \"checkModel(\\\"AixLib.Fluid.Movers.PumpsPolynomialBased.Examples.PumpHeadControlled\\\");\",", "AixLib.Fluid.Movers.PumpsPolynomialBased.Examples.PumpHeadControlled.statistics.log"); +Modelica.Utilities.Streams.print(" \"result\" : " + String(rCheck), "AixLib.Fluid.Movers.PumpsPolynomialBased.Examples.PumpHeadControlled.statistics.log"); +Modelica.Utilities.Streams.print(" },", "AixLib.Fluid.Movers.PumpsPolynomialBased.Examples.PumpHeadControlled.statistics.log"); + + +rScript=RunScript("modelica://AixLib/Resources/Scripts/Dymola/Fluid/Movers/PumpsPolynomialBased/Examples/PumpHeadControlled.mos"); +simulateModel("AixLib.Fluid.Movers.PumpsPolynomialBased.Examples.PumpHeadControlled", tolerance=1e-6, stopTime=600, method="dassl", resultFile="AixLib.Fluid.Movers.PumpsPolynomialBased.Examples.PumpHeadControlled"); +Translation of AixLib.Fluid.Movers.PumpsPolynomialBased.Examples.PumpHeadControlled +The DAE has 151 scalar unknowns and 151 scalar equations. + +Statistics + +Original Model + Number of components: 34 + Variables: 378 + Constants: 9 (9 scalars) + Parameters: 177 (481 scalars) + Unknowns: 192 (155 scalars) + Differentiated variables: 5 scalars + Equations: 158 + Nontrivial: 131 +Translated Model + Constants: 127 scalars + Free parameters: 262 scalars + Parameter depending: 127 scalars + Outputs: 7 scalars + Continuous time states: 3 scalars + Time-varying variables: 36 scalars + Alias variables: 93 scalars + Number of mixed real/discrete systems of equations: 0 + Sizes of linear systems of equations: { } + Sizes after manipulation of the linear systems: { } + Sizes of nonlinear systems of equations: {1} + Sizes after manipulation of the nonlinear systems: {0} + Number of numerical Jacobians: 0 + Initialization problem + Sizes of nonlinear systems of equations: {1} + Sizes after manipulation of the nonlinear systems: {1} + Number of numerical Jacobians: 0 + +Selected continuous time states +Statically selected continuous time states +pump.criticalDamping.x[1] +simpleValve.filter.s[1] +simpleValve.filter.s[2] +Finished +Finished + = true + +Declaring variable: Boolean rScript ; + +savelog("AixLib.Fluid.Movers.PumpsPolynomialBased.Examples.PumpHeadControlled.translation.log"); = true + + +rCheck = checkModel("AixLib.Fluid.BoilerCHP.Examples.CHPSystem"); +Check of AixLib.Fluid.BoilerCHP.Examples.CHPSystem +The model has the same number of unknowns and equations: 367 +The model could not be deduced to be symbolically well-posed. +The model has + 361+combinedHeatPower.vol.dynBal.nPorts+size(combinedHeatPower.combiTable1Ds.columns, 1) +scalar unknowns and + 347+size(combinedHeatPower.combiTable1Ds.columns, 1)+2*source.nPorts+(if not source.use_m_flow_in then 1 else 0)+(if not source.use_T_in then 1 else 0)+( if not source.use_X_in then 1 else 0)+2*sink.nPorts+(if not sink.use_p_in then 1 else 0)+(if not sink.use_T_in then 1 else 0)+(if not sink.use_X_in then 1 else 0)+(if not combinedHeatPower.vol.dynBal.use_mWat_flow then 1 else 0)+3*combinedHeatPower.vol.dynBal.nPorts +scalar equations. +However, exploiting the given numerical settings of parameters gives the same number of unknowns and equations: + 367 +Check of AixLib.Fluid.BoilerCHP.Examples.CHPSystem successful. +Declaring variable: Boolean rCheck ; + +Modelica.Utilities.Streams.print(" { \"file\" : \"AixLib/Resources/Scripts/Dymola/Fluid/BoilerCHP/Examples/CHPSystem.mos\",", "AixLib.Fluid.BoilerCHP.Examples.CHPSystem.statistics.log"); +Modelica.Utilities.Streams.print(" \"model\" : \"AixLib.Fluid.BoilerCHP.Examples.CHPSystem\",", "AixLib.Fluid.BoilerCHP.Examples.CHPSystem.statistics.log"); +Modelica.Utilities.Streams.print(" \"check\" : {", "AixLib.Fluid.BoilerCHP.Examples.CHPSystem.statistics.log"); +Modelica.Utilities.Streams.print(" \"command\" : \"checkModel(\\\"AixLib.Fluid.BoilerCHP.Examples.CHPSystem\\\");\",", "AixLib.Fluid.BoilerCHP.Examples.CHPSystem.statistics.log"); +Modelica.Utilities.Streams.print(" \"result\" : " + String(rCheck), "AixLib.Fluid.BoilerCHP.Examples.CHPSystem.statistics.log"); +Modelica.Utilities.Streams.print(" },", "AixLib.Fluid.BoilerCHP.Examples.CHPSystem.statistics.log"); + + +rScript=RunScript("modelica://AixLib/Resources/Scripts/Dymola/Fluid/BoilerCHP/Examples/CHPSystem.mos"); +simulateModel("AixLib.Fluid.BoilerCHP.Examples.CHPSystem", tolerance=1e-06, stopTime=1200, method="dassl", resultFile="AixLib.Fluid.BoilerCHP.Examples.CHPSystem"); +Translation of AixLib.Fluid.BoilerCHP.Examples.CHPSystem +The DAE has 367 scalar unknowns and 367 scalar equations. + +Statistics + +Original Model + Number of components: 105 + Variables: 786 + Constants: 8 (8 scalars) + Parameters: 360 (394 scalars) + Unknowns: 418 (371 scalars) + Differentiated variables: 8 scalars + Equations: 404 + Nontrivial: 360 +Translated Model + Constants: 177 scalars + Free parameters: 143 scalars + Parameter depending: 115 scalars + Continuous time states: 6 scalars + Time-varying variables: 112 scalars + Alias variables: 226 scalars + Number of mixed real/discrete systems of equations: 0 + Sizes of linear systems of equations: { } + Sizes after manipulation of the linear systems: { } + Sizes of nonlinear systems of equations: {8, 9} + Sizes after manipulation of the nonlinear systems: {1, 1} + Number of numerical Jacobians: 0 + Initialization problem + Sizes of linear systems of equations: {5} + Sizes after manipulation of the linear systems: {0} + +Selected continuous time states +Statically selected continuous time states +combinedHeatPower.elControl.I.y +combinedHeatPower.senTRet.T +combinedHeatPower.senTSup.T +combinedHeatPower.thControl.PI.I.y +combinedHeatPower.thControl.PI1.I.y +combinedHeatPower.vol.dynBal.medium.T +Finished +Finished + = true + +Declaring variable: Boolean rScript ; + +savelog("AixLib.Fluid.BoilerCHP.Examples.CHPSystem.translation.log"); = true + + +rCheck = checkModel("AixLib.Fluid.MassExchangers.MembraneBasedEnthalpyExchangers.Validation.DynamicValidation"); +Check of AixLib.Fluid.MassExchangers.MembraneBasedEnthalpyExchangers.Validation.DynamicValidation +The model has the same number of unknowns and equations: 5514 +The model could not be deduced to be symbolically well-posed. +The model has + 3787+32*enthalpyExchanger.n+16*enthalpyExchanger.airDuct2.heatTransfer.n+18* enthalpyExchanger.airDuct2.massTransfer.n+16*enthalpyExchanger.airDuct1.heatTransfer.n +18*enthalpyExchanger.airDuct1.massTransfer.n+5*enthalpyExchanger.membrane.heatTransfer.n +enthalpyExchanger.membrane.massTransfer.n+2*enthalpyExchanger.airDuct2.vol[1].dynBal.nPorts +2*enthalpyExchanger.airDuct2.vol[2].dynBal.nPorts+2*enthalpyExchanger.airDuct2.vol[3].dynBal.nPorts +2*enthalpyExchanger.airDuct2.vol[4].dynBal.nPorts+2*enthalpyExchanger.airDuct2.vol[5].dynBal.nPorts +2*enthalpyExchanger.airDuct2.vol[6].dynBal.nPorts+2*enthalpyExchanger.airDuct2.vol[7].dynBal.nPorts +2*enthalpyExchanger.airDuct2.vol[8].dynBal.nPorts+2*enthalpyExchanger.airDuct2.vol[9].dynBal.nPorts +2*enthalpyExchanger.airDuct2.vol[10].dynBal.nPorts+2*enthalpyExchanger.airDuct2.vol[11].dynBal.nPorts +2*enthalpyExchanger.airDuct2.vol[12].dynBal.nPorts+2*enthalpyExchanger.airDuct2.vol[13].dynBal.nPorts +2*enthalpyExchanger.airDuct2.vol[14].dynBal.nPorts+2*enthalpyExchanger.airDuct2.vol[15].dynBal.nPorts +2*enthalpyExchanger.airDuct1.vol[1].dynBal.nPorts+2*enthalpyExchanger.airDuct1.vol[2].dynBal.nPorts +2*enthalpyExchanger.airDuct1.vol[3].dynBal.nPorts+2*enthalpyExchanger.airDuct1.vol[4].dynBal.nPorts +2*enthalpyExchanger.airDuct1.vol[5].dynBal.nPorts+2*enthalpyExchanger.airDuct1.vol[6].dynBal.nPorts +2*enthalpyExchanger.airDuct1.vol[7].dynBal.nPorts+2*enthalpyExchanger.airDuct1.vol[8].dynBal.nPorts +2*enthalpyExchanger.airDuct1.vol[9].dynBal.nPorts+2*enthalpyExchanger.airDuct1.vol[10].dynBal.nPorts +2*enthalpyExchanger.airDuct1.vol[11].dynBal.nPorts+2*enthalpyExchanger.airDuct1.vol[12].dynBal.nPorts +2*enthalpyExchanger.airDuct1.vol[13].dynBal.nPorts+2*enthalpyExchanger.airDuct1.vol[14].dynBal.nPorts +2*enthalpyExchanger.airDuct1.vol[15].dynBal.nPorts+max([size(bondaryEta.columns, 1); size(bondaryEta.offset, 1)])+max([size(bondaryOda.columns, 1); size( bondaryOda.offset, 1)])+max([size(Results.columns, 1); size(Results.offset, 1)]) +2*fan.vol.dynBal.nPorts+2*fan1.vol.dynBal.nPorts +scalar unknowns and + 3439+17*enthalpyExchanger.airDuct2.heatTransfer.n+19*enthalpyExchanger.airDuct2.massTransfer.n +3*(if enthalpyExchanger.couFloArr then 2*enthalpyExchanger.n else 0)+17* enthalpyExchanger.airDuct1.heatTransfer.n+19*enthalpyExchanger.airDuct1.massTransfer.n +7*enthalpyExchanger.membrane.heatTransfer.n+3*enthalpyExchanger.membrane.massTransfer.n +2*(if enthalpyExchanger.useConPer then 1 else 0)+32*enthalpyExchanger.n+(if souEta.use_Xi_in then 2 else (if souEta.use_X_in then 1 else 3))+3* souEta.nPorts+(if not souEta.use_p_in then 1 else 0)+(if not souEta.use_T_in then 1 else 0)+(if sinEha.use_Xi_in then 2 else (if sinEha.use_X_in then 1 else 3))+3*sinEha.nPorts+(if not sinEha.use_p_in then 1 else 0)+(if not sinEha.use_T_in then 1 else 0)+(if souOda.use_Xi_in then 2 else (if souOda.use_X_in then 1 else 3))+3*souOda.nPorts+(if not souOda.use_p_in then 1 else 0)+(if not souOda.use_T_in then 1 else 0)+(if sinSup.use_Xi_in then 2 else (if sinSup.use_X_in then 1 else 3))+3*sinSup.nPorts+(if not sinSup.use_p_in then 1 else 0)+(if not sinSup.use_T_in then 1 else 0)+max([ size(bondaryEta.columns, 1); size(bondaryEta.offset, 1)])+max([size( bondaryOda.columns, 1); size(bondaryOda.offset, 1)])+max([size(Results.columns, 1); size(Results.offset, 1)])+(if conPID.reset <> AixLib.Types.Reset.Input then 1 else 0)+(if conPID1.reset <> AixLib.Types.Reset.Input then 1 else 0)+5 *enthalpyExchanger.airDuct2.vol[1].dynBal.nPorts+5*enthalpyExchanger.airDuct2.vol[2].dynBal.nPorts +5*enthalpyExchanger.airDuct2.vol[3].dynBal.nPorts+5*enthalpyExchanger.airDuct2.vol[4].dynBal.nPorts +5*enthalpyExchanger.airDuct2.vol[5].dynBal.nPorts+5*enthalpyExchanger.airDuct2.vol[6].dynBal.nPorts +5*enthalpyExchanger.airDuct2.vol[7].dynBal.nPorts+5*enthalpyExchanger.airDuct2.vol[8].dynBal.nPorts +5*enthalpyExchanger.airDuct2.vol[9].dynBal.nPorts+5*enthalpyExchanger.airDuct2.vol[10].dynBal.nPorts +5*enthalpyExchanger.airDuct2.vol[11].dynBal.nPorts+5*enthalpyExchanger.airDuct2.vol[12].dynBal.nPorts +5*enthalpyExchanger.airDuct2.vol[13].dynBal.nPorts+5*enthalpyExchanger.airDuct2.vol[14].dynBal.nPorts +5*enthalpyExchanger.airDuct2.vol[15].dynBal.nPorts+5*enthalpyExchanger.airDuct1.vol[1].dynBal.nPorts +5*enthalpyExchanger.airDuct1.vol[2].dynBal.nPorts+5*enthalpyExchanger.airDuct1.vol[3].dynBal.nPorts +5*enthalpyExchanger.airDuct1.vol[4].dynBal.nPorts+5*enthalpyExchanger.airDuct1.vol[5].dynBal.nPorts +5*enthalpyExchanger.airDuct1.vol[6].dynBal.nPorts+5*enthalpyExchanger.airDuct1.vol[7].dynBal.nPorts +5*enthalpyExchanger.airDuct1.vol[8].dynBal.nPorts+5*enthalpyExchanger.airDuct1.vol[9].dynBal.nPorts +5*enthalpyExchanger.airDuct1.vol[10].dynBal.nPorts+5*enthalpyExchanger.airDuct1.vol[11].dynBal.nPorts +5*enthalpyExchanger.airDuct1.vol[12].dynBal.nPorts+5*enthalpyExchanger.airDuct1.vol[13].dynBal.nPorts +5*enthalpyExchanger.airDuct1.vol[14].dynBal.nPorts+5*enthalpyExchanger.airDuct1.vol[15].dynBal.nPorts +(if not fan.vol.dynBal.use_mWat_flow then 1 else 0)+5*fan.vol.dynBal.nPorts+ (if (if conPID.reset == AixLib.Types.Reset.Disabled then conPID.reset else AixLib.Types.Reset.Input) <> AixLib.Types.Reset.Input then 1 else 0)+(if (if conPID.reset == AixLib.Types.Reset.Disabled then conPID.reset else AixLib.Types.Reset.Input) == AixLib.Types.Reset.Disabled then 1 else 0)+(if not fan1.vol.dynBal.use_mWat_flow then 1 else 0)+5*fan1.vol.dynBal.nPorts+( if (if conPID1.reset == AixLib.Types.Reset.Disabled then conPID1.reset else AixLib.Types.Reset.Input) <> AixLib.Types.Reset.Input then 1 else 0)+(if (if conPID1.reset == AixLib.Types.Reset.Disabled then conPID1.reset else AixLib.Types.Reset.Input) == AixLib.Types.Reset.Disabled then 1 else 0) +scalar equations. +However, exploiting the given numerical settings of parameters gives the same number of unknowns and equations: + 5514 +Check of AixLib.Fluid.MassExchangers.MembraneBasedEnthalpyExchangers.Validation.DynamicValidation successful. +Declaring variable: Boolean rCheck ; + +Modelica.Utilities.Streams.print(" { \"file\" : \"AixLib/Resources/Scripts/Dymola/Fluid/MassExchangers/MembraneBasedEnthalpyExchangers/Validation/DynamicValidation.mos\",", "AixLib.Fluid.MassExchangers.MembraneBasedEnthalpyExchangers.Validation.DynamicValidation.statistics.log"); +Modelica.Utilities.Streams.print(" \"model\" : \"AixLib.Fluid.MassExchangers.MembraneBasedEnthalpyExchangers.Validation.DynamicValidation\",", "AixLib.Fluid.MassExchangers.MembraneBasedEnthalpyExchangers.Validation.DynamicValidation.statistics.log"); +Modelica.Utilities.Streams.print(" \"check\" : {", "AixLib.Fluid.MassExchangers.MembraneBasedEnthalpyExchangers.Validation.DynamicValidation.statistics.log"); +Modelica.Utilities.Streams.print(" \"command\" : \"checkModel(\\\"AixLib.Fluid.MassExchangers.MembraneBasedEnthalpyExchangers.Validation.DynamicValidation\\\");\",", "AixLib.Fluid.MassExchangers.MembraneBasedEnthalpyExchangers.Validation.DynamicValidation.statistics.log"); +Modelica.Utilities.Streams.print(" \"result\" : " + String(rCheck), "AixLib.Fluid.MassExchangers.MembraneBasedEnthalpyExchangers.Validation.DynamicValidation.statistics.log"); +Modelica.Utilities.Streams.print(" },", "AixLib.Fluid.MassExchangers.MembraneBasedEnthalpyExchangers.Validation.DynamicValidation.statistics.log"); + + +rScript=RunScript("modelica://AixLib/Resources/Scripts/Dymola/Fluid/MassExchangers/MembraneBasedEnthalpyExchangers/Validation/DynamicValidation.mos"); +simulateModel("AixLib.Fluid.MassExchangers.MembraneBasedEnthalpyExchangers.Validation.DynamicValidation", stopTime=7200, numberOfIntervals=0, outputInterval=2, method="dassl",tolerance=1E-6, resultFile="AixLib.Fluid.MassExchangers.MembraneBasedEnthalpyExchangers.Validation.DynamicValidation"); +Translation of AixLib.Fluid.MassExchangers.MembraneBasedEnthalpyExchangers.Validation.DynamicValidation +The DAE has 5514 scalar unknowns and 5514 scalar equations. +Redundant consistent initial conditions. +Removed the following equations which are redundant and consistent: + fan1.vol.p_start = fan1.p_start; + if (enthalpyExchanger.airDuct2.vol[1].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (enthalpyExchanger.airDuct2.vol[1].dynBal.initialize_p) then + enthalpyExchanger.airDuct2.vol[1].dynBal.medium.p = enthalpyExchanger.airDuct2.vol[1].dynBal.p_start; + end if; + else + if (enthalpyExchanger.airDuct2.vol[1].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then + if (enthalpyExchanger.airDuct2.vol[1].dynBal.initialize_p) then + der(enthalpyExchanger.airDuct2.vol[1].dynBal.medium.p) = 0; + end if; + end if; + end if; + if (enthalpyExchanger.airDuct2.vol[2].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (enthalpyExchanger.airDuct2.vol[2].dynBal.initialize_p) then + enthalpyExchanger.airDuct2.vol[2].dynBal.medium.p = enthalpyExchanger.airDuct2.vol[2].dynBal.p_start; + end if; + else + if (enthalpyExchanger.airDuct2.vol[2].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then + if (enthalpyExchanger.airDuct2.vol[2].dynBal.initialize_p) then + der(enthalpyExchanger.airDuct2.vol[2].dynBal.medium.p) = 0; + end if; + end if; + end if; + if (enthalpyExchanger.airDuct2.vol[3].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (enthalpyExchanger.airDuct2.vol[3].dynBal.initialize_p) then + enthalpyExchanger.airDuct2.vol[3].dynBal.medium.p = enthalpyExchanger.airDuct2.vol[3].dynBal.p_start; + end if; + else + if (enthalpyExchanger.airDuct2.vol[3].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then + if (enthalpyExchanger.airDuct2.vol[3].dynBal.initialize_p) then + der(enthalpyExchanger.airDuct2.vol[3].dynBal.medium.p) = 0; + end if; + end if; + end if; + if (enthalpyExchanger.airDuct2.vol[4].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (enthalpyExchanger.airDuct2.vol[4].dynBal.initialize_p) then + enthalpyExchanger.airDuct2.vol[4].dynBal.medium.p = enthalpyExchanger.airDuct2.vol[4].dynBal.p_start; + end if; + else + if (enthalpyExchanger.airDuct2.vol[4].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then + if (enthalpyExchanger.airDuct2.vol[4].dynBal.initialize_p) then + der(enthalpyExchanger.airDuct2.vol[4].dynBal.medium.p) = 0; + end if; + end if; + end if; + if (enthalpyExchanger.airDuct2.vol[5].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (enthalpyExchanger.airDuct2.vol[5].dynBal.initialize_p) then + enthalpyExchanger.airDuct2.vol[5].dynBal.medium.p = enthalpyExchanger.airDuct2.vol[5].dynBal.p_start; + end if; + else + if (enthalpyExchanger.airDuct2.vol[5].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then + if (enthalpyExchanger.airDuct2.vol[5].dynBal.initialize_p) then + der(enthalpyExchanger.airDuct2.vol[5].dynBal.medium.p) = 0; + end if; + end if; + end if; + if (enthalpyExchanger.airDuct2.vol[6].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (enthalpyExchanger.airDuct2.vol[6].dynBal.initialize_p) then + enthalpyExchanger.airDuct2.vol[6].dynBal.medium.p = enthalpyExchanger.airDuct2.vol[6].dynBal.p_start; + end if; + else + if (enthalpyExchanger.airDuct2.vol[6].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then + if (enthalpyExchanger.airDuct2.vol[6].dynBal.initialize_p) then + der(enthalpyExchanger.airDuct2.vol[6].dynBal.medium.p) = 0; + end if; + end if; + end if; + if (enthalpyExchanger.airDuct2.vol[7].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (enthalpyExchanger.airDuct2.vol[7].dynBal.initialize_p) then + enthalpyExchanger.airDuct2.vol[7].dynBal.medium.p = enthalpyExchanger.airDuct2.vol[7].dynBal.p_start; + end if; + else + if (enthalpyExchanger.airDuct2.vol[7].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then + if (enthalpyExchanger.airDuct2.vol[7].dynBal.initialize_p) then + der(enthalpyExchanger.airDuct2.vol[7].dynBal.medium.p) = 0; + end if; + end if; + end if; + if (enthalpyExchanger.airDuct2.vol[8].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (enthalpyExchanger.airDuct2.vol[8].dynBal.initialize_p) then + enthalpyExchanger.airDuct2.vol[8].dynBal.medium.p = enthalpyExchanger.airDuct2.vol[8].dynBal.p_start; + end if; + else + if (enthalpyExchanger.airDuct2.vol[8].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then + if (enthalpyExchanger.airDuct2.vol[8].dynBal.initialize_p) then + der(enthalpyExchanger.airDuct2.vol[8].dynBal.medium.p) = 0; + end if; + end if; + end if; + if (enthalpyExchanger.airDuct2.vol[9].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (enthalpyExchanger.airDuct2.vol[9].dynBal.initialize_p) then + enthalpyExchanger.airDuct2.vol[9].dynBal.medium.p = enthalpyExchanger.airDuct2.vol[9].dynBal.p_start; + end if; + else + if (enthalpyExchanger.airDuct2.vol[9].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then + if (enthalpyExchanger.airDuct2.vol[9].dynBal.initialize_p) then + der(enthalpyExchanger.airDuct2.vol[9].dynBal.medium.p) = 0; + end if; + end if; + end if; + if (enthalpyExchanger.airDuct2.vol[10].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (enthalpyExchanger.airDuct2.vol[10].dynBal.initialize_p) then + enthalpyExchanger.airDuct2.vol[10].dynBal.medium.p = enthalpyExchanger.airDuct2.vol[10].dynBal.p_start; + end if; + else + if (enthalpyExchanger.airDuct2.vol[10].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then + if (enthalpyExchanger.airDuct2.vol[10].dynBal.initialize_p) then + der(enthalpyExchanger.airDuct2.vol[10].dynBal.medium.p) = 0; + end if; + end if; + end if; + if (enthalpyExchanger.airDuct2.vol[11].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (enthalpyExchanger.airDuct2.vol[11].dynBal.initialize_p) then + enthalpyExchanger.airDuct2.vol[11].dynBal.medium.p = enthalpyExchanger.airDuct2.vol[11].dynBal.p_start; + end if; + else + if (enthalpyExchanger.airDuct2.vol[11].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then + if (enthalpyExchanger.airDuct2.vol[11].dynBal.initialize_p) then + der(enthalpyExchanger.airDuct2.vol[11].dynBal.medium.p) = 0; + end if; + end if; + end if; + if (enthalpyExchanger.airDuct2.vol[12].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (enthalpyExchanger.airDuct2.vol[12].dynBal.initialize_p) then + enthalpyExchanger.airDuct2.vol[12].dynBal.medium.p = enthalpyExchanger.airDuct2.vol[12].dynBal.p_start; + end if; + else + if (enthalpyExchanger.airDuct2.vol[12].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then + if (enthalpyExchanger.airDuct2.vol[12].dynBal.initialize_p) then + der(enthalpyExchanger.airDuct2.vol[12].dynBal.medium.p) = 0; + end if; + end if; + end if; + if (enthalpyExchanger.airDuct2.vol[13].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (enthalpyExchanger.airDuct2.vol[13].dynBal.initialize_p) then + enthalpyExchanger.airDuct2.vol[13].dynBal.medium.p = enthalpyExchanger.airDuct2.vol[13].dynBal.p_start; + end if; + else + if (enthalpyExchanger.airDuct2.vol[13].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then + if (enthalpyExchanger.airDuct2.vol[13].dynBal.initialize_p) then + der(enthalpyExchanger.airDuct2.vol[13].dynBal.medium.p) = 0; + end if; + end if; + end if; + if (enthalpyExchanger.airDuct2.vol[14].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (enthalpyExchanger.airDuct2.vol[14].dynBal.initialize_p) then + enthalpyExchanger.airDuct2.vol[14].dynBal.medium.p = enthalpyExchanger.airDuct2.vol[14].dynBal.p_start; + end if; + else + if (enthalpyExchanger.airDuct2.vol[14].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then + if (enthalpyExchanger.airDuct2.vol[14].dynBal.initialize_p) then + der(enthalpyExchanger.airDuct2.vol[14].dynBal.medium.p) = 0; + end if; + end if; + end if; + if (enthalpyExchanger.airDuct2.vol[15].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (enthalpyExchanger.airDuct2.vol[15].dynBal.initialize_p) then + enthalpyExchanger.airDuct2.vol[15].dynBal.medium.p = enthalpyExchanger.airDuct2.vol[15].dynBal.p_start; + end if; + else + if (enthalpyExchanger.airDuct2.vol[15].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then + if (enthalpyExchanger.airDuct2.vol[15].dynBal.initialize_p) then + der(enthalpyExchanger.airDuct2.vol[15].dynBal.medium.p) = 0; + end if; + end if; + end if; + if (enthalpyExchanger.airDuct1.vol[1].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (enthalpyExchanger.airDuct1.vol[1].dynBal.initialize_p) then + enthalpyExchanger.airDuct1.vol[1].dynBal.medium.p = enthalpyExchanger.airDuct1.vol[1].dynBal.p_start; + end if; + else + if (enthalpyExchanger.airDuct1.vol[1].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then + if (enthalpyExchanger.airDuct1.vol[1].dynBal.initialize_p) then + der(enthalpyExchanger.airDuct1.vol[1].dynBal.medium.p) = 0; + end if; + end if; + end if; + if (enthalpyExchanger.airDuct1.vol[2].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (enthalpyExchanger.airDuct1.vol[2].dynBal.initialize_p) then + enthalpyExchanger.airDuct1.vol[2].dynBal.medium.p = enthalpyExchanger.airDuct1.vol[2].dynBal.p_start; + end if; + else + if (enthalpyExchanger.airDuct1.vol[2].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then + if (enthalpyExchanger.airDuct1.vol[2].dynBal.initialize_p) then + der(enthalpyExchanger.airDuct1.vol[2].dynBal.medium.p) = 0; + end if; + end if; + end if; + if (enthalpyExchanger.airDuct1.vol[3].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (enthalpyExchanger.airDuct1.vol[3].dynBal.initialize_p) then + enthalpyExchanger.airDuct1.vol[3].dynBal.medium.p = enthalpyExchanger.airDuct1.vol[3].dynBal.p_start; + end if; + else + if (enthalpyExchanger.airDuct1.vol[3].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then + if (enthalpyExchanger.airDuct1.vol[3].dynBal.initialize_p) then + der(enthalpyExchanger.airDuct1.vol[3].dynBal.medium.p) = 0; + end if; + end if; + end if; + if (enthalpyExchanger.airDuct1.vol[4].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (enthalpyExchanger.airDuct1.vol[4].dynBal.initialize_p) then + enthalpyExchanger.airDuct1.vol[4].dynBal.medium.p = enthalpyExchanger.airDuct1.vol[4].dynBal.p_start; + end if; + else + if (enthalpyExchanger.airDuct1.vol[4].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then + if (enthalpyExchanger.airDuct1.vol[4].dynBal.initialize_p) then + der(enthalpyExchanger.airDuct1.vol[4].dynBal.medium.p) = 0; + end if; + end if; + end if; + if (enthalpyExchanger.airDuct1.vol[5].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (enthalpyExchanger.airDuct1.vol[5].dynBal.initialize_p) then + enthalpyExchanger.airDuct1.vol[5].dynBal.medium.p = enthalpyExchanger.airDuct1.vol[5].dynBal.p_start; + end if; + else + if (enthalpyExchanger.airDuct1.vol[5].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then + if (enthalpyExchanger.airDuct1.vol[5].dynBal.initialize_p) then + der(enthalpyExchanger.airDuct1.vol[5].dynBal.medium.p) = 0; + end if; + end if; + end if; + if (enthalpyExchanger.airDuct1.vol[6].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (enthalpyExchanger.airDuct1.vol[6].dynBal.initialize_p) then + enthalpyExchanger.airDuct1.vol[6].dynBal.medium.p = enthalpyExchanger.airDuct1.vol[6].dynBal.p_start; + end if; + else + if (enthalpyExchanger.airDuct1.vol[6].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then + if (enthalpyExchanger.airDuct1.vol[6].dynBal.initialize_p) then + der(enthalpyExchanger.airDuct1.vol[6].dynBal.medium.p) = 0; + end if; + end if; + end if; + if (enthalpyExchanger.airDuct1.vol[7].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (enthalpyExchanger.airDuct1.vol[7].dynBal.initialize_p) then + enthalpyExchanger.airDuct1.vol[7].dynBal.medium.p = enthalpyExchanger.airDuct1.vol[7].dynBal.p_start; + end if; + else + if (enthalpyExchanger.airDuct1.vol[7].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then + if (enthalpyExchanger.airDuct1.vol[7].dynBal.initialize_p) then + der(enthalpyExchanger.airDuct1.vol[7].dynBal.medium.p) = 0; + end if; + end if; + end if; + if (enthalpyExchanger.airDuct1.vol[8].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (enthalpyExchanger.airDuct1.vol[8].dynBal.initialize_p) then + enthalpyExchanger.airDuct1.vol[8].dynBal.medium.p = enthalpyExchanger.airDuct1.vol[8].dynBal.p_start; + end if; + else + if (enthalpyExchanger.airDuct1.vol[8].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then + if (enthalpyExchanger.airDuct1.vol[8].dynBal.initialize_p) then + der(enthalpyExchanger.airDuct1.vol[8].dynBal.medium.p) = 0; + end if; + end if; + end if; + if (enthalpyExchanger.airDuct1.vol[9].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (enthalpyExchanger.airDuct1.vol[9].dynBal.initialize_p) then + enthalpyExchanger.airDuct1.vol[9].dynBal.medium.p = enthalpyExchanger.airDuct1.vol[9].dynBal.p_start; + end if; + else + if (enthalpyExchanger.airDuct1.vol[9].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then + if (enthalpyExchanger.airDuct1.vol[9].dynBal.initialize_p) then + der(enthalpyExchanger.airDuct1.vol[9].dynBal.medium.p) = 0; + end if; + end if; + end if; + if (enthalpyExchanger.airDuct1.vol[10].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (enthalpyExchanger.airDuct1.vol[10].dynBal.initialize_p) then + enthalpyExchanger.airDuct1.vol[10].dynBal.medium.p = enthalpyExchanger.airDuct1.vol[10].dynBal.p_start; + end if; + else + if (enthalpyExchanger.airDuct1.vol[10].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then + if (enthalpyExchanger.airDuct1.vol[10].dynBal.initialize_p) then + der(enthalpyExchanger.airDuct1.vol[10].dynBal.medium.p) = 0; + end if; + end if; + end if; + if (enthalpyExchanger.airDuct1.vol[11].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (enthalpyExchanger.airDuct1.vol[11].dynBal.initialize_p) then + enthalpyExchanger.airDuct1.vol[11].dynBal.medium.p = enthalpyExchanger.airDuct1.vol[11].dynBal.p_start; + end if; + else + if (enthalpyExchanger.airDuct1.vol[11].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then + if (enthalpyExchanger.airDuct1.vol[11].dynBal.initialize_p) then + der(enthalpyExchanger.airDuct1.vol[11].dynBal.medium.p) = 0; + end if; + end if; + end if; + if (enthalpyExchanger.airDuct1.vol[12].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (enthalpyExchanger.airDuct1.vol[12].dynBal.initialize_p) then + enthalpyExchanger.airDuct1.vol[12].dynBal.medium.p = enthalpyExchanger.airDuct1.vol[12].dynBal.p_start; + end if; + else + if (enthalpyExchanger.airDuct1.vol[12].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then + if (enthalpyExchanger.airDuct1.vol[12].dynBal.initialize_p) then + der(enthalpyExchanger.airDuct1.vol[12].dynBal.medium.p) = 0; + end if; + end if; + end if; + if (enthalpyExchanger.airDuct1.vol[13].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (enthalpyExchanger.airDuct1.vol[13].dynBal.initialize_p) then + enthalpyExchanger.airDuct1.vol[13].dynBal.medium.p = enthalpyExchanger.airDuct1.vol[13].dynBal.p_start; + end if; + else + if (enthalpyExchanger.airDuct1.vol[13].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then + if (enthalpyExchanger.airDuct1.vol[13].dynBal.initialize_p) then + der(enthalpyExchanger.airDuct1.vol[13].dynBal.medium.p) = 0; + end if; + end if; + end if; + if (enthalpyExchanger.airDuct1.vol[14].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (enthalpyExchanger.airDuct1.vol[14].dynBal.initialize_p) then + enthalpyExchanger.airDuct1.vol[14].dynBal.medium.p = enthalpyExchanger.airDuct1.vol[14].dynBal.p_start; + end if; + else + if (enthalpyExchanger.airDuct1.vol[14].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then + if (enthalpyExchanger.airDuct1.vol[14].dynBal.initialize_p) then + der(enthalpyExchanger.airDuct1.vol[14].dynBal.medium.p) = 0; + end if; + end if; + end if; + if (enthalpyExchanger.airDuct1.vol[15].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (enthalpyExchanger.airDuct1.vol[15].dynBal.initialize_p) then + enthalpyExchanger.airDuct1.vol[15].dynBal.medium.p = enthalpyExchanger.airDuct1.vol[15].dynBal.p_start; + end if; + else + if (enthalpyExchanger.airDuct1.vol[15].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then + if (enthalpyExchanger.airDuct1.vol[15].dynBal.initialize_p) then + der(enthalpyExchanger.airDuct1.vol[15].dynBal.medium.p) = 0; + end if; + end if; + end if; + if (fan.vol.dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.FixedInitial) then + if (fan.vol.dynBal.initialize_p) then + fan.vol.dynBal.medium.p = fan.vol.dynBal.p_start; + end if; + else + if (fan.vol.dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. SteadyStateInitial) then + if (fan.vol.dynBal.initialize_p) then + der(fan.vol.dynBal.medium.p) = 0; + end if; + end if; + end if; + +This required evaluation of +the interactive parameters + fan.p_start(start = 101325) + fan1.p_start(start = 101325) + sinEha.p(start = 101325) + sinSup.p(start = 101325) + souEta.p(start = 101325) + souOda.p(start = 101325) + +The redundancies involve +initial equations: + enthalpyExchanger.airDuct2.vol[1].dynBal.medium.p = 101325.0; + enthalpyExchanger.airDuct2.vol[2].dynBal.medium.p = 101325.0; + enthalpyExchanger.airDuct2.vol[3].dynBal.medium.p = 101325.0; + enthalpyExchanger.airDuct2.vol[4].dynBal.medium.p = 101325.0; + enthalpyExchanger.airDuct2.vol[5].dynBal.medium.p = 101325.0; + enthalpyExchanger.airDuct2.vol[6].dynBal.medium.p = 101325.0; + enthalpyExchanger.airDuct2.vol[7].dynBal.medium.p = 101325.0; + enthalpyExchanger.airDuct2.vol[8].dynBal.medium.p = 101325.0; + enthalpyExchanger.airDuct2.vol[9].dynBal.medium.p = 101325.0; + enthalpyExchanger.airDuct2.vol[10].dynBal.medium.p = 101325.0; + enthalpyExchanger.airDuct2.vol[11].dynBal.medium.p = 101325.0; + enthalpyExchanger.airDuct2.vol[12].dynBal.medium.p = 101325.0; + enthalpyExchanger.airDuct2.vol[13].dynBal.medium.p = 101325.0; + enthalpyExchanger.airDuct2.vol[14].dynBal.medium.p = 101325.0; + enthalpyExchanger.airDuct2.vol[15].dynBal.medium.p = 101325.0; + enthalpyExchanger.airDuct1.vol[1].dynBal.medium.p = 101325.0; + enthalpyExchanger.airDuct1.vol[2].dynBal.medium.p = 101325.0; + enthalpyExchanger.airDuct1.vol[3].dynBal.medium.p = 101325.0; + enthalpyExchanger.airDuct1.vol[4].dynBal.medium.p = 101325.0; + enthalpyExchanger.airDuct1.vol[5].dynBal.medium.p = 101325.0; + enthalpyExchanger.airDuct1.vol[6].dynBal.medium.p = 101325.0; + enthalpyExchanger.airDuct1.vol[7].dynBal.medium.p = 101325.0; + enthalpyExchanger.airDuct1.vol[8].dynBal.medium.p = 101325.0; + enthalpyExchanger.airDuct1.vol[9].dynBal.medium.p = 101325.0; + enthalpyExchanger.airDuct1.vol[10].dynBal.medium.p = 101325.0; + enthalpyExchanger.airDuct1.vol[11].dynBal.medium.p = 101325.0; + enthalpyExchanger.airDuct1.vol[12].dynBal.medium.p = 101325.0; + enthalpyExchanger.airDuct1.vol[13].dynBal.medium.p = 101325.0; + enthalpyExchanger.airDuct1.vol[14].dynBal.medium.p = 101325.0; + enthalpyExchanger.airDuct1.vol[15].dynBal.medium.p = 101325.0; + fan.vol.dynBal.medium.p = fan.vol.dynBal.p_start; + fan1.vol.dynBal.medium.p = fan1.vol.dynBal.p_start; + + +Statistics + +Original Model + Number of components: 678 + Variables: 7286 + Constants: 168 (168 scalars) + Parameters: 2808 (3271 scalars) + Unknowns: 4310 (5682 scalars) + Differentiated variables: 129 scalars + Equations: 2965 + Nontrivial: 2307 +Translated Model + Constants: 2679 scalars + Free parameters: 251 scalars + Parameter depending: 1419 scalars + Continuous time states: 97 scalars + Time-varying variables: 1772 scalars + Alias variables: 3000 scalars + Number of mixed real/discrete systems of equations: 0 + Sizes of linear systems of equations: {2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 3, 3, 3, 3, 3, 3, 3, 3, 3, 3, 3, 3, 3, 3, 3} + Sizes after manipulation of the linear systems: {0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2} + Sizes of nonlinear systems of equations: {1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1} + Sizes after manipulation of the nonlinear systems: {0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0} + Number of numerical Jacobians: 0 + Initialization problem + Sizes of nonlinear systems of equations: {1, 1} + Sizes after manipulation of the nonlinear systems: {0, 0} + Number of numerical Jacobians: 0 + +Selected continuous time states +Statically selected continuous time states +conPID.I.y +conPID1.I.y +enthalpyExchanger.airDuct1.senRelHum.phi +enthalpyExchanger.airDuct1.senTem.T +enthalpyExchanger.airDuct1.vol[1].dynBal.medium.Xi[1] +enthalpyExchanger.airDuct1.vol[1].dynBal.U +enthalpyExchanger.airDuct1.vol[2].dynBal.medium.Xi[1] +enthalpyExchanger.airDuct1.vol[2].dynBal.U +enthalpyExchanger.airDuct1.vol[3].dynBal.medium.Xi[1] +enthalpyExchanger.airDuct1.vol[3].dynBal.U +enthalpyExchanger.airDuct1.vol[4].dynBal.medium.Xi[1] +enthalpyExchanger.airDuct1.vol[4].dynBal.U +enthalpyExchanger.airDuct1.vol[5].dynBal.medium.Xi[1] +enthalpyExchanger.airDuct1.vol[5].dynBal.U +enthalpyExchanger.airDuct1.vol[6].dynBal.medium.Xi[1] +enthalpyExchanger.airDuct1.vol[6].dynBal.U +enthalpyExchanger.airDuct1.vol[7].dynBal.medium.Xi[1] +enthalpyExchanger.airDuct1.vol[7].dynBal.U +enthalpyExchanger.airDuct1.vol[8].dynBal.medium.Xi[1] +enthalpyExchanger.airDuct1.vol[8].dynBal.U +enthalpyExchanger.airDuct1.vol[9].dynBal.medium.Xi[1] +enthalpyExchanger.airDuct1.vol[9].dynBal.U +enthalpyExchanger.airDuct1.vol[10].dynBal.medium.Xi[1] +enthalpyExchanger.airDuct1.vol[10].dynBal.U +enthalpyExchanger.airDuct1.vol[11].dynBal.medium.Xi[1] +enthalpyExchanger.airDuct1.vol[11].dynBal.U +enthalpyExchanger.airDuct1.vol[12].dynBal.medium.Xi[1] +enthalpyExchanger.airDuct1.vol[12].dynBal.U +enthalpyExchanger.airDuct1.vol[13].dynBal.medium.Xi[1] +enthalpyExchanger.airDuct1.vol[13].dynBal.U +enthalpyExchanger.airDuct1.vol[14].dynBal.medium.Xi[1] +enthalpyExchanger.airDuct1.vol[14].dynBal.U +enthalpyExchanger.airDuct1.vol[15].dynBal.medium.Xi[1] +enthalpyExchanger.airDuct1.vol[15].dynBal.U +enthalpyExchanger.airDuct2.senRelHum.phi +enthalpyExchanger.airDuct2.senTem.T +enthalpyExchanger.airDuct2.vol[1].dynBal.medium.Xi[1] +enthalpyExchanger.airDuct2.vol[1].dynBal.U +enthalpyExchanger.airDuct2.vol[2].dynBal.medium.Xi[1] +enthalpyExchanger.airDuct2.vol[2].dynBal.U +enthalpyExchanger.airDuct2.vol[3].dynBal.medium.Xi[1] +enthalpyExchanger.airDuct2.vol[3].dynBal.U +enthalpyExchanger.airDuct2.vol[4].dynBal.medium.Xi[1] +enthalpyExchanger.airDuct2.vol[4].dynBal.U +enthalpyExchanger.airDuct2.vol[5].dynBal.medium.Xi[1] +enthalpyExchanger.airDuct2.vol[5].dynBal.U +enthalpyExchanger.airDuct2.vol[6].dynBal.medium.Xi[1] +enthalpyExchanger.airDuct2.vol[6].dynBal.U +enthalpyExchanger.airDuct2.vol[7].dynBal.medium.Xi[1] +enthalpyExchanger.airDuct2.vol[7].dynBal.U +enthalpyExchanger.airDuct2.vol[8].dynBal.medium.Xi[1] +enthalpyExchanger.airDuct2.vol[8].dynBal.U +enthalpyExchanger.airDuct2.vol[9].dynBal.medium.Xi[1] +enthalpyExchanger.airDuct2.vol[9].dynBal.U +enthalpyExchanger.airDuct2.vol[10].dynBal.medium.Xi[1] +enthalpyExchanger.airDuct2.vol[10].dynBal.U +enthalpyExchanger.airDuct2.vol[11].dynBal.medium.Xi[1] +enthalpyExchanger.airDuct2.vol[11].dynBal.U +enthalpyExchanger.airDuct2.vol[12].dynBal.medium.Xi[1] +enthalpyExchanger.airDuct2.vol[12].dynBal.U +enthalpyExchanger.airDuct2.vol[13].dynBal.medium.Xi[1] +enthalpyExchanger.airDuct2.vol[13].dynBal.U +enthalpyExchanger.airDuct2.vol[14].dynBal.medium.Xi[1] +enthalpyExchanger.airDuct2.vol[14].dynBal.U +enthalpyExchanger.airDuct2.vol[15].dynBal.medium.Xi[1] +enthalpyExchanger.airDuct2.vol[15].dynBal.U +enthalpyExchanger.membrane.heatTransfer.Ts[1] +enthalpyExchanger.membrane.heatTransfer.Ts[2] +enthalpyExchanger.membrane.heatTransfer.Ts[3] +enthalpyExchanger.membrane.heatTransfer.Ts[4] +enthalpyExchanger.membrane.heatTransfer.Ts[5] +enthalpyExchanger.membrane.heatTransfer.Ts[6] +enthalpyExchanger.membrane.heatTransfer.Ts[7] +enthalpyExchanger.membrane.heatTransfer.Ts[8] +enthalpyExchanger.membrane.heatTransfer.Ts[9] +enthalpyExchanger.membrane.heatTransfer.Ts[10] +enthalpyExchanger.membrane.heatTransfer.Ts[11] +enthalpyExchanger.membrane.heatTransfer.Ts[12] +enthalpyExchanger.membrane.heatTransfer.Ts[13] +enthalpyExchanger.membrane.heatTransfer.Ts[14] +enthalpyExchanger.membrane.heatTransfer.Ts[15] +fan.filter.s[1] +fan.filter.s[2] +fan.vol.dynBal.medium.Xi[1] +fan.vol.dynBal.U +fan1.filter.s[1] +fan1.filter.s[2] +fan1.vol.dynBal.medium.Xi[1] +fan1.vol.dynBal.U +senMasFraEha.X +senMasFraEta.X +senMasFraOda.X +senMasFraSup.X +senTemEha.T +senTemEta.T +senTemOda.T +senTemSup.T +Finished +Finished + = true + +Declaring variable: Boolean rScript ; + +savelog("AixLib.Fluid.MassExchangers.MembraneBasedEnthalpyExchangers.Validation.DynamicValidation.translation.log"); = true + + +rCheck = checkModel("AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.PlugFlowPipeZeta"); +Check of AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.PlugFlowPipeZeta +Warning: Local "m_flow_small" conflict with inherited. Should be identical +Warning: Component m_flow_small(min = << Empty >>), + but previously m_flow_small(min = 0). + The components are not identical. + + For element m_flow_small found at + + File: /tmp/tmp-AixLib-1-qvb0s8zm/AixLib/Fluid/DistrictHeatingCooling/Pipes/PlugFlowPipeZeta.mo, line 36 + Conflict with element from + File: /tmp/tmp-AixLib-1-qvb0s8zm/AixLib/Fluid/Interfaces/PartialTwoPortInterface.mo, line 10 + Component context: pip + Component declared as PlugFlowPipeZeta pip in AixLib.Fluid.DistrictHeatingCooling.Pipes + File: /tmp/tmp-AixLib-1-qvb0s8zm/AixLib/Fluid/DistrictHeatingCooling/Pipes/Examples/PlugFlowPipeZeta.mo, line 18 +The model has the same number of unknowns and equations: 187 +The model could not be deduced to be symbolically well-posed. +The model has + 185+pip.vol.dynBal.nPorts +scalar unknowns and + 171+(if sin.use_Xi_in then 1 else (if sin.use_X_in then 0 else 1))+(if not sin.use_p_in then 1 else 0)+2*sin.nPorts+(if not sin.use_T_in then 1 else 0)+ (if sou.use_Xi_in then 1 else (if sou.use_X_in then 0 else 1))+(if not sou.use_m_flow_in then 1 else 0)+2*sou.nPorts+(if not sou.use_T_in then 1 else 0)+(if not pip.vol.dynBal.use_mWat_flow then 1 else 0)+3* pip.vol.dynBal.nPorts +scalar equations. +However, exploiting the given numerical settings of parameters gives the same number of unknowns and equations: + 187 +Check of AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.PlugFlowPipeZeta successful. +Declaring variable: Boolean rCheck ; + +Modelica.Utilities.Streams.print(" { \"file\" : \"AixLib/Resources/Scripts/Dymola/Fluid/DistrictHeatingCooling/Pipes/Examples/PlugFlowPipeZeta.mos\",", "AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.PlugFlowPipeZeta.statistics.log"); +Modelica.Utilities.Streams.print(" \"model\" : \"AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.PlugFlowPipeZeta\",", "AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.PlugFlowPipeZeta.statistics.log"); +Modelica.Utilities.Streams.print(" \"check\" : {", "AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.PlugFlowPipeZeta.statistics.log"); +Modelica.Utilities.Streams.print(" \"command\" : \"checkModel(\\\"AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.PlugFlowPipeZeta\\\");\",", "AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.PlugFlowPipeZeta.statistics.log"); +Modelica.Utilities.Streams.print(" \"result\" : " + String(rCheck), "AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.PlugFlowPipeZeta.statistics.log"); +Modelica.Utilities.Streams.print(" },", "AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.PlugFlowPipeZeta.statistics.log"); + + +rScript=RunScript("modelica://AixLib/Resources/Scripts/Dymola/Fluid/DistrictHeatingCooling/Pipes/Examples/PlugFlowPipeZeta.mos"); +simulateModel("AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.PlugFlowPipeZeta", stopTime=1000, method="dassl", tolerance=1e-6, resultFile="AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.PlugFlowPipeZeta"); +Translation of AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.PlugFlowPipeZeta +Warning: Local "m_flow_small" conflict with inherited. Should be identical +Warning: Component m_flow_small(min = << Empty >>), + but previously m_flow_small(min = 0). + The components are not identical. + + For element m_flow_small found at + + File: /tmp/tmp-AixLib-1-qvb0s8zm/AixLib/Fluid/DistrictHeatingCooling/Pipes/PlugFlowPipeZeta.mo, line 36 + Conflict with element from + File: /tmp/tmp-AixLib-1-qvb0s8zm/AixLib/Fluid/Interfaces/PartialTwoPortInterface.mo, line 10 + Component context: pip + Component declared as PlugFlowPipeZeta pip in AixLib.Fluid.DistrictHeatingCooling.Pipes + File: /tmp/tmp-AixLib-1-qvb0s8zm/AixLib/Fluid/DistrictHeatingCooling/Pipes/Examples/PlugFlowPipeZeta.mo, line 18 +The DAE has 187 scalar unknowns and 187 scalar equations. + +Statistics + +Original Model + Number of components: 34 + Variables: 537 + Constants: 10 (10 scalars) + Parameters: 262 (255 scalars) + Unknowns: 265 (193 scalars) + Differentiated variables: 6 scalars + Equations: 220 + Nontrivial: 186 +Translated Model + Constants: 189 scalars + Free parameters: 46 scalars + Parameter depending: 66 scalars + Continuous time states: 5 scalars + Time-varying variables: 39 scalars + Alias variables: 118 scalars + Number of mixed real/discrete systems of equations: 0 + Sizes of linear systems of equations: { } + Sizes after manipulation of the linear systems: { } + Sizes of nonlinear systems of equations: { } + Sizes after manipulation of the nonlinear systems: { } + Number of numerical Jacobians: 0 + +Selected continuous time states +Statically selected continuous time states +pip.plugFlowCore.del.x +pip.plugFlowCore.timDel.x +pip.vol.dynBal.U +senTemIn.T +senTemOut.T +Finished +Warning: WARNINGS have been issued. +Finished + = true + +Declaring variable: Boolean rScript ; + +savelog("AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.PlugFlowPipeZeta.translation.log"); = true + + +rCheck = checkModel("AixLib.Fluid.Pools.Examples.IndoorSwimmingPoolExternalHeatingSystem"); +Check of AixLib.Fluid.Pools.Examples.IndoorSwimmingPoolExternalHeatingSystem +The model has the same number of unknowns and equations: 733 +The model has the same number of unknowns and equations +for the given numerical settings of parameters: 733 +Check of AixLib.Fluid.Pools.Examples.IndoorSwimmingPoolExternalHeatingSystem successful. +Declaring variable: Boolean rCheck ; + +Modelica.Utilities.Streams.print(" { \"file\" : \"AixLib/Resources/Scripts/Dymola/Fluid/Pools/Examples/IndoorSwimmingPoolExternalHeatingSystem.mos\",", "AixLib.Fluid.Pools.Examples.IndoorSwimmingPoolExternalHeatingSystem.statistics.log"); +Modelica.Utilities.Streams.print(" \"model\" : \"AixLib.Fluid.Pools.Examples.IndoorSwimmingPoolExternalHeatingSystem\",", "AixLib.Fluid.Pools.Examples.IndoorSwimmingPoolExternalHeatingSystem.statistics.log"); +Modelica.Utilities.Streams.print(" \"check\" : {", "AixLib.Fluid.Pools.Examples.IndoorSwimmingPoolExternalHeatingSystem.statistics.log"); +Modelica.Utilities.Streams.print(" \"command\" : \"checkModel(\\\"AixLib.Fluid.Pools.Examples.IndoorSwimmingPoolExternalHeatingSystem\\\");\",", "AixLib.Fluid.Pools.Examples.IndoorSwimmingPoolExternalHeatingSystem.statistics.log"); +Modelica.Utilities.Streams.print(" \"result\" : " + String(rCheck), "AixLib.Fluid.Pools.Examples.IndoorSwimmingPoolExternalHeatingSystem.statistics.log"); +Modelica.Utilities.Streams.print(" },", "AixLib.Fluid.Pools.Examples.IndoorSwimmingPoolExternalHeatingSystem.statistics.log"); + + +rScript=RunScript("modelica://AixLib/Resources/Scripts/Dymola/Fluid/Pools/Examples/IndoorSwimmingPoolExternalHeatingSystem.mos"); +simulateModel("AixLib.Fluid.Pools.Examples.IndoorSwimmingPoolExternalHeatingSystem", tolerance=1e-6, stopTime=604800, numberOfIntervals=0, outputInterval=900, method="CVode", resultFile="AixLib.Fluid.Pools.Examples.IndoorSwimmingPoolExternalHeatingSystem"); +Translation of AixLib.Fluid.Pools.Examples.IndoorSwimmingPoolExternalHeatingSystem +The DAE has 733 scalar unknowns and 733 scalar equations. + +Statistics + +Original Model + Number of components: 171 + Variables: 1742 + Constants: 45 (45 scalars) + Parameters: 777 (964 scalars) + Unknowns: 920 (764 scalars) + Differentiated variables: 3 scalars + Equations: 763 + Nontrivial: 619 +Translated Model + Constants: 589 scalars + Free parameters: 134 scalars + Parameter depending: 413 scalars + Continuous time states: 3 scalars + Time-varying variables: 191 scalars + Alias variables: 446 scalars + Number of mixed real/discrete systems of equations: 1 + Sizes of linear systems of equations: {26} + Sizes after manipulation of the linear systems: {13} + Sizes of nonlinear systems of equations: {79, 1, 1} + Sizes after manipulation of the nonlinear systems: {17, 0, 1} + Number of numerical Jacobians: 0 + Initialization problem + Sizes of nonlinear systems of equations: {1, 78, 1} + Sizes after manipulation of the nonlinear systems: {1, 17, 1} + Number of numerical Jacobians: 0 + +Selected continuous time states +Statically selected continuous time states +indoorSwimming.cirPump.filter.s[1] +indoorSwimming.cirPump.filter.s[2] +PI.I.y +Finished +Finished + = true + +Declaring variable: Boolean rScript ; + +savelog("AixLib.Fluid.Pools.Examples.IndoorSwimmingPoolExternalHeatingSystem.translation.log"); = true + + +rCheck = checkModel("AixLib.Fluid.Storage.Examples.StorageSimpleExample"); +Check of AixLib.Fluid.Storage.Examples.StorageSimpleExample +The model has the same number of unknowns and equations: 964 +The model could not be deduced to be symbolically well-posed. +The model has + 938+storageSimple.layer[1].dynBal.nPorts+storageSimple.layer[2].dynBal.nPorts+ storageSimple.layer[3].dynBal.nPorts+storageSimple.layer_HE[1].dynBal.nPorts+ storageSimple.layer_HE[2].dynBal.nPorts+storageSimple.layer_HE[3].dynBal.nPorts +2*storageSimple.n+heatingRod.vol.dynBal.nPorts+simpleConsumer.volume.dynBal.nPorts +pumpGen.vol.dynBal.nPorts+pumpCon.vol.dynBal.nPorts +scalar unknowns and + 869+(if storageSimple.use_TOut then 2*storageSimple.n else 0)+(if pressureBoundary.use_Xi_in then 1 else (if pressureBoundary.use_X_in then 0 else 1))+(if not pressureBoundary.use_p_in then 1 else 0)+2*pressureBoundary.nPorts +(if not pressureBoundary.use_T_in then 1 else 0)+(if pressureBoundary1.use_Xi_in then 1 else (if pressureBoundary1.use_X_in then 0 else 1))+(if not pressureBoundary1.use_p_in then 1 else 0)+2*pressureBoundary1.nPorts+(if not pressureBoundary1.use_T_in then 1 else 0)+(if PIDHR.reset <> AixLib.Types.Reset. Input then 1 else 0)+(if PIDPumpGen.reset <> AixLib.Types.Reset.Input then 1 else 0)+(if PIDPumpCon.reset <> AixLib.Types.Reset.Input then 1 else 0)+(if not storageSimple.layer[1].dynBal.use_mWat_flow then 1 else 0)+3* storageSimple.layer[1].dynBal.nPorts+(if not storageSimple.layer[2].dynBal.use_mWat_flow then 1 else 0)+3*storageSimple.layer[2].dynBal.nPorts+(if not storageSimple.layer[3].dynBal.use_mWat_flow then 1 else 0)+3*storageSimple.layer[3].dynBal.nPorts +(if not storageSimple.layer_HE[1].dynBal.use_mWat_flow then 1 else 0)+3* storageSimple.layer_HE[1].dynBal.nPorts+(if not storageSimple.layer_HE[2].dynBal.use_mWat_flow then 1 else 0)+3*storageSimple.layer_HE[2].dynBal.nPorts+(if not storageSimple.layer_HE[3].dynBal.use_mWat_flow then 1 else 0)+3* storageSimple.layer_HE[3].dynBal.nPorts+(if not heatingRod.vol.dynBal.use_mWat_flow then 1 else 0)+3*heatingRod.vol.dynBal.nPorts+(if not simpleConsumer.volume.dynBal.use_mWat_flow then 1 else 0)+3*simpleConsumer.volume.dynBal.nPorts+(if not pumpGen.vol.dynBal.use_mWat_flow then 1 else 0)+3*pumpGen.vol.dynBal.nPorts+( if not pumpCon.vol.dynBal.use_mWat_flow then 1 else 0)+3*pumpCon.vol.dynBal.nPorts +(if (if PIDHR.reset == AixLib.Types.Reset.Disabled then PIDHR.reset else AixLib.Types.Reset.Input) <> AixLib.Types.Reset.Input then 1 else 0)+(if (if PIDHR.reset == AixLib.Types.Reset.Disabled then PIDHR.reset else AixLib.Types.Reset.Input) == AixLib.Types.Reset.Disabled then 1 else 0)+(if ( if PIDPumpGen.reset == AixLib.Types.Reset.Disabled then PIDPumpGen.reset else AixLib.Types.Reset.Input) <> AixLib.Types.Reset.Input then 1 else 0)+(if (if PIDPumpGen.reset == AixLib.Types.Reset.Disabled then PIDPumpGen.reset else AixLib.Types.Reset.Input) == AixLib.Types.Reset.Disabled then 1 else 0)+(if ( if PIDPumpCon.reset == AixLib.Types.Reset.Disabled then PIDPumpCon.reset else AixLib.Types.Reset.Input) <> AixLib.Types.Reset.Input then 1 else 0)+(if (if PIDPumpCon.reset == AixLib.Types.Reset.Disabled then PIDPumpCon.reset else AixLib.Types.Reset.Input) == AixLib.Types.Reset.Disabled then 1 else 0) +scalar equations. +However, exploiting the given numerical settings of parameters gives the same number of unknowns and equations: + 964 +Check of AixLib.Fluid.Storage.Examples.StorageSimpleExample successful. +Declaring variable: Boolean rCheck ; + +Modelica.Utilities.Streams.print(" { \"file\" : \"AixLib/Resources/Scripts/Dymola/Fluid/Storage/Examples/StorageSimpleExample.mos\",", "AixLib.Fluid.Storage.Examples.StorageSimpleExample.statistics.log"); +Modelica.Utilities.Streams.print(" \"model\" : \"AixLib.Fluid.Storage.Examples.StorageSimpleExample\",", "AixLib.Fluid.Storage.Examples.StorageSimpleExample.statistics.log"); +Modelica.Utilities.Streams.print(" \"check\" : {", "AixLib.Fluid.Storage.Examples.StorageSimpleExample.statistics.log"); +Modelica.Utilities.Streams.print(" \"command\" : \"checkModel(\\\"AixLib.Fluid.Storage.Examples.StorageSimpleExample\\\");\",", "AixLib.Fluid.Storage.Examples.StorageSimpleExample.statistics.log"); +Modelica.Utilities.Streams.print(" \"result\" : " + String(rCheck), "AixLib.Fluid.Storage.Examples.StorageSimpleExample.statistics.log"); +Modelica.Utilities.Streams.print(" },", "AixLib.Fluid.Storage.Examples.StorageSimpleExample.statistics.log"); + + +rScript=RunScript("modelica://AixLib/Resources/Scripts/Dymola/Fluid/Storage/Examples/StorageSimpleExample.mos"); +simulateModel("AixLib.Fluid.Storage.Examples.StorageSimpleExample", tolerance=1e-6, stopTime=38200, method="dassl", resultFile="AixLib.Fluid.Storage.Examples.StorageSimpleExample"); +Translation of AixLib.Fluid.Storage.Examples.StorageSimpleExample +The DAE has 964 scalar unknowns and 964 scalar equations. + +Statistics + +Original Model + Number of components: 247 + Variables: 2530 + Constants: 57 (57 scalars) + Parameters: 1181 (1670 scalars) + Unknowns: 1292 (1010 scalars) + Differentiated variables: 28 scalars + Equations: 1101 + Nontrivial: 860 +Translated Model + Constants: 1047 scalars + Free parameters: 186 scalars + Parameter depending: 627 scalars + Outputs: 1 scalars + Continuous time states: 17 scalars + Time-varying variables: 245 scalars + Alias variables: 632 scalars + Number of mixed real/discrete systems of equations: 0 + Sizes of linear systems of equations: {4} + Sizes after manipulation of the linear systems: {0} + Sizes of nonlinear systems of equations: {5, 7} + Sizes after manipulation of the nonlinear systems: {1, 1} + Number of numerical Jacobians: 0 + Initialization problem + Sizes of nonlinear systems of equations: {5, 1, 7, 1} + Sizes after manipulation of the nonlinear systems: {1, 0, 1, 0} + Sizes of simplified homotopy nonlinear systems of equations: {5, 1, 7, 1} + Sizes after manipulation of the simplified homotopy nonlinear systems: {1, 0, 1, 0} + Number of numerical Jacobians: 0 + +Selected continuous time states +Statically selected continuous time states +heatingRod.vol.dynBal.U +PIDHR.I.y +PIDPumpCon.I.y +PIDPumpGen.I.y +pumpCon.filter.s[1] +pumpCon.filter.s[2] +pumpCon.vol.dynBal.U +pumpGen.filter.s[1] +pumpGen.filter.s[2] +pumpGen.vol.dynBal.U +simpleConsumer.heatCapacitor.T +storageSimple.layer[1].dynBal.U +storageSimple.layer[2].dynBal.U +storageSimple.layer[3].dynBal.U +storageSimple.layer_HE[1].dynBal.U +storageSimple.layer_HE[2].dynBal.U +storageSimple.layer_HE[3].dynBal.U +Finished +Finished + = true + +Declaring variable: Boolean rScript ; + +savelog("AixLib.Fluid.Storage.Examples.StorageSimpleExample.translation.log"); = true + + +rCheck = checkModel("AixLib.Fluid.HeatPumps.ModularReversible.Examples.VCLibAirToWater_OneRoomRadiator"); +Check of AixLib.Fluid.HeatPumps.ModularReversible.Examples.VCLibAirToWater_OneRoomRadiator +The model has the same number of unknowns and equations: 1648 +The model could not be deduced to be symbolically well-posed. +The model has + 1603+2*(rad.nEle+vol.dynBal.nPorts)+max([size(timTab.columns, 1); size( timTab.offset, 1)])+rad.vol[1].dynBal.nPorts+rad.vol[2].dynBal.nPorts+ rad.vol[3].dynBal.nPorts+rad.vol[4].dynBal.nPorts+rad.vol[5].dynBal.nPorts+ rad.sumCon.nin+rad.sumRad.nin+heaPum.con.vol.dynBal.nPorts+2*heaPum.eva.vol.dynBal.nPorts +size(heaPum.safCtr.opeEnv.bouMapHea.tabBou.columns, 1)+heaPum.safCtr.opeEnv.bouMapHea.nor.nu +size(heaPum.safCtr.opeEnv.bouMapCoo.tabBou.columns, 1)+heaPum.safCtr.opeEnv.bouMapCoo.nor.nu +scalar unknowns and + 1555+max([size(timTab.columns, 1); size(timTab.offset, 1)])+(if weaDat.pAtmSou == AixLib.BoundaryConditions.Types.DataSource.Parameter then 1 else 0)+(if weaDat.TDewPoiSou == AixLib.BoundaryConditions.Types.DataSource.Parameter then 1 else 0)+(if weaDat.TDryBulSou == AixLib.BoundaryConditions.Types.DataSource. Parameter then 1 else 0)+(if weaDat.TBlaSkySou == AixLib.BoundaryConditions.Types.DataSource. Parameter then 1 else 0)+(if weaDat.relHumSou == AixLib.BoundaryConditions.Types.DataSource. Parameter then 1 else 0)+(if weaDat.opaSkyCovSou == AixLib.BoundaryConditions.Types.DataSource. Parameter then 1 else 0)+(if weaDat.ceiHeiSou == AixLib.BoundaryConditions.Types.DataSource. Parameter then 1 else 0)+(if weaDat.totSkyCovSou == AixLib.BoundaryConditions.Types.DataSource. Parameter then 1 else 0)+(if weaDat.winSpeSou == AixLib.BoundaryConditions.Types.DataSource. Parameter then 1 else 0)+(if weaDat.winDirSou == AixLib.BoundaryConditions.Types.DataSource. Parameter then 1 else 0)+(if weaDat.HInfHorSou == AixLib.BoundaryConditions.Types.DataSource. Parameter then 1 else 0)+(if weaDat.HSou == AixLib.BoundaryConditions.Types.RadiationDataSource. Input_HDirNor_HDifHor then 2 else 1)+(if weaDat.HSou == AixLib.BoundaryConditions.Types.RadiationDataSource. Input_HDirNor_HGloHor then 2 else 1)+(if weaDat.HSou == AixLib.BoundaryConditions.Types.RadiationDataSource. Input_HGloHor_HDifHor then 2 else 1)+(if sou.use_Xi_in then 2 else (if sou.use_X_in then 1 else 3))+3*sou.nPorts+(if not sou.use_p_in then 1 else 0) +(if not sou.use_T_in then 1 else 0)+(if sin.use_Xi_in then 2 else (if sin.use_X_in then 1 else 3))+3*sin.nPorts+(if not sin.use_p_in then 1 else 0) +(if not sin.use_T_in then 1 else 0)+(if preSou.use_Xi_in then 1 else (if preSou.use_X_in then 0 else 1))+(if not preSou.use_p_in then 1 else 0)+2* preSou.nPorts+(if not preSou.use_T_in then 1 else 0)+(if not vol.dynBal.use_mWat_flow then 1 else 0)+5*vol.dynBal.nPorts+(if not rad.vol[1].dynBal.use_mWat_flow then 1 else 0)+3*rad.vol[1].dynBal.nPorts+(if not rad.vol[2].dynBal.use_mWat_flow then 1 else 0)+3*rad.vol[2].dynBal.nPorts +(if not rad.vol[3].dynBal.use_mWat_flow then 1 else 0)+3*rad.vol[3].dynBal.nPorts +(if not rad.vol[4].dynBal.use_mWat_flow then 1 else 0)+3*rad.vol[4].dynBal.nPorts +(if not rad.vol[5].dynBal.use_mWat_flow then 1 else 0)+3*rad.vol[5].dynBal.nPorts +(if not pumHeaPum.vol.steBal.use_mWat_flow then 1 else 0)+(if not pumHeaPumSou.vol.steBal.use_mWat_flow then 1 else 0)+(if not heaPum.con.vol.dynBal.use_mWat_flow then 1 else 0)+3*heaPum.con.vol.dynBal.nPorts+(if not heaPum.eva.vol.dynBal.use_mWat_flow then 1 else 0)+5*heaPum.eva.vol.dynBal.nPorts+size(heaPum.safCtr.opeEnv.bouMapHea.tabBou.columns, 1)+size(heaPum.safCtr.opeEnv.bouMapCoo.tabBou.columns, 1)+2*rad.nEle +scalar equations. +However, exploiting the given numerical settings of parameters gives the same number of unknowns and equations: + 1648 +Check of AixLib.Fluid.HeatPumps.ModularReversible.Examples.VCLibAirToWater_OneRoomRadiator successful. +Declaring variable: Boolean rCheck ; + +Modelica.Utilities.Streams.print(" { \"file\" : \"AixLib/Resources/Scripts/Dymola/Fluid/HeatPumps/ModularReversible/Examples/VCLibAirToWater_OneRoomRadiator.mos\",", "AixLib.Fluid.HeatPumps.ModularReversible.Examples.VCLibAirToWater_OneRoomRadiator.statistics.log"); +Modelica.Utilities.Streams.print(" \"model\" : \"AixLib.Fluid.HeatPumps.ModularReversible.Examples.VCLibAirToWater_OneRoomRadiator\",", "AixLib.Fluid.HeatPumps.ModularReversible.Examples.VCLibAirToWater_OneRoomRadiator.statistics.log"); +Modelica.Utilities.Streams.print(" \"check\" : {", "AixLib.Fluid.HeatPumps.ModularReversible.Examples.VCLibAirToWater_OneRoomRadiator.statistics.log"); +Modelica.Utilities.Streams.print(" \"command\" : \"checkModel(\\\"AixLib.Fluid.HeatPumps.ModularReversible.Examples.VCLibAirToWater_OneRoomRadiator\\\");\",", "AixLib.Fluid.HeatPumps.ModularReversible.Examples.VCLibAirToWater_OneRoomRadiator.statistics.log"); +Modelica.Utilities.Streams.print(" \"result\" : " + String(rCheck), "AixLib.Fluid.HeatPumps.ModularReversible.Examples.VCLibAirToWater_OneRoomRadiator.statistics.log"); +Modelica.Utilities.Streams.print(" },", "AixLib.Fluid.HeatPumps.ModularReversible.Examples.VCLibAirToWater_OneRoomRadiator.statistics.log"); + + +rScript=RunScript("modelica://AixLib/Resources/Scripts/Dymola/Fluid/HeatPumps/ModularReversible/Examples/VCLibAirToWater_OneRoomRadiator.mos"); +simulateModel("AixLib.Fluid.HeatPumps.ModularReversible.Examples.VCLibAirToWater_OneRoomRadiator", stopTime=86400, method="CVode", tolerance=1e-08, resultFile="AixLib.Fluid.HeatPumps.ModularReversible.Examples.VCLibAirToWater_OneRoomRadiator"); +Translation of AixLib.Fluid.HeatPumps.ModularReversible.Examples.VCLibAirToWater_OneRoomRadiator +The DAE has 1648 scalar unknowns and 1648 scalar equations. +Redundant consistent initial conditions. +Removed the following equations which are redundant and consistent: + heaPum.eva.p_start = heaPum.pEva_start; + +This required evaluation of +the interactive parameters + heaPum.pEva_start(start = 101325) + sin.p(start = 101325) + + +Statistics + +Original Model + Number of components: 429 + Variables: 3472 + Constants: 77 (77 scalars) + Parameters: 1665 (2022 scalars) + Unknowns: 1730 (1705 scalars) + Differentiated variables: 22 scalars + Equations: 1612 + Nontrivial: 1342 +Translated Model + Constants: 1493 scalars + Free parameters: 220 scalars + Parameter depending: 765 scalars + Outputs: 24 scalars + Continuous time states: 14 scalars + Time-varying variables: 351 scalars + Alias variables: 975 scalars + Number of mixed real/discrete systems of equations: 0 + Sizes of linear systems of equations: {2, 2, 2, 2, 2, 4} + Sizes after manipulation of the linear systems: {0, 0, 0, 0, 0, 0} + Sizes of nonlinear systems of equations: {3} + Sizes after manipulation of the nonlinear systems: {1} + Number of numerical Jacobians: 0 + Initialization problem + Sizes of nonlinear systems of equations: {11, 1, 1, 2} + Sizes after manipulation of the nonlinear systems: {5, 1, 1, 1} + Sizes of simplified homotopy nonlinear systems of equations: {2} + Sizes after manipulation of the simplified homotopy nonlinear systems: {1} + Number of numerical Jacobians: 0 + +Selected continuous time states +Statically selected continuous time states +heaPum.con.vol.dynBal.U +heaPum.eva.vol.dynBal.medium.Xi[1] +heaPum.eva.vol.dynBal.U +oneRooRadHeaPumCtr.PIDHea.I.y +rad.vol[1].dynBal.U +rad.vol[2].dynBal.U +rad.vol[3].dynBal.U +rad.vol[4].dynBal.U +rad.vol[5].dynBal.U +temRet.T +temSup.T +vol.dynBal.m +vol.dynBal.medium.Xi[1] +vol.hOut_internal +Finished +Finished + = true + +Declaring variable: Boolean rScript ; + +savelog("AixLib.Fluid.HeatPumps.ModularReversible.Examples.VCLibAirToWater_OneRoomRadiator.translation.log"); = true + + +rCheck = checkModel("AixLib.Fluid.DistrictHeatingCooling.Demands.Examples.OpenLoopHeatPumpCarnot"); +Check of AixLib.Fluid.DistrictHeatingCooling.Demands.Examples.OpenLoopHeatPumpCarnot +The model has the same number of unknowns and equations: 699 +The model could not be deduced to be symbolically well-posed. +The model has + 691+pipeSupply.vol_b.dynBal.nPorts+pipeSupply.vol_a.dynBal.nPorts+ pipeReturn.vol_b.dynBal.nPorts+pipeReturn.vol_a.dynBal.nPorts +scalar unknowns and + 647+(if sourceIdeal.source.use_Xi_in then 1 else (if sourceIdeal.source.use_X_in then 0 else 1))+(if not sourceIdeal.source.use_p_in then 1 else 0)+2* sourceIdeal.source.nPorts+(if not sourceIdeal.source.use_T_in then 1 else 0)+ (if sourceIdeal.sink.use_Xi_in then 1 else (if sourceIdeal.sink.use_X_in then 0 else 1))+(if not sourceIdeal.sink.use_p_in then 1 else 0)+2*sourceIdeal.sink.nPorts +(if not sourceIdeal.sink.use_T_in then 1 else 0)+(if demand.sink.use_Xi_in then 1 else (if demand.sink.use_X_in then 0 else 1))+(if not demand.sink.use_m_flow_in then 1 else 0)+2*demand.sink.nPorts+(if not demand.sink.use_T_in then 1 else 0)+(if demand.source.use_Xi_in then 1 else ( if demand.source.use_X_in then 0 else 1))+(if not demand.source.use_m_flow_in then 1 else 0)+2*demand.source.nPorts+(if not demand.source.use_T_in then 1 else 0)+(if demand.sourceHeating.use_Xi_in then 1 else (if demand.sourceHeating.use_X_in then 0 else 1))+(if not demand.sourceHeating.use_m_flow_in then 1 else 0)+2* demand.sourceHeating.nPorts+(if not demand.sourceHeating.use_T_in then 1 else 0)+(if demand.sinkHeating.use_Xi_in then 1 else (if demand.sinkHeating.use_X_in then 0 else 1))+(if not demand.sinkHeating.use_p_in then 1 else 0)+2* demand.sinkHeating.nPorts+(if not demand.sinkHeating.use_T_in then 1 else 0)+ (if not demand.heaPum.eva.vol.steBal.use_mWat_flow then 1 else 0)+(if not pipeSupply.vol_b.dynBal.use_mWat_flow then 1 else 0)+3*pipeSupply.vol_b.dynBal.nPorts +(if not pipeSupply.vol_a.dynBal.use_mWat_flow then 1 else 0)+3* pipeSupply.vol_a.dynBal.nPorts+(if not pipeReturn.vol_b.dynBal.use_mWat_flow then 1 else 0)+3*pipeReturn.vol_b.dynBal.nPorts+(if not pipeReturn.vol_a.dynBal.use_mWat_flow then 1 else 0)+3*pipeReturn.vol_a.dynBal.nPorts +scalar equations. +However, exploiting the given numerical settings of parameters gives the same number of unknowns and equations: + 699 +Check of AixLib.Fluid.DistrictHeatingCooling.Demands.Examples.OpenLoopHeatPumpCarnot successful. +Declaring variable: Boolean rCheck ; + +Modelica.Utilities.Streams.print(" { \"file\" : \"AixLib/Resources/Scripts/Dymola/Fluid/DistrictHeatingCooling/Demands/Examples/OpenLoopHeatPumpCarnot.mos\",", "AixLib.Fluid.DistrictHeatingCooling.Demands.Examples.OpenLoopHeatPumpCarnot.statistics.log"); +Modelica.Utilities.Streams.print(" \"model\" : \"AixLib.Fluid.DistrictHeatingCooling.Demands.Examples.OpenLoopHeatPumpCarnot\",", "AixLib.Fluid.DistrictHeatingCooling.Demands.Examples.OpenLoopHeatPumpCarnot.statistics.log"); +Modelica.Utilities.Streams.print(" \"check\" : {", "AixLib.Fluid.DistrictHeatingCooling.Demands.Examples.OpenLoopHeatPumpCarnot.statistics.log"); +Modelica.Utilities.Streams.print(" \"command\" : \"checkModel(\\\"AixLib.Fluid.DistrictHeatingCooling.Demands.Examples.OpenLoopHeatPumpCarnot\\\");\",", "AixLib.Fluid.DistrictHeatingCooling.Demands.Examples.OpenLoopHeatPumpCarnot.statistics.log"); +Modelica.Utilities.Streams.print(" \"result\" : " + String(rCheck), "AixLib.Fluid.DistrictHeatingCooling.Demands.Examples.OpenLoopHeatPumpCarnot.statistics.log"); +Modelica.Utilities.Streams.print(" },", "AixLib.Fluid.DistrictHeatingCooling.Demands.Examples.OpenLoopHeatPumpCarnot.statistics.log"); + + +rScript=RunScript("modelica://AixLib/Resources/Scripts/Dymola/Fluid/DistrictHeatingCooling/Demands/Examples/OpenLoopHeatPumpCarnot.mos"); +translateModel("AixLib.Fluid.DistrictHeatingCooling.Demands.Examples.OpenLoopHeatPumpCarnot"); +Translation of AixLib.Fluid.DistrictHeatingCooling.Demands.Examples.OpenLoopHeatPumpCarnot +The DAE has 699 scalar unknowns and 699 scalar equations. + +Statistics + +Original Model + Number of components: 145 + Variables: 1843 + Constants: 38 (38 scalars) + Parameters: 847 (817 scalars) + Unknowns: 958 (725 scalars) + Differentiated variables: 15 scalars + Equations: 799 + Nontrivial: 663 +Translated Model + Constants: 653 scalars + Free parameters: 145 scalars + Parameter depending: 165 scalars + Continuous time states: 11 scalars + Time-varying variables: 163 scalars + Alias variables: 454 scalars + Number of mixed real/discrete systems of equations: 0 + Sizes of linear systems of equations: { } + Sizes after manipulation of the linear systems: { } + Sizes of nonlinear systems of equations: {13, 8} + Sizes after manipulation of the nonlinear systems: {1, 1} + Number of numerical Jacobians: 0 + Initialization problem + Sizes of nonlinear systems of equations: {13, 8} + Sizes after manipulation of the nonlinear systems: {1, 1} + Number of numerical Jacobians: 0 + +Selected continuous time states +Statically selected continuous time states +demand.senT_return.T +demand.senT_supply.T +pControl.I.y +pipeReturn.del.x +pipeReturn.timDel.x +pipeReturn.vol_a.dynBal.U +pipeReturn.vol_b.dynBal.U +pipeSupply.del.x +pipeSupply.timDel.x +pipeSupply.vol_a.dynBal.U +pipeSupply.vol_b.dynBal.U +Finished + = true +simulateModel("AixLib.Fluid.DistrictHeatingCooling.Demands.Examples.OpenLoopHeatPumpCarnot", stopTime=100000, method="dassl", tolerance=1e-006, resultFile="AixLib.Fluid.DistrictHeatingCooling.Demands.Examples.OpenLoopHeatPumpCarnot"); +Finished +Finished + = true + +Declaring variable: Boolean rScript ; + +savelog("AixLib.Fluid.DistrictHeatingCooling.Demands.Examples.OpenLoopHeatPumpCarnot.translation.log"); = true + + +rCheck = checkModel("AixLib.Fluid.FixedResistances.Examples.SimplePipe"); +Check of AixLib.Fluid.FixedResistances.Examples.SimplePipe +The model has the same number of unknowns and equations: 368 +The model could not be deduced to be symbolically well-posed. +The model has + 360+simplePipe.vol[1].dynBal.nPorts+simplePipe.vol[2].dynBal.nPorts+ simplePipe.vol[3].dynBal.nPorts+simplePipe.vol[4].dynBal.nPorts +scalar unknowns and + 334+2*Source.nPorts+(if not Source.use_m_flow_in then 1 else 0)+(if not Source.use_T_in then 1 else 0)+(if not Source.use_X_in then 1 else 0)+2* Sink.nPorts+(if not simplePipe.vol[1].dynBal.use_mWat_flow then 1 else 0)+3* simplePipe.vol[1].dynBal.nPorts+(if not simplePipe.vol[2].dynBal.use_mWat_flow then 1 else 0)+3*simplePipe.vol[2].dynBal.nPorts+(if not simplePipe.vol[3].dynBal.use_mWat_flow then 1 else 0)+3*simplePipe.vol[3].dynBal.nPorts+(if not simplePipe.vol[4].dynBal.use_mWat_flow then 1 else 0)+3*simplePipe.vol[4].dynBal.nPorts +scalar equations. +However, exploiting the given numerical settings of parameters gives the same number of unknowns and equations: + 368 +Check of AixLib.Fluid.FixedResistances.Examples.SimplePipe successful. +Declaring variable: Boolean rCheck ; + +Modelica.Utilities.Streams.print(" { \"file\" : \"AixLib/Resources/Scripts/Dymola/Fluid/FixedResistances/Examples/SimplePipe.mos\",", "AixLib.Fluid.FixedResistances.Examples.SimplePipe.statistics.log"); +Modelica.Utilities.Streams.print(" \"model\" : \"AixLib.Fluid.FixedResistances.Examples.SimplePipe\",", "AixLib.Fluid.FixedResistances.Examples.SimplePipe.statistics.log"); +Modelica.Utilities.Streams.print(" \"check\" : {", "AixLib.Fluid.FixedResistances.Examples.SimplePipe.statistics.log"); +Modelica.Utilities.Streams.print(" \"command\" : \"checkModel(\\\"AixLib.Fluid.FixedResistances.Examples.SimplePipe\\\");\",", "AixLib.Fluid.FixedResistances.Examples.SimplePipe.statistics.log"); +Modelica.Utilities.Streams.print(" \"result\" : " + String(rCheck), "AixLib.Fluid.FixedResistances.Examples.SimplePipe.statistics.log"); +Modelica.Utilities.Streams.print(" },", "AixLib.Fluid.FixedResistances.Examples.SimplePipe.statistics.log"); + + +rScript=RunScript("modelica://AixLib/Resources/Scripts/Dymola/Fluid/FixedResistances/Examples/SimplePipe.mos"); +translateModel("AixLib.Fluid.FixedResistances.Examples.SimplePipe"); +Translation of AixLib.Fluid.FixedResistances.Examples.SimplePipe +The DAE has 368 scalar unknowns and 368 scalar equations. + +Statistics + +Original Model + Number of components: 80 + Variables: 963 + Constants: 18 (18 scalars) + Parameters: 450 (428 scalars) + Unknowns: 495 (378 scalars) + Differentiated variables: 14 scalars + Equations: 363 + Nontrivial: 270 +Translated Model + Constants: 341 scalars + Free parameters: 44 scalars + Parameter depending: 126 scalars + Continuous time states: 10 scalars + Time-varying variables: 71 scalars + Alias variables: 242 scalars + Number of mixed real/discrete systems of equations: 0 + Sizes of linear systems of equations: { } + Sizes after manipulation of the linear systems: { } + Sizes of nonlinear systems of equations: { } + Sizes after manipulation of the nonlinear systems: { } + Number of numerical Jacobians: 0 + +Selected continuous time states +Statically selected continuous time states +senTemIn.T +senTemOut.T +simplePipe.PipeWall[1].CylindricLoad1.heatCapacitor.T +simplePipe.PipeWall[2].CylindricLoad1.heatCapacitor.T +simplePipe.PipeWall[3].CylindricLoad1.heatCapacitor.T +simplePipe.PipeWall[4].CylindricLoad1.heatCapacitor.T +simplePipe.vol[1].dynBal.U +simplePipe.vol[2].dynBal.U +simplePipe.vol[3].dynBal.U +simplePipe.vol[4].dynBal.U +Finished + = true +simulateModel("AixLib.Fluid.FixedResistances.Examples.SimplePipe", stopTime=1000, method="dassl", tolerance=1e-006, resultFile="AixLib.Fluid.FixedResistances.Examples.SimplePipe"); +Finished + = true + +Declaring variable: Boolean rScript ; + +savelog("AixLib.Fluid.FixedResistances.Examples.SimplePipe.translation.log"); = true + + +rCheck = checkModel("AixLib.Fluid.Movers.DpControlledMovers.Examples.DpVar"); +Check of AixLib.Fluid.Movers.DpControlledMovers.Examples.DpVar +The model has the same number of unknowns and equations: 250 +The model could not be deduced to be symbolically well-posed. +The model has + 248+vol.dynBal.nPorts +scalar unknowns and + 237+(if sou.use_Xi_in then 1 else (if sou.use_X_in then 0 else 1))+(if not sou.use_p_in then 1 else 0)+2*sou.nPorts+(if not sou.use_T_in then 1 else 0)+ (if not dpControlled_dp.mov.vol.steBal.use_mWat_flow then 1 else 0)+(if not vol.dynBal.use_mWat_flow then 1 else 0)+3*vol.dynBal.nPorts +scalar equations. +However, exploiting the given numerical settings of parameters gives the same number of unknowns and equations: + 250 +Check of AixLib.Fluid.Movers.DpControlledMovers.Examples.DpVar successful. +Declaring variable: Boolean rCheck ; + +Modelica.Utilities.Streams.print(" { \"file\" : \"AixLib/Resources/Scripts/Dymola/Fluid/Movers/DpControlledMovers/Examples/DpVar.mos\",", "AixLib.Fluid.Movers.DpControlledMovers.Examples.DpVar.statistics.log"); +Modelica.Utilities.Streams.print(" \"model\" : \"AixLib.Fluid.Movers.DpControlledMovers.Examples.DpVar\",", "AixLib.Fluid.Movers.DpControlledMovers.Examples.DpVar.statistics.log"); +Modelica.Utilities.Streams.print(" \"check\" : {", "AixLib.Fluid.Movers.DpControlledMovers.Examples.DpVar.statistics.log"); +Modelica.Utilities.Streams.print(" \"command\" : \"checkModel(\\\"AixLib.Fluid.Movers.DpControlledMovers.Examples.DpVar\\\");\",", "AixLib.Fluid.Movers.DpControlledMovers.Examples.DpVar.statistics.log"); +Modelica.Utilities.Streams.print(" \"result\" : " + String(rCheck), "AixLib.Fluid.Movers.DpControlledMovers.Examples.DpVar.statistics.log"); +Modelica.Utilities.Streams.print(" },", "AixLib.Fluid.Movers.DpControlledMovers.Examples.DpVar.statistics.log"); + + +rScript=RunScript("modelica://AixLib/Resources/Scripts/Dymola/Fluid/Movers/DpControlledMovers/Examples/DpVar.mos"); +simulateModel("AixLib.Fluid.Movers.DpControlledMovers.Examples.DpVar", startTime=0, stopTime=3600, tolerance=1e-6, method="dassl", resultFile="AixLib.Fluid.Movers.DpControlledMovers.Examples.DpVar"); +Translation of AixLib.Fluid.Movers.DpControlledMovers.Examples.DpVar +The DAE has 250 scalar unknowns and 250 scalar equations. + +Statistics + +Original Model + Number of components: 82 + Variables: 814 + Constants: 19 (19 scalars) + Parameters: 465 (949 scalars) + Unknowns: 330 (265 scalars) + Differentiated variables: 7 scalars + Equations: 284 + Nontrivial: 236 +Translated Model + Constants: 686 scalars + Free parameters: 51 scalars + Parameter depending: 271 scalars + Outputs: 1 scalars + Continuous time states: 5 scalars + Time-varying variables: 61 scalars + Alias variables: 164 scalars + Number of mixed real/discrete systems of equations: 0 + Sizes of linear systems of equations: { } + Sizes after manipulation of the linear systems: { } + Sizes of nonlinear systems of equations: {3, 1} + Sizes after manipulation of the nonlinear systems: {1, 1} + Number of numerical Jacobians: 0 + Initialization problem + Sizes of nonlinear systems of equations: {3, 1, 1} + Sizes after manipulation of the nonlinear systems: {1, 0, 1} + Sizes of simplified homotopy nonlinear systems of equations: {3, 1} + Sizes after manipulation of the simplified homotopy nonlinear systems: {1, 0} + Number of numerical Jacobians: 0 + +Selected continuous time states +Statically selected continuous time states +dpControlled_dp.mov.filter.s[1] +dpControlled_dp.mov.filter.s[2] +integrator.y +val.filter.s[1] +val.filter.s[2] +Finished +Finished + = true + + + +Declaring variable: Boolean rScript ; + +savelog("AixLib.Fluid.Movers.DpControlledMovers.Examples.DpVar.translation.log"); = true + + +rCheck = checkModel("AixLib.Fluid.BoilerCHP.Examples.CHPSystemNoControl"); +Check of AixLib.Fluid.BoilerCHP.Examples.CHPSystemNoControl +The model has the same number of unknowns and equations: 181 +The model could not be deduced to be symbolically well-posed. +The model has + 175+combinedHeatPower.vol.dynBal.nPorts+size(combinedHeatPower.combiTable1Ds.columns, 1) +scalar unknowns and + 161+size(combinedHeatPower.combiTable1Ds.columns, 1)+2*source.nPorts+(if not source.use_m_flow_in then 1 else 0)+(if not source.use_T_in then 1 else 0)+( if not source.use_X_in then 1 else 0)+2*sink.nPorts+(if not sink.use_p_in then 1 else 0)+(if not sink.use_T_in then 1 else 0)+(if not sink.use_X_in then 1 else 0)+(if not combinedHeatPower.vol.dynBal.use_mWat_flow then 1 else 0)+3*combinedHeatPower.vol.dynBal.nPorts +scalar equations. +However, exploiting the given numerical settings of parameters gives the same number of unknowns and equations: + 181 +Check of AixLib.Fluid.BoilerCHP.Examples.CHPSystemNoControl successful. +Declaring variable: Boolean rCheck ; + +Modelica.Utilities.Streams.print(" { \"file\" : \"AixLib/Resources/Scripts/Dymola/Fluid/BoilerCHP/Examples/CHPSystemNoControl.mos\",", "AixLib.Fluid.BoilerCHP.Examples.CHPSystemNoControl.statistics.log"); +Modelica.Utilities.Streams.print(" \"model\" : \"AixLib.Fluid.BoilerCHP.Examples.CHPSystemNoControl\",", "AixLib.Fluid.BoilerCHP.Examples.CHPSystemNoControl.statistics.log"); +Modelica.Utilities.Streams.print(" \"check\" : {", "AixLib.Fluid.BoilerCHP.Examples.CHPSystemNoControl.statistics.log"); +Modelica.Utilities.Streams.print(" \"command\" : \"checkModel(\\\"AixLib.Fluid.BoilerCHP.Examples.CHPSystemNoControl\\\");\",", "AixLib.Fluid.BoilerCHP.Examples.CHPSystemNoControl.statistics.log"); +Modelica.Utilities.Streams.print(" \"result\" : " + String(rCheck), "AixLib.Fluid.BoilerCHP.Examples.CHPSystemNoControl.statistics.log"); +Modelica.Utilities.Streams.print(" },", "AixLib.Fluid.BoilerCHP.Examples.CHPSystemNoControl.statistics.log"); + + +rScript=RunScript("modelica://AixLib/Resources/Scripts/Dymola/Fluid/BoilerCHP/Examples/CHPSystemNoControl.mos"); +simulateModel("AixLib.Fluid.BoilerCHP.Examples.CHPSystemNoControl", tolerance=1e-06, stopTime=300, method="dassl", resultFile="AixLib.Fluid.BoilerCHP.Examples.CHPSystemNoControl"); +Translation of AixLib.Fluid.BoilerCHP.Examples.CHPSystemNoControl +The DAE has 181 scalar unknowns and 181 scalar equations. + +Statistics + +Original Model + Number of components: 38 + Variables: 432 + Constants: 5 (5 scalars) + Parameters: 195 (229 scalars) + Unknowns: 232 (185 scalars) + Differentiated variables: 5 scalars + Equations: 210 + Nontrivial: 170 +Translated Model + Constants: 143 scalars + Free parameters: 58 scalars + Parameter depending: 71 scalars + Continuous time states: 3 scalars + Time-varying variables: 38 scalars + Alias variables: 109 scalars + Number of mixed real/discrete systems of equations: 0 + Sizes of linear systems of equations: {5} + Sizes after manipulation of the linear systems: {0} + Sizes of nonlinear systems of equations: { } + Sizes after manipulation of the nonlinear systems: { } + Number of numerical Jacobians: 0 + +Selected continuous time states +Statically selected continuous time states +combinedHeatPower.internalCapacity.T +combinedHeatPower.senTRet.T +combinedHeatPower.senTSup.T +Finished +Finished + = true + +Declaring variable: Boolean rScript ; + +savelog("AixLib.Fluid.BoilerCHP.Examples.CHPSystemNoControl.translation.log"); = true + + +rCheck = checkModel("AixLib.Fluid.Examples.GeothermalHeatPump.GeothermalHeatPump"); +Check of AixLib.Fluid.Examples.GeothermalHeatPump.GeothermalHeatPump +Warning: Redeclaration requires a subtype. + But missing component dp_start. + In redeclaration of PeakLoadDeviceModel. + File: /tmp/tmp-AixLib-2-a64q3il9/AixLib/Fluid/Examples/GeothermalHeatPump/BaseClasses/GeothermalHeatPumpBase.mo, line 20 + Context: AixLib.Fluid.Examples.GeothermalHeatPump.GeothermalHeatPump.PeakLoadDeviceModel +The model has the same number of unknowns and equations: 4699 +Check of AixLib.Fluid.Examples.GeothermalHeatPump.GeothermalHeatPump successful. +Declaring variable: Boolean rCheck ; + +Modelica.Utilities.Streams.print(" { \"file\" : \"AixLib/Resources/Scripts/Dymola/Fluid/Examples/GeothermalHeatPump/GeothermalHeatPump.mos\",", "AixLib.Fluid.Examples.GeothermalHeatPump.GeothermalHeatPump.statistics.log"); +Modelica.Utilities.Streams.print(" \"model\" : \"AixLib.Fluid.Examples.GeothermalHeatPump.GeothermalHeatPump\",", "AixLib.Fluid.Examples.GeothermalHeatPump.GeothermalHeatPump.statistics.log"); +Modelica.Utilities.Streams.print(" \"check\" : {", "AixLib.Fluid.Examples.GeothermalHeatPump.GeothermalHeatPump.statistics.log"); +Modelica.Utilities.Streams.print(" \"command\" : \"checkModel(\\\"AixLib.Fluid.Examples.GeothermalHeatPump.GeothermalHeatPump\\\");\",", "AixLib.Fluid.Examples.GeothermalHeatPump.GeothermalHeatPump.statistics.log"); +Modelica.Utilities.Streams.print(" \"result\" : " + String(rCheck), "AixLib.Fluid.Examples.GeothermalHeatPump.GeothermalHeatPump.statistics.log"); +Modelica.Utilities.Streams.print(" },", "AixLib.Fluid.Examples.GeothermalHeatPump.GeothermalHeatPump.statistics.log"); + + +rScript=RunScript("modelica://AixLib/Resources/Scripts/Dymola/Fluid/Examples/GeothermalHeatPump/GeothermalHeatPump.mos"); +simulateModel("AixLib.Fluid.Examples.GeothermalHeatPump.GeothermalHeatPump", startTime=0, stopTime=86400, method="dassl", tolerance=1e-06, resultFile="AixLib.Fluid.Examples.GeothermalHeatPump.GeothermalHeatPump"); +Translation of AixLib.Fluid.Examples.GeothermalHeatPump.GeothermalHeatPump +Warning: Redeclaration requires a subtype. + But missing component dp_start. + In redeclaration of PeakLoadDeviceModel. + File: /tmp/tmp-AixLib-2-a64q3il9/AixLib/Fluid/Examples/GeothermalHeatPump/BaseClasses/GeothermalHeatPumpBase.mo, line 20 + Context: AixLib.Fluid.Examples.GeothermalHeatPump.GeothermalHeatPump.PeakLoadDeviceModel +The DAE has 4699 scalar unknowns and 4699 scalar equations. + +Statistics + +Original Model + Number of components: 1061 + Variables: 12395 + Constants: 219 (219 scalars) + Parameters: 6093 (7317 scalars) + Unknowns: 6083 (4872 scalars) + Differentiated variables: 147 scalars + Equations: 4946 + Nontrivial: 3872 +Translated Model + Constants: 4154 scalars + Free parameters: 914 scalars + Parameter depending: 3104 scalars + Outputs: 17 scalars + Continuous time states: 109 scalars + Time-varying variables: 1171 scalars + Alias variables: 3065 scalars + Number of mixed real/discrete systems of equations: 0 + Sizes of linear systems of equations: {2, 3, 2, 2, 4, 3, 17, 2, 2, 2, 2, 2, 2, 2, 2, 3, 4, 2, 4, 3, 17, 4, 2, 2, 2, 2, 2, 2, 2, 2} + Sizes after manipulation of the linear systems: {0, 0, 0, 0, 0, 0, 8, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 8, 0, 0, 0, 0, 0, 0, 0, 0, 0} + Sizes of nonlinear systems of equations: {5, 12, 12, 5, 6, 6, 6, 3, 1, 6, 6, 6, 6, 6, 6, 6} + Sizes after manipulation of the nonlinear systems: {1, 1, 1, 1, 1, 1, 1, 0, 0, 1, 1, 1, 1, 1, 1, 1} + Number of numerical Jacobians: 0 + Initialization problem + Sizes of nonlinear systems of equations: {5, 1, 12, 1, 12, 1, 5, 1, 3, 1} + Sizes after manipulation of the nonlinear systems: {2, 0, 1, 0, 1, 0, 1, 0, 1, 0} + Sizes of simplified homotopy nonlinear systems of equations: {5, 1, 12, 1, 12, 1, 5, 1, 3, 1} + Sizes after manipulation of the simplified homotopy nonlinear systems: {2, 0, 1, 0, 1, 0, 1, 0, 1, 0} + Number of numerical Jacobians: 0 + +Sparse solvers enabled: false +Enabled for integrator Jacobian: false +Model sparse and large enough: true. +Sparse solvers are available for dassl, lsodar, cvode, ida, radau, esdirk*, sdirk*. +Enable sparse solvers by setting Advanced.Translation.SparseActivate. +Selected continuous time states +Statically selected continuous time states +coldStorage.bottomCover.loadIns.T +coldStorage.bottomCover.loadWall.T +coldStorage.heatingCoil1.pipe[1].del.x +coldStorage.heatingCoil1.pipe[1].timDel.x +coldStorage.heatingCoil1.pipe[1].vol_a.dynBal.U +coldStorage.heatingCoil1.pipe[1].vol_b.dynBal.U +coldStorage.heatingCoil1.pipe[2].del.x +coldStorage.heatingCoil1.pipe[2].timDel.x +coldStorage.heatingCoil1.pipe[2].vol_a.dynBal.U +coldStorage.heatingCoil1.pipe[2].vol_b.dynBal.U +coldStorage.heatingCoil1.pipe[3].del.x +coldStorage.heatingCoil1.pipe[3].timDel.x +coldStorage.heatingCoil1.pipe[3].vol_a.dynBal.U +coldStorage.heatingCoil1.pipe[3].vol_b.dynBal.U +coldStorage.heatingCoil1.pipe[4].del.x +coldStorage.heatingCoil1.pipe[4].timDel.x +coldStorage.heatingCoil1.pipe[4].vol_a.dynBal.U +coldStorage.heatingCoil1.pipe[4].vol_b.dynBal.U +coldStorage.heatingCoil1.pipe[5].del.x +coldStorage.heatingCoil1.pipe[5].timDel.x +coldStorage.heatingCoil1.pipe[5].vol_a.dynBal.U +coldStorage.heatingCoil1.pipe[5].vol_b.dynBal.U +coldStorage.layer[1].dynBal.U +coldStorage.layer[2].dynBal.U +coldStorage.layer[3].dynBal.U +coldStorage.layer[4].dynBal.U +coldStorage.layer[5].dynBal.U +coldStorage.storageMantle[1].Insulation.CylindricLoad1.heatCapacitor.T +coldStorage.storageMantle[1].Wall.CylindricLoad1.heatCapacitor.T +coldStorage.storageMantle[2].Insulation.CylindricLoad1.heatCapacitor.T +coldStorage.storageMantle[2].Wall.CylindricLoad1.heatCapacitor.T +coldStorage.storageMantle[3].Insulation.CylindricLoad1.heatCapacitor.T +coldStorage.storageMantle[3].Wall.CylindricLoad1.heatCapacitor.T +coldStorage.storageMantle[4].Insulation.CylindricLoad1.heatCapacitor.T +coldStorage.storageMantle[4].Wall.CylindricLoad1.heatCapacitor.T +coldStorage.storageMantle[5].Insulation.CylindricLoad1.heatCapacitor.T +coldStorage.storageMantle[5].Wall.CylindricLoad1.heatCapacitor.T +coldStorage.topCover.loadIns.T +coldStorage.topCover.loadWall.T +heatPump.con.vol.dynBal.U +heatPump.eva.vol.dynBal.U +heatStorage.bottomCover.loadIns.T +heatStorage.bottomCover.loadWall.T +heatStorage.heatingCoil1.pipe[1].del.x +heatStorage.heatingCoil1.pipe[1].timDel.x +heatStorage.heatingCoil1.pipe[1].vol_a.dynBal.U +heatStorage.heatingCoil1.pipe[1].vol_b.dynBal.U +heatStorage.heatingCoil1.pipe[2].del.x +heatStorage.heatingCoil1.pipe[2].timDel.x +heatStorage.heatingCoil1.pipe[2].vol_a.dynBal.U +heatStorage.heatingCoil1.pipe[2].vol_b.dynBal.U +heatStorage.heatingCoil1.pipe[3].del.x +heatStorage.heatingCoil1.pipe[3].timDel.x +heatStorage.heatingCoil1.pipe[3].vol_a.dynBal.U +heatStorage.heatingCoil1.pipe[3].vol_b.dynBal.U +heatStorage.heatingCoil1.pipe[4].del.x +heatStorage.heatingCoil1.pipe[4].timDel.x +heatStorage.heatingCoil1.pipe[4].vol_a.dynBal.U +heatStorage.heatingCoil1.pipe[4].vol_b.dynBal.U +heatStorage.heatingCoil1.pipe[5].del.x +heatStorage.heatingCoil1.pipe[5].timDel.x +heatStorage.heatingCoil1.pipe[5].vol_a.dynBal.U +heatStorage.heatingCoil1.pipe[5].vol_b.dynBal.U +heatStorage.layer[1].dynBal.U +heatStorage.layer[2].dynBal.U +heatStorage.layer[3].dynBal.U +heatStorage.layer[4].dynBal.U +heatStorage.layer[5].dynBal.U +heatStorage.storageMantle[1].Insulation.CylindricLoad1.heatCapacitor.T +heatStorage.storageMantle[1].Wall.CylindricLoad1.heatCapacitor.T +heatStorage.storageMantle[2].Insulation.CylindricLoad1.heatCapacitor.T +heatStorage.storageMantle[2].Wall.CylindricLoad1.heatCapacitor.T +heatStorage.storageMantle[3].Insulation.CylindricLoad1.heatCapacitor.T +heatStorage.storageMantle[3].Wall.CylindricLoad1.heatCapacitor.T +heatStorage.storageMantle[4].Insulation.CylindricLoad1.heatCapacitor.T +heatStorage.storageMantle[4].Wall.CylindricLoad1.heatCapacitor.T +heatStorage.storageMantle[5].Insulation.CylindricLoad1.heatCapacitor.T +heatStorage.storageMantle[5].Wall.CylindricLoad1.heatCapacitor.T +heatStorage.topCover.loadIns.T +heatStorage.topCover.loadWall.T +peaLoaDev.boiler.internalControl.ControlerHeater.PI.I.y +peaLoaDev.boiler.internalControl.eEnergyMeter_P.q_joule +peaLoaDev.boiler.internalControl.eEnergyMeter_S.q_joule +peaLoaDev.boiler.senTRet.T +peaLoaDev.boiler.senTSup.T +peaLoaDev.boiler.vol.dynBal.U +pumpColdConsumer.filter.s[1] +pumpColdConsumer.filter.s[2] +pumpColdConsumer.vol.dynBal.U +pumpCondenser.filter.s[1] +pumpCondenser.filter.s[2] +pumpCondenser.vol.dynBal.U +pumpEvaporator.filter.s[1] +pumpEvaporator.filter.s[2] +pumpEvaporator.vol.dynBal.U +pumpGeothermalSource.filter.s[1] +pumpGeothermalSource.filter.s[2] +pumpGeothermalSource.vol.dynBal.U +pumpHeatConsumer.filter.s[1] +pumpHeatConsumer.filter.s[2] +pumpHeatConsumer.vol.dynBal.U +valveColdStorage.filter.s[1] +valveColdStorage.filter.s[2] +valveHeatSink.filter.s[1] +valveHeatSink.filter.s[2] +valveHeatSource.filter.s[1] +valveHeatSource.filter.s[2] +valveHeatStorage.filter.s[1] +valveHeatStorage.filter.s[2] +Finished +Warning: WARNINGS have been issued. +Finished + = true + +Declaring variable: Boolean rScript ; + +savelog("AixLib.Fluid.Examples.GeothermalHeatPump.GeothermalHeatPump.translation.log"); = true + + +rCheck = checkModel("AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.PlugFlowPipeEmbedded"); +Check of AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.PlugFlowPipeEmbedded +Warning: Local "m_flow_small" conflict with inherited. Should be identical +Warning: Component m_flow_small(min = << Empty >>), + but previously m_flow_small(min = 0). + The components are not identical. + + For element m_flow_small found at + + File: /tmp/tmp-AixLib-2-a64q3il9/AixLib/Fluid/DistrictHeatingCooling/Pipes/PlugFlowPipeEmbedded.mo, line 41 + Conflict with element from + File: /tmp/tmp-AixLib-2-a64q3il9/AixLib/Fluid/Interfaces/PartialTwoPortInterface.mo, line 10 + Component context: pip + Component declared as PlugFlowPipeEmbedded pip in AixLib.Fluid.DistrictHeatingCooling.Pipes + File: /tmp/tmp-AixLib-2-a64q3il9/AixLib/Fluid/DistrictHeatingCooling/Pipes/Examples/PlugFlowPipeEmbedded.mo, line 19 +Warning: Local "m_flow_small" conflict with inherited. Should be identical +Warning: Component m_flow_small(min = << Empty >>), + but previously m_flow_small(min = 0). + The components are not identical. + + For element m_flow_small found at + + File: /tmp/tmp-AixLib-2-a64q3il9/AixLib/Fluid/DistrictHeatingCooling/Pipes/PlugFlowPipeZeta.mo, line 36 + Conflict with element from + File: /tmp/tmp-AixLib-2-a64q3il9/AixLib/Fluid/Interfaces/PartialTwoPortInterface.mo, line 10 + Component context: pip.plugFlowPipeZeta + Component declared as PlugFlowPipeZeta plugFlowPipeZeta in AixLib.Fluid.DistrictHeatingCooling.Pipes + File: /tmp/tmp-AixLib-2-a64q3il9/AixLib/Fluid/DistrictHeatingCooling/Pipes/PlugFlowPipeEmbedded.mo, line 122 +The model has the same number of unknowns and equations: 256 +The model could not be deduced to be symbolically well-posed. +The model has + 254+pip.plugFlowPipeZeta.vol.dynBal.nPorts +scalar unknowns and + 240+(if sin.use_Xi_in then 1 else (if sin.use_X_in then 0 else 1))+(if not sin.use_p_in then 1 else 0)+2*sin.nPorts+(if not sin.use_T_in then 1 else 0)+ (if sou.use_Xi_in then 1 else (if sou.use_X_in then 0 else 1))+(if not sou.use_m_flow_in then 1 else 0)+2*sou.nPorts+(if not sou.use_T_in then 1 else 0)+(if not pip.plugFlowPipeZeta.vol.dynBal.use_mWat_flow then 1 else 0) +3*pip.plugFlowPipeZeta.vol.dynBal.nPorts +scalar equations. +However, exploiting the given numerical settings of parameters gives the same number of unknowns and equations: + 256 +Check of AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.PlugFlowPipeEmbedded successful. +Declaring variable: Boolean rCheck ; + +Modelica.Utilities.Streams.print(" { \"file\" : \"AixLib/Resources/Scripts/Dymola/Fluid/DistrictHeatingCooling/Pipes/Examples/PlugFlowPipeEmbedded.mos\",", "AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.PlugFlowPipeEmbedded.statistics.log"); +Modelica.Utilities.Streams.print(" \"model\" : \"AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.PlugFlowPipeEmbedded\",", "AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.PlugFlowPipeEmbedded.statistics.log"); +Modelica.Utilities.Streams.print(" \"check\" : {", "AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.PlugFlowPipeEmbedded.statistics.log"); +Modelica.Utilities.Streams.print(" \"command\" : \"checkModel(\\\"AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.PlugFlowPipeEmbedded\\\");\",", "AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.PlugFlowPipeEmbedded.statistics.log"); +Modelica.Utilities.Streams.print(" \"result\" : " + String(rCheck), "AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.PlugFlowPipeEmbedded.statistics.log"); +Modelica.Utilities.Streams.print(" },", "AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.PlugFlowPipeEmbedded.statistics.log"); + + +rScript=RunScript("modelica://AixLib/Resources/Scripts/Dymola/Fluid/DistrictHeatingCooling/Pipes/Examples/PlugFlowPipeEmbedded.mos"); +translateModel("AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.PlugFlowPipeEmbedded"); +Translation of AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.PlugFlowPipeEmbedded +Warning: Local "m_flow_small" conflict with inherited. Should be identical +Warning: Component m_flow_small(min = << Empty >>), + but previously m_flow_small(min = 0). + The components are not identical. + + For element m_flow_small found at + + File: /tmp/tmp-AixLib-2-a64q3il9/AixLib/Fluid/DistrictHeatingCooling/Pipes/PlugFlowPipeEmbedded.mo, line 41 + Conflict with element from + File: /tmp/tmp-AixLib-2-a64q3il9/AixLib/Fluid/Interfaces/PartialTwoPortInterface.mo, line 10 + Component context: pip + Component declared as PlugFlowPipeEmbedded pip in AixLib.Fluid.DistrictHeatingCooling.Pipes + File: /tmp/tmp-AixLib-2-a64q3il9/AixLib/Fluid/DistrictHeatingCooling/Pipes/Examples/PlugFlowPipeEmbedded.mo, line 19 +Warning: Local "m_flow_small" conflict with inherited. Should be identical +Warning: Component m_flow_small(min = << Empty >>), + but previously m_flow_small(min = 0). + The components are not identical. + + For element m_flow_small found at + + File: /tmp/tmp-AixLib-2-a64q3il9/AixLib/Fluid/DistrictHeatingCooling/Pipes/PlugFlowPipeZeta.mo, line 36 + Conflict with element from + File: /tmp/tmp-AixLib-2-a64q3il9/AixLib/Fluid/Interfaces/PartialTwoPortInterface.mo, line 10 + Component context: pip.plugFlowPipeZeta + Component declared as PlugFlowPipeZeta plugFlowPipeZeta in AixLib.Fluid.DistrictHeatingCooling.Pipes + File: /tmp/tmp-AixLib-2-a64q3il9/AixLib/Fluid/DistrictHeatingCooling/Pipes/PlugFlowPipeEmbedded.mo, line 122 +The DAE has 256 scalar unknowns and 256 scalar equations. + +Statistics + +Original Model + Number of components: 53 + Variables: 739 + Constants: 11 (11 scalars) + Parameters: 390 (383 scalars) + Unknowns: 338 (264 scalars) + Differentiated variables: 9 scalars + Equations: 267 + Nontrivial: 229 +Translated Model + Constants: 224 scalars + Free parameters: 64 scalars + Parameter depending: 145 scalars + Continuous time states: 8 scalars + Time-varying variables: 57 scalars + Alias variables: 168 scalars + Number of mixed real/discrete systems of equations: 0 + Sizes of linear systems of equations: {2, 2} + Sizes after manipulation of the linear systems: {0, 0} + Sizes of nonlinear systems of equations: {6} + Sizes after manipulation of the nonlinear systems: {1} + Number of numerical Jacobians: 0 + Initialization problem + Sizes of nonlinear systems of equations: {14} + Sizes after manipulation of the nonlinear systems: {6} + Number of numerical Jacobians: 0 + +Selected continuous time states +Statically selected continuous time states +pip.cylindricHeatTransfer_1.CylindricLoad1.heatCapacitor.T +pip.cylindricHeatTransfer_2.CylindricLoad1.heatCapacitor.T +pip.cylindricHeatTransfer_3.CylindricLoad1.heatCapacitor.T +pip.plugFlowPipeZeta.plugFlowCore.del.x +pip.plugFlowPipeZeta.plugFlowCore.timDel.x +pip.plugFlowPipeZeta.vol.dynBal.U +senTemIn.T +senTemOut.T +Finished +Warning: WARNINGS have been issued. + = true +simulateModel("AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.PlugFlowPipeEmbedded", stopTime=1000, method="dassl", tolerance=1e-6, resultFile="AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.PlugFlowPipeEmbedded"); +Finished + = true + +Declaring variable: Boolean rScript ; + +savelog("AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.PlugFlowPipeEmbedded.translation.log"); = true + + +rCheck = checkModel("AixLib.Fluid.HeatExchangers.Examples.HeatingRod"); +Check of AixLib.Fluid.HeatExchangers.Examples.HeatingRod +The model has the same number of unknowns and equations: 327 +The model could not be deduced to be symbolically well-posed. +The model has + 322+vol.dynBal.nPorts+heatingRod.vol.dynBal.nPorts +scalar unknowns and + 301+(if conPI.reset <> AixLib.Types.Reset.Input then 1 else 0)+(if bou.use_Xi_in then 1 else (if bou.use_X_in then 0 else 1))+(if not bou.use_p_in then 1 else 0)+2*bou.nPorts+(if not bou.use_T_in then 1 else 0)+(if not vol.dynBal.use_mWat_flow then 1 else 0)+3*vol.dynBal.nPorts+(if not mov.vol.steBal.use_mWat_flow then 1 else 0)+(if (if conPI.reset == AixLib.Types.Reset.Disabled then conPI.reset else AixLib.Types.Reset.Input) <> AixLib.Types.Reset.Input then 1 else 0)+(if (if conPI.reset == AixLib.Types.Reset.Disabled then conPI.reset else AixLib.Types.Reset.Input) == AixLib.Types.Reset.Disabled then 1 else 0)+(if not heatingRod.vol.dynBal.use_mWat_flow then 1 else 0)+3*heatingRod.vol.dynBal.nPorts +scalar equations. +However, exploiting the given numerical settings of parameters gives the same number of unknowns and equations: + 327 +Check of AixLib.Fluid.HeatExchangers.Examples.HeatingRod successful. +Declaring variable: Boolean rCheck ; + +Modelica.Utilities.Streams.print(" { \"file\" : \"AixLib/Resources/Scripts/Dymola/Fluid/HeatExchangers/Examples/HeatingRod.mos\",", "AixLib.Fluid.HeatExchangers.Examples.HeatingRod.statistics.log"); +Modelica.Utilities.Streams.print(" \"model\" : \"AixLib.Fluid.HeatExchangers.Examples.HeatingRod\",", "AixLib.Fluid.HeatExchangers.Examples.HeatingRod.statistics.log"); +Modelica.Utilities.Streams.print(" \"check\" : {", "AixLib.Fluid.HeatExchangers.Examples.HeatingRod.statistics.log"); +Modelica.Utilities.Streams.print(" \"command\" : \"checkModel(\\\"AixLib.Fluid.HeatExchangers.Examples.HeatingRod\\\");\",", "AixLib.Fluid.HeatExchangers.Examples.HeatingRod.statistics.log"); +Modelica.Utilities.Streams.print(" \"result\" : " + String(rCheck), "AixLib.Fluid.HeatExchangers.Examples.HeatingRod.statistics.log"); +Modelica.Utilities.Streams.print(" },", "AixLib.Fluid.HeatExchangers.Examples.HeatingRod.statistics.log"); + + +rScript=RunScript("modelica://AixLib/Resources/Scripts/Dymola/Fluid/HeatExchangers/Examples/HeatingRod.mos"); +simulateModel("AixLib.Fluid.HeatExchangers.Examples.HeatingRod", stopTime=172800, method="Radau", tolerance=1e-6, resultFile="AixLib.Fluid.HeatExchangers.Examples.HeatingRod"); +Translation of AixLib.Fluid.HeatExchangers.Examples.HeatingRod +The DAE has 327 scalar unknowns and 327 scalar equations. + +Statistics + +Original Model + Number of components: 93 + Variables: 927 + Constants: 21 (21 scalars) + Parameters: 472 (578 scalars) + Unknowns: 434 (342 scalars) + Differentiated variables: 8 scalars + Equations: 376 + Nontrivial: 305 +Translated Model + Constants: 397 scalars + Free parameters: 66 scalars + Parameter depending: 209 scalars + Outputs: 2 scalars + Continuous time states: 6 scalars + Time-varying variables: 79 scalars + Alias variables: 190 scalars + Number of mixed real/discrete systems of equations: 0 + Sizes of linear systems of equations: {2} + Sizes after manipulation of the linear systems: {0} + Sizes of nonlinear systems of equations: { } + Sizes after manipulation of the nonlinear systems: { } + Number of numerical Jacobians: 0 + +Selected continuous time states +Statically selected continuous time states +conPI.I.y +heatingRod.vol.dynBal.U +mov.filter.s[1] +mov.filter.s[2] +THeaOut.T +vol.dynBal.U +Finished +Finished + = true + +Declaring variable: Boolean rScript ; + +savelog("AixLib.Fluid.HeatExchangers.Examples.HeatingRod.translation.log"); = true + + +rCheck = checkModel("AixLib.Fluid.Storage.Examples.StorageBoiler"); +Check of AixLib.Fluid.Storage.Examples.StorageBoiler +The model has the same number of unknowns and equations: 3241 +Check of AixLib.Fluid.Storage.Examples.StorageBoiler successful. +Declaring variable: Boolean rCheck ; + +Modelica.Utilities.Streams.print(" { \"file\" : \"AixLib/Resources/Scripts/Dymola/Fluid/Storage/Examples/StorageBoiler.mos\",", "AixLib.Fluid.Storage.Examples.StorageBoiler.statistics.log"); +Modelica.Utilities.Streams.print(" \"model\" : \"AixLib.Fluid.Storage.Examples.StorageBoiler\",", "AixLib.Fluid.Storage.Examples.StorageBoiler.statistics.log"); +Modelica.Utilities.Streams.print(" \"check\" : {", "AixLib.Fluid.Storage.Examples.StorageBoiler.statistics.log"); +Modelica.Utilities.Streams.print(" \"command\" : \"checkModel(\\\"AixLib.Fluid.Storage.Examples.StorageBoiler\\\");\",", "AixLib.Fluid.Storage.Examples.StorageBoiler.statistics.log"); +Modelica.Utilities.Streams.print(" \"result\" : " + String(rCheck), "AixLib.Fluid.Storage.Examples.StorageBoiler.statistics.log"); +Modelica.Utilities.Streams.print(" },", "AixLib.Fluid.Storage.Examples.StorageBoiler.statistics.log"); + + +rScript=RunScript("modelica://AixLib/Resources/Scripts/Dymola/Fluid/Storage/Examples/StorageBoiler.mos"); +simulateModel("AixLib.Fluid.Storage.Examples.StorageBoiler", tolerance=1e-6, stopTime=86400, method="dassl", resultFile="AixLib.Fluid.Storage.Examples.StorageBoiler"); +Translation of AixLib.Fluid.Storage.Examples.StorageBoiler +The DAE has 3241 scalar unknowns and 3241 scalar equations. + +Statistics + +Original Model + Number of components: 651 + Variables: 8627 + Constants: 159 (159 scalars) + Parameters: 4092 (4095 scalars) + Unknowns: 4376 (3344 scalars) + Differentiated variables: 106 scalars + Equations: 3314 + Nontrivial: 2545 +Translated Model + Constants: 2850 scalars + Free parameters: 287 scalars + Parameter depending: 1523 scalars + Continuous time states: 76 scalars + Time-varying variables: 843 scalars + Alias variables: 2095 scalars + Number of mixed real/discrete systems of equations: 0 + Sizes of linear systems of equations: {4, 3, 3, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 4, 3, 3, 2, 2, 2, 2, 2, 2, 2, 2, 2} + Sizes after manipulation of the linear systems: {0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0} + Sizes of nonlinear systems of equations: {22, 1, 6, 6, 6, 6, 6, 6, 6, 6, 6, 6, 1} + Sizes after manipulation of the nonlinear systems: {1, 0, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1} + Number of numerical Jacobians: 0 + Initialization problem + Sizes of nonlinear systems of equations: {22, 1, 1} + Sizes after manipulation of the nonlinear systems: {1, 0, 1} + Sizes of simplified homotopy nonlinear systems of equations: {22, 1} + Sizes after manipulation of the simplified homotopy nonlinear systems: {1, 0} + Number of numerical Jacobians: 0 + +Selected continuous time states +Statically selected continuous time states +bufferStorage.bottomCover.loadIns.T +bufferStorage.bottomCover.loadWall.T +bufferStorage.heatingCoil1.pipe[1].del.x +bufferStorage.heatingCoil1.pipe[1].timDel.x +bufferStorage.heatingCoil1.pipe[1].vol_a.dynBal.U +bufferStorage.heatingCoil1.pipe[1].vol_b.dynBal.U +bufferStorage.heatingCoil1.pipe[2].del.x +bufferStorage.heatingCoil1.pipe[2].timDel.x +bufferStorage.heatingCoil1.pipe[2].vol_a.dynBal.U +bufferStorage.heatingCoil1.pipe[2].vol_b.dynBal.U +bufferStorage.heatingCoil1.pipe[3].del.x +bufferStorage.heatingCoil1.pipe[3].timDel.x +bufferStorage.heatingCoil1.pipe[3].vol_a.dynBal.U +bufferStorage.heatingCoil1.pipe[3].vol_b.dynBal.U +bufferStorage.heatingCoil1.pipe[4].del.x +bufferStorage.heatingCoil1.pipe[4].timDel.x +bufferStorage.heatingCoil1.pipe[4].vol_a.dynBal.U +bufferStorage.heatingCoil1.pipe[4].vol_b.dynBal.U +bufferStorage.heatingCoil1.pipe[5].del.x +bufferStorage.heatingCoil1.pipe[5].timDel.x +bufferStorage.heatingCoil1.pipe[5].vol_a.dynBal.U +bufferStorage.heatingCoil1.pipe[5].vol_b.dynBal.U +bufferStorage.heatingCoil1.pipe[6].del.x +bufferStorage.heatingCoil1.pipe[6].timDel.x +bufferStorage.heatingCoil1.pipe[6].vol_a.dynBal.U +bufferStorage.heatingCoil1.pipe[6].vol_b.dynBal.U +bufferStorage.heatingCoil1.pipe[7].del.x +bufferStorage.heatingCoil1.pipe[7].timDel.x +bufferStorage.heatingCoil1.pipe[7].vol_a.dynBal.U +bufferStorage.heatingCoil1.pipe[7].vol_b.dynBal.U +bufferStorage.heatingCoil1.pipe[8].del.x +bufferStorage.heatingCoil1.pipe[8].timDel.x +bufferStorage.heatingCoil1.pipe[8].vol_a.dynBal.U +bufferStorage.heatingCoil1.pipe[8].vol_b.dynBal.U +bufferStorage.heatingCoil1.pipe[9].del.x +bufferStorage.heatingCoil1.pipe[9].timDel.x +bufferStorage.heatingCoil1.pipe[9].vol_a.dynBal.U +bufferStorage.heatingCoil1.pipe[9].vol_b.dynBal.U +bufferStorage.heatingCoil1.pipe[10].del.x +bufferStorage.heatingCoil1.pipe[10].timDel.x +bufferStorage.heatingCoil1.pipe[10].vol_a.dynBal.U +bufferStorage.heatingCoil1.pipe[10].vol_b.dynBal.U +bufferStorage.layer[1].dynBal.U +bufferStorage.layer[2].dynBal.U +bufferStorage.layer[3].dynBal.U +bufferStorage.layer[4].dynBal.U +bufferStorage.layer[5].dynBal.U +bufferStorage.layer[6].dynBal.U +bufferStorage.layer[7].dynBal.U +bufferStorage.layer[8].dynBal.U +bufferStorage.layer[9].dynBal.U +bufferStorage.layer[10].dynBal.U +bufferStorage.storageMantle[1].Insulation.CylindricLoad1.heatCapacitor.T +bufferStorage.storageMantle[1].Wall.CylindricLoad1.heatCapacitor.T +bufferStorage.storageMantle[2].Insulation.CylindricLoad1.heatCapacitor.T +bufferStorage.storageMantle[2].Wall.CylindricLoad1.heatCapacitor.T +bufferStorage.storageMantle[3].Insulation.CylindricLoad1.heatCapacitor.T +bufferStorage.storageMantle[3].Wall.CylindricLoad1.heatCapacitor.T +bufferStorage.storageMantle[4].Insulation.CylindricLoad1.heatCapacitor.T +bufferStorage.storageMantle[4].Wall.CylindricLoad1.heatCapacitor.T +bufferStorage.storageMantle[5].Insulation.CylindricLoad1.heatCapacitor.T +bufferStorage.storageMantle[5].Wall.CylindricLoad1.heatCapacitor.T +bufferStorage.storageMantle[6].Insulation.CylindricLoad1.heatCapacitor.T +bufferStorage.storageMantle[6].Wall.CylindricLoad1.heatCapacitor.T +bufferStorage.storageMantle[7].Insulation.CylindricLoad1.heatCapacitor.T +bufferStorage.storageMantle[7].Wall.CylindricLoad1.heatCapacitor.T +bufferStorage.storageMantle[8].Insulation.CylindricLoad1.heatCapacitor.T +bufferStorage.storageMantle[8].Wall.CylindricLoad1.heatCapacitor.T +bufferStorage.storageMantle[9].Insulation.CylindricLoad1.heatCapacitor.T +bufferStorage.storageMantle[9].Wall.CylindricLoad1.heatCapacitor.T +bufferStorage.storageMantle[10].Insulation.CylindricLoad1.heatCapacitor.T +bufferStorage.storageMantle[10].Wall.CylindricLoad1.heatCapacitor.T +bufferStorage.topCover.loadIns.T +bufferStorage.topCover.loadWall.T +pump.filter.s[1] +pump.filter.s[2] +Finished +Finished + = true + +Declaring variable: Boolean rScript ; + +savelog("AixLib.Fluid.Storage.Examples.StorageBoiler.translation.log"); = true + + +rCheck = checkModel("AixLib.Fluid.DistrictHeatingCooling.Demands.Examples.OpenLoopVarTSupplyDpFixedTempDifferenceBypass"); +Check of AixLib.Fluid.DistrictHeatingCooling.Demands.Examples.OpenLoopVarTSupplyDpFixedTempDifferenceBypass +The model has the same number of unknowns and equations: 572 +The model could not be deduced to be symbolically well-posed. +The model has + 562+demand.vol.dynBal.nPorts+pipeSupply.vol_b.dynBal.nPorts+pipeSupply.vol_a.dynBal.nPorts +pipeReturn.vol_b.dynBal.nPorts+pipeReturn.vol_a.dynBal.nPorts +scalar unknowns and + 522+(if sourceIdeal.source.use_Xi_in then 1 else (if sourceIdeal.source.use_X_in then 0 else 1))+(if not sourceIdeal.source.use_p_in then 1 else 0)+2* sourceIdeal.source.nPorts+(if not sourceIdeal.source.use_T_in then 1 else 0)+ (if sourceIdeal.sink.use_Xi_in then 1 else (if sourceIdeal.sink.use_X_in then 0 else 1))+(if not sourceIdeal.sink.use_p_in then 1 else 0)+2*sourceIdeal.sink.nPorts +(if not sourceIdeal.sink.use_T_in then 1 else 0)+(if demand.sink.use_Xi_in then 1 else (if demand.sink.use_X_in then 0 else 1))+(if not demand.sink.use_m_flow_in then 1 else 0)+2*demand.sink.nPorts+(if not demand.sink.use_T_in then 1 else 0)+(if demand.source.use_Xi_in then 1 else ( if demand.source.use_X_in then 0 else 1))+(if not demand.source.use_m_flow_in then 1 else 0)+2*demand.source.nPorts+(if not demand.source.use_T_in then 1 else 0)+(if not demand.vol.dynBal.use_mWat_flow then 1 else 0)+3* demand.vol.dynBal.nPorts+(if not pipeSupply.vol_b.dynBal.use_mWat_flow then 1 else 0)+3*pipeSupply.vol_b.dynBal.nPorts+(if not pipeSupply.vol_a.dynBal.use_mWat_flow then 1 else 0)+3*pipeSupply.vol_a.dynBal.nPorts+(if not pipeReturn.vol_b.dynBal.use_mWat_flow then 1 else 0)+3*pipeReturn.vol_b.dynBal.nPorts+(if not pipeReturn.vol_a.dynBal.use_mWat_flow then 1 else 0)+3*pipeReturn.vol_a.dynBal.nPorts +scalar equations. +However, exploiting the given numerical settings of parameters gives the same number of unknowns and equations: + 572 +Check of AixLib.Fluid.DistrictHeatingCooling.Demands.Examples.OpenLoopVarTSupplyDpFixedTempDifferenceBypass successful. +Declaring variable: Boolean rCheck ; + +Modelica.Utilities.Streams.print(" { \"file\" : \"AixLib/Resources/Scripts/Dymola/Fluid/DistrictHeatingCooling/Demands/Examples/OpenLoopVarTSupplyDpFixedTempDifferenceBypass.mos\",", "AixLib.Fluid.DistrictHeatingCooling.Demands.Examples.OpenLoopVarTSupplyDpFixedTempDifferenceBypass.statistics.log"); +Modelica.Utilities.Streams.print(" \"model\" : \"AixLib.Fluid.DistrictHeatingCooling.Demands.Examples.OpenLoopVarTSupplyDpFixedTempDifferenceBypass\",", "AixLib.Fluid.DistrictHeatingCooling.Demands.Examples.OpenLoopVarTSupplyDpFixedTempDifferenceBypass.statistics.log"); +Modelica.Utilities.Streams.print(" \"check\" : {", "AixLib.Fluid.DistrictHeatingCooling.Demands.Examples.OpenLoopVarTSupplyDpFixedTempDifferenceBypass.statistics.log"); +Modelica.Utilities.Streams.print(" \"command\" : \"checkModel(\\\"AixLib.Fluid.DistrictHeatingCooling.Demands.Examples.OpenLoopVarTSupplyDpFixedTempDifferenceBypass\\\");\",", "AixLib.Fluid.DistrictHeatingCooling.Demands.Examples.OpenLoopVarTSupplyDpFixedTempDifferenceBypass.statistics.log"); +Modelica.Utilities.Streams.print(" \"result\" : " + String(rCheck), "AixLib.Fluid.DistrictHeatingCooling.Demands.Examples.OpenLoopVarTSupplyDpFixedTempDifferenceBypass.statistics.log"); +Modelica.Utilities.Streams.print(" },", "AixLib.Fluid.DistrictHeatingCooling.Demands.Examples.OpenLoopVarTSupplyDpFixedTempDifferenceBypass.statistics.log"); + + +rScript=RunScript("modelica://AixLib/Resources/Scripts/Dymola/Fluid/DistrictHeatingCooling/Demands/Examples/OpenLoopVarTSupplyDpFixedTempDifferenceBypass.mos"); +translateModel("AixLib.Fluid.DistrictHeatingCooling.Demands.Examples.OpenLoopVarTSupplyDpFixedTempDifferenceBypass"); +Translation of AixLib.Fluid.DistrictHeatingCooling.Demands.Examples.OpenLoopVarTSupplyDpFixedTempDifferenceBypass +The DAE has 572 scalar unknowns and 572 scalar equations. + +Statistics + +Original Model + Number of components: 114 + Variables: 1506 + Constants: 29 (29 scalars) + Parameters: 675 (646 scalars) + Unknowns: 802 (590 scalars) + Differentiated variables: 17 scalars + Equations: 680 + Nontrivial: 543 +Translated Model + Constants: 509 scalars + Free parameters: 121 scalars + Parameter depending: 138 scalars + Continuous time states: 12 scalars + Time-varying variables: 132 scalars + Alias variables: 365 scalars + Number of mixed real/discrete systems of equations: 0 + Sizes of linear systems of equations: { } + Sizes after manipulation of the linear systems: { } + Sizes of nonlinear systems of equations: {8} + Sizes after manipulation of the nonlinear systems: {1} + Number of numerical Jacobians: 0 + Initialization problem + Sizes of nonlinear systems of equations: {8} + Sizes after manipulation of the nonlinear systems: {1} + Number of numerical Jacobians: 0 + +Selected continuous time states +Statically selected continuous time states +demand.senT_return.T +demand.senT_supply.T +demand.vol.dynBal.U +pControl.I.y +pipeReturn.del.x +pipeReturn.timDel.x +pipeReturn.vol_a.dynBal.U +pipeReturn.vol_b.dynBal.U +pipeSupply.del.x +pipeSupply.timDel.x +pipeSupply.vol_a.dynBal.U +pipeSupply.vol_b.dynBal.U +Finished + = true +simulateModel("AixLib.Fluid.DistrictHeatingCooling.Demands.Examples.OpenLoopVarTSupplyDpFixedTempDifferenceBypass", stopTime=100000, method="dassl", tolerance=1e-006, resultFile="AixLib.Fluid.DistrictHeatingCooling.Demands.Examples.OpenLoopVarTSupplyDpFixedTempDifferenceBypass"); +Finished +Finished + = true + +Declaring variable: Boolean rScript ; + +savelog("AixLib.Fluid.DistrictHeatingCooling.Demands.Examples.OpenLoopVarTSupplyDpFixedTempDifferenceBypass.translation.log"); = true + + +rCheck = checkModel("AixLib.Fluid.Storage.Examples.StorageSolarCollector"); +Check of AixLib.Fluid.Storage.Examples.StorageSolarCollector +The model has the same number of unknowns and equations: 3387 +Check of AixLib.Fluid.Storage.Examples.StorageSolarCollector successful. +Declaring variable: Boolean rCheck ; + +Modelica.Utilities.Streams.print(" { \"file\" : \"AixLib/Resources/Scripts/Dymola/Fluid/Storage/Examples/StorageSolarCollector.mos\",", "AixLib.Fluid.Storage.Examples.StorageSolarCollector.statistics.log"); +Modelica.Utilities.Streams.print(" \"model\" : \"AixLib.Fluid.Storage.Examples.StorageSolarCollector\",", "AixLib.Fluid.Storage.Examples.StorageSolarCollector.statistics.log"); +Modelica.Utilities.Streams.print(" \"check\" : {", "AixLib.Fluid.Storage.Examples.StorageSolarCollector.statistics.log"); +Modelica.Utilities.Streams.print(" \"command\" : \"checkModel(\\\"AixLib.Fluid.Storage.Examples.StorageSolarCollector\\\");\",", "AixLib.Fluid.Storage.Examples.StorageSolarCollector.statistics.log"); +Modelica.Utilities.Streams.print(" \"result\" : " + String(rCheck), "AixLib.Fluid.Storage.Examples.StorageSolarCollector.statistics.log"); +Modelica.Utilities.Streams.print(" },", "AixLib.Fluid.Storage.Examples.StorageSolarCollector.statistics.log"); + + +rScript=RunScript("modelica://AixLib/Resources/Scripts/Dymola/Fluid/Storage/Examples/StorageSolarCollector.mos"); +simulateModel("AixLib.Fluid.Storage.Examples.StorageSolarCollector", tolerance=1e-6, stopTime=172800, method="dassl", resultFile="AixLib.Fluid.Storage.Examples.StorageSolarCollector"); +Translation of AixLib.Fluid.Storage.Examples.StorageSolarCollector +The DAE has 3387 scalar unknowns and 3387 scalar equations. + +Statistics + +Original Model + Number of components: 688 + Variables: 8995 + Constants: 163 (163 scalars) + Parameters: 4276 (4349 scalars) + Unknowns: 4556 (3492 scalars) + Differentiated variables: 114 scalars + Equations: 3534 + Nontrivial: 2710 +Translated Model + Constants: 2919 scalars + Free parameters: 421 scalars + Parameter depending: 1578 scalars + Continuous time states: 83 scalars + Time-varying variables: 870 scalars + Alias variables: 2216 scalars + Number of mixed real/discrete systems of equations: 0 + Sizes of linear systems of equations: {4, 3, 3, 2, 2, 2, 4, 3, 3, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2} + Sizes after manipulation of the linear systems: {0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0} + Sizes of nonlinear systems of equations: {24, 1, 6, 6, 6, 6, 6, 6, 6, 6, 6, 6} + Sizes after manipulation of the nonlinear systems: {1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1} + Number of numerical Jacobians: 0 + Initialization problem + Sizes of nonlinear systems of equations: {24, 1, 1} + Sizes after manipulation of the nonlinear systems: {1, 0, 1} + Sizes of simplified homotopy nonlinear systems of equations: {24, 1} + Sizes after manipulation of the simplified homotopy nonlinear systems: {1, 0} + Number of numerical Jacobians: 0 + +Selected continuous time states +Statically selected continuous time states +bufferStorage.bottomCover.loadIns.T +bufferStorage.bottomCover.loadWall.T +bufferStorage.heatingCoil1.pipe[1].del.x +bufferStorage.heatingCoil1.pipe[1].timDel.x +bufferStorage.heatingCoil1.pipe[1].vol_a.dynBal.U +bufferStorage.heatingCoil1.pipe[1].vol_b.dynBal.U +bufferStorage.heatingCoil1.pipe[2].del.x +bufferStorage.heatingCoil1.pipe[2].timDel.x +bufferStorage.heatingCoil1.pipe[2].vol_a.dynBal.U +bufferStorage.heatingCoil1.pipe[2].vol_b.dynBal.U +bufferStorage.heatingCoil1.pipe[3].del.x +bufferStorage.heatingCoil1.pipe[3].timDel.x +bufferStorage.heatingCoil1.pipe[3].vol_a.dynBal.U +bufferStorage.heatingCoil1.pipe[3].vol_b.dynBal.U +bufferStorage.heatingCoil1.pipe[4].del.x +bufferStorage.heatingCoil1.pipe[4].timDel.x +bufferStorage.heatingCoil1.pipe[4].vol_a.dynBal.U +bufferStorage.heatingCoil1.pipe[4].vol_b.dynBal.U +bufferStorage.heatingCoil1.pipe[5].del.x +bufferStorage.heatingCoil1.pipe[5].timDel.x +bufferStorage.heatingCoil1.pipe[5].vol_a.dynBal.U +bufferStorage.heatingCoil1.pipe[5].vol_b.dynBal.U +bufferStorage.heatingCoil1.pipe[6].del.x +bufferStorage.heatingCoil1.pipe[6].timDel.x +bufferStorage.heatingCoil1.pipe[6].vol_a.dynBal.U +bufferStorage.heatingCoil1.pipe[6].vol_b.dynBal.U +bufferStorage.heatingCoil1.pipe[7].del.x +bufferStorage.heatingCoil1.pipe[7].timDel.x +bufferStorage.heatingCoil1.pipe[7].vol_a.dynBal.U +bufferStorage.heatingCoil1.pipe[7].vol_b.dynBal.U +bufferStorage.heatingCoil1.pipe[8].del.x +bufferStorage.heatingCoil1.pipe[8].timDel.x +bufferStorage.heatingCoil1.pipe[8].vol_a.dynBal.U +bufferStorage.heatingCoil1.pipe[8].vol_b.dynBal.U +bufferStorage.heatingCoil1.pipe[9].del.x +bufferStorage.heatingCoil1.pipe[9].timDel.x +bufferStorage.heatingCoil1.pipe[9].vol_a.dynBal.U +bufferStorage.heatingCoil1.pipe[9].vol_b.dynBal.U +bufferStorage.heatingCoil1.pipe[10].del.x +bufferStorage.heatingCoil1.pipe[10].timDel.x +bufferStorage.heatingCoil1.pipe[10].vol_a.dynBal.U +bufferStorage.heatingCoil1.pipe[10].vol_b.dynBal.U +bufferStorage.layer[1].dynBal.U +bufferStorage.layer[2].dynBal.U +bufferStorage.layer[3].dynBal.U +bufferStorage.layer[4].dynBal.U +bufferStorage.layer[5].dynBal.U +bufferStorage.layer[6].dynBal.U +bufferStorage.layer[7].dynBal.U +bufferStorage.layer[8].dynBal.U +bufferStorage.layer[9].dynBal.U +bufferStorage.layer[10].dynBal.U +bufferStorage.storageMantle[1].Insulation.CylindricLoad1.heatCapacitor.T +bufferStorage.storageMantle[1].Wall.CylindricLoad1.heatCapacitor.T +bufferStorage.storageMantle[2].Insulation.CylindricLoad1.heatCapacitor.T +bufferStorage.storageMantle[2].Wall.CylindricLoad1.heatCapacitor.T +bufferStorage.storageMantle[3].Insulation.CylindricLoad1.heatCapacitor.T +bufferStorage.storageMantle[3].Wall.CylindricLoad1.heatCapacitor.T +bufferStorage.storageMantle[4].Insulation.CylindricLoad1.heatCapacitor.T +bufferStorage.storageMantle[4].Wall.CylindricLoad1.heatCapacitor.T +bufferStorage.storageMantle[5].Insulation.CylindricLoad1.heatCapacitor.T +bufferStorage.storageMantle[5].Wall.CylindricLoad1.heatCapacitor.T +bufferStorage.storageMantle[6].Insulation.CylindricLoad1.heatCapacitor.T +bufferStorage.storageMantle[6].Wall.CylindricLoad1.heatCapacitor.T +bufferStorage.storageMantle[7].Insulation.CylindricLoad1.heatCapacitor.T +bufferStorage.storageMantle[7].Wall.CylindricLoad1.heatCapacitor.T +bufferStorage.storageMantle[8].Insulation.CylindricLoad1.heatCapacitor.T +bufferStorage.storageMantle[8].Wall.CylindricLoad1.heatCapacitor.T +bufferStorage.storageMantle[9].Insulation.CylindricLoad1.heatCapacitor.T +bufferStorage.storageMantle[9].Wall.CylindricLoad1.heatCapacitor.T +bufferStorage.storageMantle[10].Insulation.CylindricLoad1.heatCapacitor.T +bufferStorage.storageMantle[10].Wall.CylindricLoad1.heatCapacitor.T +bufferStorage.topCover.loadIns.T +bufferStorage.topCover.loadWall.T +PI.I.y +pump.filter.s[1] +pump.filter.s[2] +solarThermal.senTRet.T +solarThermal.senTSup.T +solarThermal.vol.dynBal.U +temperatureSensor.T +valve.filter.s[1] +valve.filter.s[2] +Finished +Finished + = true + +Declaring variable: Boolean rScript ; + +savelog("AixLib.Fluid.Storage.Examples.StorageSolarCollector.translation.log"); = true + + +rCheck = checkModel("AixLib.Fluid.MassExchangers.MembraneBasedEnthalpyExchangers.Examples.Test_EnthalpyExchanger"); +Check of AixLib.Fluid.MassExchangers.MembraneBasedEnthalpyExchangers.Examples.Test_EnthalpyExchanger +The model has the same number of unknowns and equations: 5083 +The model could not be deduced to be symbolically well-posed. +The model has + 3373+32*enthalpyExchanger.n+16*enthalpyExchanger.airDuct2.heatTransfer.n+18* enthalpyExchanger.airDuct2.massTransfer.n+16*enthalpyExchanger.airDuct1.heatTransfer.n +18*enthalpyExchanger.airDuct1.massTransfer.n+5*enthalpyExchanger.membrane.heatTransfer.n +enthalpyExchanger.membrane.massTransfer.n+2*enthalpyExchanger.airDuct2.vol[1].dynBal.nPorts +2*enthalpyExchanger.airDuct2.vol[2].dynBal.nPorts+2*enthalpyExchanger.airDuct2.vol[3].dynBal.nPorts +2*enthalpyExchanger.airDuct2.vol[4].dynBal.nPorts+2*enthalpyExchanger.airDuct2.vol[5].dynBal.nPorts +2*enthalpyExchanger.airDuct2.vol[6].dynBal.nPorts+2*enthalpyExchanger.airDuct2.vol[7].dynBal.nPorts +2*enthalpyExchanger.airDuct2.vol[8].dynBal.nPorts+2*enthalpyExchanger.airDuct2.vol[9].dynBal.nPorts +2*enthalpyExchanger.airDuct2.vol[10].dynBal.nPorts+2*enthalpyExchanger.airDuct2.vol[11].dynBal.nPorts +2*enthalpyExchanger.airDuct2.vol[12].dynBal.nPorts+2*enthalpyExchanger.airDuct2.vol[13].dynBal.nPorts +2*enthalpyExchanger.airDuct2.vol[14].dynBal.nPorts+2*enthalpyExchanger.airDuct2.vol[15].dynBal.nPorts +2*enthalpyExchanger.airDuct1.vol[1].dynBal.nPorts+2*enthalpyExchanger.airDuct1.vol[2].dynBal.nPorts +2*enthalpyExchanger.airDuct1.vol[3].dynBal.nPorts+2*enthalpyExchanger.airDuct1.vol[4].dynBal.nPorts +2*enthalpyExchanger.airDuct1.vol[5].dynBal.nPorts+2*enthalpyExchanger.airDuct1.vol[6].dynBal.nPorts +2*enthalpyExchanger.airDuct1.vol[7].dynBal.nPorts+2*enthalpyExchanger.airDuct1.vol[8].dynBal.nPorts +2*enthalpyExchanger.airDuct1.vol[9].dynBal.nPorts+2*enthalpyExchanger.airDuct1.vol[10].dynBal.nPorts +2*enthalpyExchanger.airDuct1.vol[11].dynBal.nPorts+2*enthalpyExchanger.airDuct1.vol[12].dynBal.nPorts +2*enthalpyExchanger.airDuct1.vol[13].dynBal.nPorts+2*enthalpyExchanger.airDuct1.vol[14].dynBal.nPorts +2*enthalpyExchanger.airDuct1.vol[15].dynBal.nPorts +scalar unknowns and + 3043+17*enthalpyExchanger.airDuct2.heatTransfer.n+19*enthalpyExchanger.airDuct2.massTransfer.n +3*(if enthalpyExchanger.couFloArr then 2*enthalpyExchanger.n else 0)+17* enthalpyExchanger.airDuct1.heatTransfer.n+19*enthalpyExchanger.airDuct1.massTransfer.n +7*enthalpyExchanger.membrane.heatTransfer.n+3*enthalpyExchanger.membrane.massTransfer.n +2*(if enthalpyExchanger.useConPer then 1 else 0)+32*enthalpyExchanger.n+(if souAirHot.use_Xi_in then 2 else (if souAirHot.use_X_in then 1 else 3))+3* souAirHot.nPorts+(if not souAirHot.use_p_in then 1 else 0)+(if not souAirHot.use_T_in then 1 else 0)+(if sinAirHot.use_Xi_in then 2 else (if sinAirHot.use_X_in then 1 else 3))+3*sinAirHot.nPorts+(if not sinAirHot.use_p_in then 1 else 0)+(if not sinAirHot.use_T_in then 1 else 0)+( if souAirCol.use_Xi_in then 2 else (if souAirCol.use_X_in then 1 else 3))+3* souAirCol.nPorts+(if not souAirCol.use_p_in then 1 else 0)+(if not souAirCol.use_T_in then 1 else 0)+(if sinAirCol.use_Xi_in then 2 else (if sinAirCol.use_X_in then 1 else 3))+3*sinAirCol.nPorts+(if not sinAirCol.use_p_in then 1 else 0)+(if not sinAirCol.use_T_in then 1 else 0)+5 *enthalpyExchanger.airDuct2.vol[1].dynBal.nPorts+5*enthalpyExchanger.airDuct2.vol[2].dynBal.nPorts +5*enthalpyExchanger.airDuct2.vol[3].dynBal.nPorts+5*enthalpyExchanger.airDuct2.vol[4].dynBal.nPorts +5*enthalpyExchanger.airDuct2.vol[5].dynBal.nPorts+5*enthalpyExchanger.airDuct2.vol[6].dynBal.nPorts +5*enthalpyExchanger.airDuct2.vol[7].dynBal.nPorts+5*enthalpyExchanger.airDuct2.vol[8].dynBal.nPorts +5*enthalpyExchanger.airDuct2.vol[9].dynBal.nPorts+5*enthalpyExchanger.airDuct2.vol[10].dynBal.nPorts +5*enthalpyExchanger.airDuct2.vol[11].dynBal.nPorts+5*enthalpyExchanger.airDuct2.vol[12].dynBal.nPorts +5*enthalpyExchanger.airDuct2.vol[13].dynBal.nPorts+5*enthalpyExchanger.airDuct2.vol[14].dynBal.nPorts +5*enthalpyExchanger.airDuct2.vol[15].dynBal.nPorts+5*enthalpyExchanger.airDuct1.vol[1].dynBal.nPorts +5*enthalpyExchanger.airDuct1.vol[2].dynBal.nPorts+5*enthalpyExchanger.airDuct1.vol[3].dynBal.nPorts +5*enthalpyExchanger.airDuct1.vol[4].dynBal.nPorts+5*enthalpyExchanger.airDuct1.vol[5].dynBal.nPorts +5*enthalpyExchanger.airDuct1.vol[6].dynBal.nPorts+5*enthalpyExchanger.airDuct1.vol[7].dynBal.nPorts +5*enthalpyExchanger.airDuct1.vol[8].dynBal.nPorts+5*enthalpyExchanger.airDuct1.vol[9].dynBal.nPorts +5*enthalpyExchanger.airDuct1.vol[10].dynBal.nPorts+5*enthalpyExchanger.airDuct1.vol[11].dynBal.nPorts +5*enthalpyExchanger.airDuct1.vol[12].dynBal.nPorts+5*enthalpyExchanger.airDuct1.vol[13].dynBal.nPorts +5*enthalpyExchanger.airDuct1.vol[14].dynBal.nPorts+5*enthalpyExchanger.airDuct1.vol[15].dynBal.nPorts +scalar equations. +However, exploiting the given numerical settings of parameters gives the same number of unknowns and equations: + 5083 +Check of AixLib.Fluid.MassExchangers.MembraneBasedEnthalpyExchangers.Examples.Test_EnthalpyExchanger successful. +Declaring variable: Boolean rCheck ; + +Modelica.Utilities.Streams.print(" { \"file\" : \"AixLib/Resources/Scripts/Dymola/Fluid/MassExchangers/MembraneBasedEnthalpyExchangers/Examples/Test_EnthalpyExchanger.mos\",", "AixLib.Fluid.MassExchangers.MembraneBasedEnthalpyExchangers.Examples.Test_EnthalpyExchanger.statistics.log"); +Modelica.Utilities.Streams.print(" \"model\" : \"AixLib.Fluid.MassExchangers.MembraneBasedEnthalpyExchangers.Examples.Test_EnthalpyExchanger\",", "AixLib.Fluid.MassExchangers.MembraneBasedEnthalpyExchangers.Examples.Test_EnthalpyExchanger.statistics.log"); +Modelica.Utilities.Streams.print(" \"check\" : {", "AixLib.Fluid.MassExchangers.MembraneBasedEnthalpyExchangers.Examples.Test_EnthalpyExchanger.statistics.log"); +Modelica.Utilities.Streams.print(" \"command\" : \"checkModel(\\\"AixLib.Fluid.MassExchangers.MembraneBasedEnthalpyExchangers.Examples.Test_EnthalpyExchanger\\\");\",", "AixLib.Fluid.MassExchangers.MembraneBasedEnthalpyExchangers.Examples.Test_EnthalpyExchanger.statistics.log"); +Modelica.Utilities.Streams.print(" \"result\" : " + String(rCheck), "AixLib.Fluid.MassExchangers.MembraneBasedEnthalpyExchangers.Examples.Test_EnthalpyExchanger.statistics.log"); +Modelica.Utilities.Streams.print(" },", "AixLib.Fluid.MassExchangers.MembraneBasedEnthalpyExchangers.Examples.Test_EnthalpyExchanger.statistics.log"); + + +rScript=RunScript("modelica://AixLib/Resources/Scripts/Dymola/Fluid/MassExchangers/MembraneBasedEnthalpyExchangers/Examples/Test_EnthalpyExchanger.mos"); +simulateModel("AixLib.Fluid.MassExchangers.MembraneBasedEnthalpyExchangers.Examples.Test_EnthalpyExchanger", stopTime=7200, outputInterval=10, method="dassl", tolerance=1e-6, resultFile="AixLib.Fluid.MassExchangers.MembraneBasedEnthalpyExchangers.Examples.Test_EnthalpyExchanger"); +Translation of AixLib.Fluid.MassExchangers.MembraneBasedEnthalpyExchangers.Examples.Test_EnthalpyExchanger +The DAE has 5083 scalar unknowns and 5083 scalar equations. +Redundant consistent initial conditions. +Removed the following equations which are redundant and consistent: + if (enthalpyExchanger.airDuct2.vol[1].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (enthalpyExchanger.airDuct2.vol[1].dynBal.initialize_p) then + enthalpyExchanger.airDuct2.vol[1].dynBal.medium.p = enthalpyExchanger.airDuct2.vol[1].dynBal.p_start; + end if; + else + if (enthalpyExchanger.airDuct2.vol[1].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then + if (enthalpyExchanger.airDuct2.vol[1].dynBal.initialize_p) then + der(enthalpyExchanger.airDuct2.vol[1].dynBal.medium.p) = 0; + end if; + end if; + end if; + if (enthalpyExchanger.airDuct2.vol[2].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (enthalpyExchanger.airDuct2.vol[2].dynBal.initialize_p) then + enthalpyExchanger.airDuct2.vol[2].dynBal.medium.p = enthalpyExchanger.airDuct2.vol[2].dynBal.p_start; + end if; + else + if (enthalpyExchanger.airDuct2.vol[2].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then + if (enthalpyExchanger.airDuct2.vol[2].dynBal.initialize_p) then + der(enthalpyExchanger.airDuct2.vol[2].dynBal.medium.p) = 0; + end if; + end if; + end if; + if (enthalpyExchanger.airDuct2.vol[3].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (enthalpyExchanger.airDuct2.vol[3].dynBal.initialize_p) then + enthalpyExchanger.airDuct2.vol[3].dynBal.medium.p = enthalpyExchanger.airDuct2.vol[3].dynBal.p_start; + end if; + else + if (enthalpyExchanger.airDuct2.vol[3].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then + if (enthalpyExchanger.airDuct2.vol[3].dynBal.initialize_p) then + der(enthalpyExchanger.airDuct2.vol[3].dynBal.medium.p) = 0; + end if; + end if; + end if; + if (enthalpyExchanger.airDuct2.vol[4].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (enthalpyExchanger.airDuct2.vol[4].dynBal.initialize_p) then + enthalpyExchanger.airDuct2.vol[4].dynBal.medium.p = enthalpyExchanger.airDuct2.vol[4].dynBal.p_start; + end if; + else + if (enthalpyExchanger.airDuct2.vol[4].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then + if (enthalpyExchanger.airDuct2.vol[4].dynBal.initialize_p) then + der(enthalpyExchanger.airDuct2.vol[4].dynBal.medium.p) = 0; + end if; + end if; + end if; + if (enthalpyExchanger.airDuct2.vol[5].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (enthalpyExchanger.airDuct2.vol[5].dynBal.initialize_p) then + enthalpyExchanger.airDuct2.vol[5].dynBal.medium.p = enthalpyExchanger.airDuct2.vol[5].dynBal.p_start; + end if; + else + if (enthalpyExchanger.airDuct2.vol[5].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then + if (enthalpyExchanger.airDuct2.vol[5].dynBal.initialize_p) then + der(enthalpyExchanger.airDuct2.vol[5].dynBal.medium.p) = 0; + end if; + end if; + end if; + if (enthalpyExchanger.airDuct2.vol[6].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (enthalpyExchanger.airDuct2.vol[6].dynBal.initialize_p) then + enthalpyExchanger.airDuct2.vol[6].dynBal.medium.p = enthalpyExchanger.airDuct2.vol[6].dynBal.p_start; + end if; + else + if (enthalpyExchanger.airDuct2.vol[6].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then + if (enthalpyExchanger.airDuct2.vol[6].dynBal.initialize_p) then + der(enthalpyExchanger.airDuct2.vol[6].dynBal.medium.p) = 0; + end if; + end if; + end if; + if (enthalpyExchanger.airDuct2.vol[7].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (enthalpyExchanger.airDuct2.vol[7].dynBal.initialize_p) then + enthalpyExchanger.airDuct2.vol[7].dynBal.medium.p = enthalpyExchanger.airDuct2.vol[7].dynBal.p_start; + end if; + else + if (enthalpyExchanger.airDuct2.vol[7].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then + if (enthalpyExchanger.airDuct2.vol[7].dynBal.initialize_p) then + der(enthalpyExchanger.airDuct2.vol[7].dynBal.medium.p) = 0; + end if; + end if; + end if; + if (enthalpyExchanger.airDuct2.vol[8].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (enthalpyExchanger.airDuct2.vol[8].dynBal.initialize_p) then + enthalpyExchanger.airDuct2.vol[8].dynBal.medium.p = enthalpyExchanger.airDuct2.vol[8].dynBal.p_start; + end if; + else + if (enthalpyExchanger.airDuct2.vol[8].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then + if (enthalpyExchanger.airDuct2.vol[8].dynBal.initialize_p) then + der(enthalpyExchanger.airDuct2.vol[8].dynBal.medium.p) = 0; + end if; + end if; + end if; + if (enthalpyExchanger.airDuct2.vol[9].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (enthalpyExchanger.airDuct2.vol[9].dynBal.initialize_p) then + enthalpyExchanger.airDuct2.vol[9].dynBal.medium.p = enthalpyExchanger.airDuct2.vol[9].dynBal.p_start; + end if; + else + if (enthalpyExchanger.airDuct2.vol[9].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then + if (enthalpyExchanger.airDuct2.vol[9].dynBal.initialize_p) then + der(enthalpyExchanger.airDuct2.vol[9].dynBal.medium.p) = 0; + end if; + end if; + end if; + if (enthalpyExchanger.airDuct2.vol[10].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (enthalpyExchanger.airDuct2.vol[10].dynBal.initialize_p) then + enthalpyExchanger.airDuct2.vol[10].dynBal.medium.p = enthalpyExchanger.airDuct2.vol[10].dynBal.p_start; + end if; + else + if (enthalpyExchanger.airDuct2.vol[10].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then + if (enthalpyExchanger.airDuct2.vol[10].dynBal.initialize_p) then + der(enthalpyExchanger.airDuct2.vol[10].dynBal.medium.p) = 0; + end if; + end if; + end if; + if (enthalpyExchanger.airDuct2.vol[11].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (enthalpyExchanger.airDuct2.vol[11].dynBal.initialize_p) then + enthalpyExchanger.airDuct2.vol[11].dynBal.medium.p = enthalpyExchanger.airDuct2.vol[11].dynBal.p_start; + end if; + else + if (enthalpyExchanger.airDuct2.vol[11].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then + if (enthalpyExchanger.airDuct2.vol[11].dynBal.initialize_p) then + der(enthalpyExchanger.airDuct2.vol[11].dynBal.medium.p) = 0; + end if; + end if; + end if; + if (enthalpyExchanger.airDuct2.vol[12].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (enthalpyExchanger.airDuct2.vol[12].dynBal.initialize_p) then + enthalpyExchanger.airDuct2.vol[12].dynBal.medium.p = enthalpyExchanger.airDuct2.vol[12].dynBal.p_start; + end if; + else + if (enthalpyExchanger.airDuct2.vol[12].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then + if (enthalpyExchanger.airDuct2.vol[12].dynBal.initialize_p) then + der(enthalpyExchanger.airDuct2.vol[12].dynBal.medium.p) = 0; + end if; + end if; + end if; + if (enthalpyExchanger.airDuct2.vol[13].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (enthalpyExchanger.airDuct2.vol[13].dynBal.initialize_p) then + enthalpyExchanger.airDuct2.vol[13].dynBal.medium.p = enthalpyExchanger.airDuct2.vol[13].dynBal.p_start; + end if; + else + if (enthalpyExchanger.airDuct2.vol[13].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then + if (enthalpyExchanger.airDuct2.vol[13].dynBal.initialize_p) then + der(enthalpyExchanger.airDuct2.vol[13].dynBal.medium.p) = 0; + end if; + end if; + end if; + if (enthalpyExchanger.airDuct2.vol[14].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (enthalpyExchanger.airDuct2.vol[14].dynBal.initialize_p) then + enthalpyExchanger.airDuct2.vol[14].dynBal.medium.p = enthalpyExchanger.airDuct2.vol[14].dynBal.p_start; + end if; + else + if (enthalpyExchanger.airDuct2.vol[14].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then + if (enthalpyExchanger.airDuct2.vol[14].dynBal.initialize_p) then + der(enthalpyExchanger.airDuct2.vol[14].dynBal.medium.p) = 0; + end if; + end if; + end if; + if (enthalpyExchanger.airDuct2.vol[15].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (enthalpyExchanger.airDuct2.vol[15].dynBal.initialize_p) then + enthalpyExchanger.airDuct2.vol[15].dynBal.medium.p = enthalpyExchanger.airDuct2.vol[15].dynBal.p_start; + end if; + else + if (enthalpyExchanger.airDuct2.vol[15].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then + if (enthalpyExchanger.airDuct2.vol[15].dynBal.initialize_p) then + der(enthalpyExchanger.airDuct2.vol[15].dynBal.medium.p) = 0; + end if; + end if; + end if; + if (enthalpyExchanger.airDuct1.vol[1].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (enthalpyExchanger.airDuct1.vol[1].dynBal.initialize_p) then + enthalpyExchanger.airDuct1.vol[1].dynBal.medium.p = enthalpyExchanger.airDuct1.vol[1].dynBal.p_start; + end if; + else + if (enthalpyExchanger.airDuct1.vol[1].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then + if (enthalpyExchanger.airDuct1.vol[1].dynBal.initialize_p) then + der(enthalpyExchanger.airDuct1.vol[1].dynBal.medium.p) = 0; + end if; + end if; + end if; + if (enthalpyExchanger.airDuct1.vol[2].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (enthalpyExchanger.airDuct1.vol[2].dynBal.initialize_p) then + enthalpyExchanger.airDuct1.vol[2].dynBal.medium.p = enthalpyExchanger.airDuct1.vol[2].dynBal.p_start; + end if; + else + if (enthalpyExchanger.airDuct1.vol[2].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then + if (enthalpyExchanger.airDuct1.vol[2].dynBal.initialize_p) then + der(enthalpyExchanger.airDuct1.vol[2].dynBal.medium.p) = 0; + end if; + end if; + end if; + if (enthalpyExchanger.airDuct1.vol[3].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (enthalpyExchanger.airDuct1.vol[3].dynBal.initialize_p) then + enthalpyExchanger.airDuct1.vol[3].dynBal.medium.p = enthalpyExchanger.airDuct1.vol[3].dynBal.p_start; + end if; + else + if (enthalpyExchanger.airDuct1.vol[3].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then + if (enthalpyExchanger.airDuct1.vol[3].dynBal.initialize_p) then + der(enthalpyExchanger.airDuct1.vol[3].dynBal.medium.p) = 0; + end if; + end if; + end if; + if (enthalpyExchanger.airDuct1.vol[4].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (enthalpyExchanger.airDuct1.vol[4].dynBal.initialize_p) then + enthalpyExchanger.airDuct1.vol[4].dynBal.medium.p = enthalpyExchanger.airDuct1.vol[4].dynBal.p_start; + end if; + else + if (enthalpyExchanger.airDuct1.vol[4].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then + if (enthalpyExchanger.airDuct1.vol[4].dynBal.initialize_p) then + der(enthalpyExchanger.airDuct1.vol[4].dynBal.medium.p) = 0; + end if; + end if; + end if; + if (enthalpyExchanger.airDuct1.vol[5].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (enthalpyExchanger.airDuct1.vol[5].dynBal.initialize_p) then + enthalpyExchanger.airDuct1.vol[5].dynBal.medium.p = enthalpyExchanger.airDuct1.vol[5].dynBal.p_start; + end if; + else + if (enthalpyExchanger.airDuct1.vol[5].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then + if (enthalpyExchanger.airDuct1.vol[5].dynBal.initialize_p) then + der(enthalpyExchanger.airDuct1.vol[5].dynBal.medium.p) = 0; + end if; + end if; + end if; + if (enthalpyExchanger.airDuct1.vol[6].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (enthalpyExchanger.airDuct1.vol[6].dynBal.initialize_p) then + enthalpyExchanger.airDuct1.vol[6].dynBal.medium.p = enthalpyExchanger.airDuct1.vol[6].dynBal.p_start; + end if; + else + if (enthalpyExchanger.airDuct1.vol[6].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then + if (enthalpyExchanger.airDuct1.vol[6].dynBal.initialize_p) then + der(enthalpyExchanger.airDuct1.vol[6].dynBal.medium.p) = 0; + end if; + end if; + end if; + if (enthalpyExchanger.airDuct1.vol[7].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (enthalpyExchanger.airDuct1.vol[7].dynBal.initialize_p) then + enthalpyExchanger.airDuct1.vol[7].dynBal.medium.p = enthalpyExchanger.airDuct1.vol[7].dynBal.p_start; + end if; + else + if (enthalpyExchanger.airDuct1.vol[7].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then + if (enthalpyExchanger.airDuct1.vol[7].dynBal.initialize_p) then + der(enthalpyExchanger.airDuct1.vol[7].dynBal.medium.p) = 0; + end if; + end if; + end if; + if (enthalpyExchanger.airDuct1.vol[8].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (enthalpyExchanger.airDuct1.vol[8].dynBal.initialize_p) then + enthalpyExchanger.airDuct1.vol[8].dynBal.medium.p = enthalpyExchanger.airDuct1.vol[8].dynBal.p_start; + end if; + else + if (enthalpyExchanger.airDuct1.vol[8].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then + if (enthalpyExchanger.airDuct1.vol[8].dynBal.initialize_p) then + der(enthalpyExchanger.airDuct1.vol[8].dynBal.medium.p) = 0; + end if; + end if; + end if; + if (enthalpyExchanger.airDuct1.vol[9].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (enthalpyExchanger.airDuct1.vol[9].dynBal.initialize_p) then + enthalpyExchanger.airDuct1.vol[9].dynBal.medium.p = enthalpyExchanger.airDuct1.vol[9].dynBal.p_start; + end if; + else + if (enthalpyExchanger.airDuct1.vol[9].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then + if (enthalpyExchanger.airDuct1.vol[9].dynBal.initialize_p) then + der(enthalpyExchanger.airDuct1.vol[9].dynBal.medium.p) = 0; + end if; + end if; + end if; + if (enthalpyExchanger.airDuct1.vol[10].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (enthalpyExchanger.airDuct1.vol[10].dynBal.initialize_p) then + enthalpyExchanger.airDuct1.vol[10].dynBal.medium.p = enthalpyExchanger.airDuct1.vol[10].dynBal.p_start; + end if; + else + if (enthalpyExchanger.airDuct1.vol[10].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then + if (enthalpyExchanger.airDuct1.vol[10].dynBal.initialize_p) then + der(enthalpyExchanger.airDuct1.vol[10].dynBal.medium.p) = 0; + end if; + end if; + end if; + if (enthalpyExchanger.airDuct1.vol[11].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (enthalpyExchanger.airDuct1.vol[11].dynBal.initialize_p) then + enthalpyExchanger.airDuct1.vol[11].dynBal.medium.p = enthalpyExchanger.airDuct1.vol[11].dynBal.p_start; + end if; + else + if (enthalpyExchanger.airDuct1.vol[11].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then + if (enthalpyExchanger.airDuct1.vol[11].dynBal.initialize_p) then + der(enthalpyExchanger.airDuct1.vol[11].dynBal.medium.p) = 0; + end if; + end if; + end if; + if (enthalpyExchanger.airDuct1.vol[12].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (enthalpyExchanger.airDuct1.vol[12].dynBal.initialize_p) then + enthalpyExchanger.airDuct1.vol[12].dynBal.medium.p = enthalpyExchanger.airDuct1.vol[12].dynBal.p_start; + end if; + else + if (enthalpyExchanger.airDuct1.vol[12].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then + if (enthalpyExchanger.airDuct1.vol[12].dynBal.initialize_p) then + der(enthalpyExchanger.airDuct1.vol[12].dynBal.medium.p) = 0; + end if; + end if; + end if; + if (enthalpyExchanger.airDuct1.vol[13].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (enthalpyExchanger.airDuct1.vol[13].dynBal.initialize_p) then + enthalpyExchanger.airDuct1.vol[13].dynBal.medium.p = enthalpyExchanger.airDuct1.vol[13].dynBal.p_start; + end if; + else + if (enthalpyExchanger.airDuct1.vol[13].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then + if (enthalpyExchanger.airDuct1.vol[13].dynBal.initialize_p) then + der(enthalpyExchanger.airDuct1.vol[13].dynBal.medium.p) = 0; + end if; + end if; + end if; + if (enthalpyExchanger.airDuct1.vol[14].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (enthalpyExchanger.airDuct1.vol[14].dynBal.initialize_p) then + enthalpyExchanger.airDuct1.vol[14].dynBal.medium.p = enthalpyExchanger.airDuct1.vol[14].dynBal.p_start; + end if; + else + if (enthalpyExchanger.airDuct1.vol[14].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then + if (enthalpyExchanger.airDuct1.vol[14].dynBal.initialize_p) then + der(enthalpyExchanger.airDuct1.vol[14].dynBal.medium.p) = 0; + end if; + end if; + end if; + if (enthalpyExchanger.airDuct1.vol[15].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (enthalpyExchanger.airDuct1.vol[15].dynBal.initialize_p) then + enthalpyExchanger.airDuct1.vol[15].dynBal.medium.p = enthalpyExchanger.airDuct1.vol[15].dynBal.p_start; + end if; + else + if (enthalpyExchanger.airDuct1.vol[15].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then + if (enthalpyExchanger.airDuct1.vol[15].dynBal.initialize_p) then + der(enthalpyExchanger.airDuct1.vol[15].dynBal.medium.p) = 0; + end if; + end if; + end if; + +This required evaluation of +the interactive parameters + sinAirCol.p(start = 101325) + sinAirHot.p(start = 101325) + +The redundancies involve +initial equations: + enthalpyExchanger.airDuct2.vol[1].dynBal.medium.p = 101325.0; + enthalpyExchanger.airDuct2.vol[2].dynBal.medium.p = 101325.0; + enthalpyExchanger.airDuct2.vol[3].dynBal.medium.p = 101325.0; + enthalpyExchanger.airDuct2.vol[4].dynBal.medium.p = 101325.0; + enthalpyExchanger.airDuct2.vol[5].dynBal.medium.p = 101325.0; + enthalpyExchanger.airDuct2.vol[6].dynBal.medium.p = 101325.0; + enthalpyExchanger.airDuct2.vol[7].dynBal.medium.p = 101325.0; + enthalpyExchanger.airDuct2.vol[8].dynBal.medium.p = 101325.0; + enthalpyExchanger.airDuct2.vol[9].dynBal.medium.p = 101325.0; + enthalpyExchanger.airDuct2.vol[10].dynBal.medium.p = 101325.0; + enthalpyExchanger.airDuct2.vol[11].dynBal.medium.p = 101325.0; + enthalpyExchanger.airDuct2.vol[12].dynBal.medium.p = 101325.0; + enthalpyExchanger.airDuct2.vol[13].dynBal.medium.p = 101325.0; + enthalpyExchanger.airDuct2.vol[14].dynBal.medium.p = 101325.0; + enthalpyExchanger.airDuct2.vol[15].dynBal.medium.p = 101325.0; + enthalpyExchanger.airDuct1.vol[1].dynBal.medium.p = 101325.0; + enthalpyExchanger.airDuct1.vol[2].dynBal.medium.p = 101325.0; + enthalpyExchanger.airDuct1.vol[3].dynBal.medium.p = 101325.0; + enthalpyExchanger.airDuct1.vol[4].dynBal.medium.p = 101325.0; + enthalpyExchanger.airDuct1.vol[5].dynBal.medium.p = 101325.0; + enthalpyExchanger.airDuct1.vol[6].dynBal.medium.p = 101325.0; + enthalpyExchanger.airDuct1.vol[7].dynBal.medium.p = 101325.0; + enthalpyExchanger.airDuct1.vol[8].dynBal.medium.p = 101325.0; + enthalpyExchanger.airDuct1.vol[9].dynBal.medium.p = 101325.0; + enthalpyExchanger.airDuct1.vol[10].dynBal.medium.p = 101325.0; + enthalpyExchanger.airDuct1.vol[11].dynBal.medium.p = 101325.0; + enthalpyExchanger.airDuct1.vol[12].dynBal.medium.p = 101325.0; + enthalpyExchanger.airDuct1.vol[13].dynBal.medium.p = 101325.0; + enthalpyExchanger.airDuct1.vol[14].dynBal.medium.p = 101325.0; + enthalpyExchanger.airDuct1.vol[15].dynBal.medium.p = 101325.0; + + +Statistics + +Original Model + Number of components: 556 + Variables: 6181 + Constants: 154 (154 scalars) + Parameters: 2178 (2382 scalars) + Unknowns: 3849 (5219 scalars) + Differentiated variables: 117 scalars + Equations: 2512 + Nontrivial: 1919 +Translated Model + Constants: 2167 scalars + Free parameters: 163 scalars + Parameter depending: 1007 scalars + Continuous time states: 87 scalars + Time-varying variables: 1614 scalars + Alias variables: 2804 scalars + Number of mixed real/discrete systems of equations: 0 + Sizes of linear systems of equations: {2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 3, 3, 3, 3, 3, 3, 3, 3, 3, 3, 3, 3, 3, 3, 3} + Sizes after manipulation of the linear systems: {0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2} + Sizes of nonlinear systems of equations: {1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1} + Sizes after manipulation of the nonlinear systems: {0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0} + Number of numerical Jacobians: 0 + +Selected continuous time states +Statically selected continuous time states +enthalpyExchanger.airDuct1.senRelHum.phi +enthalpyExchanger.airDuct1.senTem.T +enthalpyExchanger.airDuct1.vol[1].dynBal.medium.Xi[1] +enthalpyExchanger.airDuct1.vol[1].dynBal.U +enthalpyExchanger.airDuct1.vol[2].dynBal.medium.Xi[1] +enthalpyExchanger.airDuct1.vol[2].dynBal.U +enthalpyExchanger.airDuct1.vol[3].dynBal.medium.Xi[1] +enthalpyExchanger.airDuct1.vol[3].dynBal.U +enthalpyExchanger.airDuct1.vol[4].dynBal.medium.Xi[1] +enthalpyExchanger.airDuct1.vol[4].dynBal.U +enthalpyExchanger.airDuct1.vol[5].dynBal.medium.Xi[1] +enthalpyExchanger.airDuct1.vol[5].dynBal.U +enthalpyExchanger.airDuct1.vol[6].dynBal.medium.Xi[1] +enthalpyExchanger.airDuct1.vol[6].dynBal.U +enthalpyExchanger.airDuct1.vol[7].dynBal.medium.Xi[1] +enthalpyExchanger.airDuct1.vol[7].dynBal.U +enthalpyExchanger.airDuct1.vol[8].dynBal.medium.Xi[1] +enthalpyExchanger.airDuct1.vol[8].dynBal.U +enthalpyExchanger.airDuct1.vol[9].dynBal.medium.Xi[1] +enthalpyExchanger.airDuct1.vol[9].dynBal.U +enthalpyExchanger.airDuct1.vol[10].dynBal.medium.Xi[1] +enthalpyExchanger.airDuct1.vol[10].dynBal.U +enthalpyExchanger.airDuct1.vol[11].dynBal.medium.Xi[1] +enthalpyExchanger.airDuct1.vol[11].dynBal.U +enthalpyExchanger.airDuct1.vol[12].dynBal.medium.Xi[1] +enthalpyExchanger.airDuct1.vol[12].dynBal.U +enthalpyExchanger.airDuct1.vol[13].dynBal.medium.Xi[1] +enthalpyExchanger.airDuct1.vol[13].dynBal.U +enthalpyExchanger.airDuct1.vol[14].dynBal.medium.Xi[1] +enthalpyExchanger.airDuct1.vol[14].dynBal.U +enthalpyExchanger.airDuct1.vol[15].dynBal.medium.Xi[1] +enthalpyExchanger.airDuct1.vol[15].dynBal.U +enthalpyExchanger.airDuct2.senRelHum.phi +enthalpyExchanger.airDuct2.senTem.T +enthalpyExchanger.airDuct2.vol[1].dynBal.medium.Xi[1] +enthalpyExchanger.airDuct2.vol[1].dynBal.U +enthalpyExchanger.airDuct2.vol[2].dynBal.medium.Xi[1] +enthalpyExchanger.airDuct2.vol[2].dynBal.U +enthalpyExchanger.airDuct2.vol[3].dynBal.medium.Xi[1] +enthalpyExchanger.airDuct2.vol[3].dynBal.U +enthalpyExchanger.airDuct2.vol[4].dynBal.medium.Xi[1] +enthalpyExchanger.airDuct2.vol[4].dynBal.U +enthalpyExchanger.airDuct2.vol[5].dynBal.medium.Xi[1] +enthalpyExchanger.airDuct2.vol[5].dynBal.U +enthalpyExchanger.airDuct2.vol[6].dynBal.medium.Xi[1] +enthalpyExchanger.airDuct2.vol[6].dynBal.U +enthalpyExchanger.airDuct2.vol[7].dynBal.medium.Xi[1] +enthalpyExchanger.airDuct2.vol[7].dynBal.U +enthalpyExchanger.airDuct2.vol[8].dynBal.medium.Xi[1] +enthalpyExchanger.airDuct2.vol[8].dynBal.U +enthalpyExchanger.airDuct2.vol[9].dynBal.medium.Xi[1] +enthalpyExchanger.airDuct2.vol[9].dynBal.U +enthalpyExchanger.airDuct2.vol[10].dynBal.medium.Xi[1] +enthalpyExchanger.airDuct2.vol[10].dynBal.U +enthalpyExchanger.airDuct2.vol[11].dynBal.medium.Xi[1] +enthalpyExchanger.airDuct2.vol[11].dynBal.U +enthalpyExchanger.airDuct2.vol[12].dynBal.medium.Xi[1] +enthalpyExchanger.airDuct2.vol[12].dynBal.U +enthalpyExchanger.airDuct2.vol[13].dynBal.medium.Xi[1] +enthalpyExchanger.airDuct2.vol[13].dynBal.U +enthalpyExchanger.airDuct2.vol[14].dynBal.medium.Xi[1] +enthalpyExchanger.airDuct2.vol[14].dynBal.U +enthalpyExchanger.airDuct2.vol[15].dynBal.medium.Xi[1] +enthalpyExchanger.airDuct2.vol[15].dynBal.U +enthalpyExchanger.membrane.heatTransfer.Ts[1] +enthalpyExchanger.membrane.heatTransfer.Ts[2] +enthalpyExchanger.membrane.heatTransfer.Ts[3] +enthalpyExchanger.membrane.heatTransfer.Ts[4] +enthalpyExchanger.membrane.heatTransfer.Ts[5] +enthalpyExchanger.membrane.heatTransfer.Ts[6] +enthalpyExchanger.membrane.heatTransfer.Ts[7] +enthalpyExchanger.membrane.heatTransfer.Ts[8] +enthalpyExchanger.membrane.heatTransfer.Ts[9] +enthalpyExchanger.membrane.heatTransfer.Ts[10] +enthalpyExchanger.membrane.heatTransfer.Ts[11] +enthalpyExchanger.membrane.heatTransfer.Ts[12] +enthalpyExchanger.membrane.heatTransfer.Ts[13] +enthalpyExchanger.membrane.heatTransfer.Ts[14] +enthalpyExchanger.membrane.heatTransfer.Ts[15] +senMasFraColIn.X +senMasFraColOut.X +senMasFraHotIn.X +senMasFraHotOut.X +senTemColIn.T +senTemColOut.T +senTemHotIn.T +senTemHotOut.T +Finished +Finished + = true + +Declaring variable: Boolean rScript ; + +savelog("AixLib.Fluid.MassExchangers.MembraneBasedEnthalpyExchangers.Examples.Test_EnthalpyExchanger.translation.log"); = true + + +rCheck = checkModel("AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.DHCPipe"); +Check of AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.DHCPipe +Warning: Local "m_flow_small" conflict with inherited. Should be identical +Warning: Component m_flow_small(min = << Empty >>), + but previously m_flow_small(min = 0). + The components are not identical. + + For element m_flow_small found at + + File: /tmp/tmp-AixLib-3-vnnf4reh/AixLib/Fluid/DistrictHeatingCooling/Pipes/DHCPipe.mo, line 39 + Conflict with element from + File: /tmp/tmp-AixLib-3-vnnf4reh/AixLib/Fluid/Interfaces/PartialTwoPortInterface.mo, line 10 + Component context: pip + Component declared as DHCPipe pip in AixLib.Fluid.DistrictHeatingCooling.Pipes + File: /tmp/tmp-AixLib-3-vnnf4reh/AixLib/Fluid/DistrictHeatingCooling/Pipes/Examples/DHCPipe.mo, line 18 +Warning: Local "m_flow_small" conflict with inherited. Should be identical +Warning: Component m_flow_small(min = << Empty >>), + but previously m_flow_small(min = 0). + The components are not identical. + + For element m_flow_small found at + + File: /tmp/tmp-AixLib-3-vnnf4reh/AixLib/Fluid/DistrictHeatingCooling/Pipes/DHCPipe.mo, line 39 + Conflict with element from + File: /tmp/tmp-AixLib-3-vnnf4reh/AixLib/Fluid/Interfaces/PartialTwoPortInterface.mo, line 10 + Component context: pip1 + Component declared as DHCPipe pip1 in AixLib.Fluid.DistrictHeatingCooling.Pipes + File: /tmp/tmp-AixLib-3-vnnf4reh/AixLib/Fluid/DistrictHeatingCooling/Pipes/Examples/DHCPipe.mo, line 68 +Warning: Local "m_flow_small" conflict with inherited. Should be identical +Warning: Component m_flow_small(min = << Empty >>), + but previously m_flow_small(min = 0). + The components are not identical. + + For element m_flow_small found at + + File: /tmp/tmp-AixLib-3-vnnf4reh/AixLib/Fluid/DistrictHeatingCooling/Pipes/DHCPipe.mo, line 39 + Conflict with element from + File: /tmp/tmp-AixLib-3-vnnf4reh/AixLib/Fluid/Interfaces/PartialTwoPortInterface.mo, line 10 + Component context: pip2 + Component declared as DHCPipe pip2 in AixLib.Fluid.DistrictHeatingCooling.Pipes + File: /tmp/tmp-AixLib-3-vnnf4reh/AixLib/Fluid/DistrictHeatingCooling/Pipes/Examples/DHCPipe.mo, line 114 +Warning: Local "m_flow_small" conflict with inherited. Should be identical +Warning: Component m_flow_small(min = << Empty >>), + but previously m_flow_small(min = 0). + The components are not identical. + + For element m_flow_small found at + + File: /tmp/tmp-AixLib-3-vnnf4reh/AixLib/Fluid/DistrictHeatingCooling/Pipes/DHCPipe.mo, line 39 + Conflict with element from + File: /tmp/tmp-AixLib-3-vnnf4reh/AixLib/Fluid/Interfaces/PartialTwoPortInterface.mo, line 10 + Component context: pip3 + Component declared as DHCPipe pip3 in AixLib.Fluid.DistrictHeatingCooling.Pipes + File: /tmp/tmp-AixLib-3-vnnf4reh/AixLib/Fluid/DistrictHeatingCooling/Pipes/Examples/DHCPipe.mo, line 161 +The model has the same number of unknowns and equations: 804 +The model could not be deduced to be symbolically well-posed. +The model has + 796+pip.vol.dynBal.nPorts+pip1.vol.dynBal.nPorts+pip2.vol.dynBal.nPorts+ pip3.vol.dynBal.nPorts +scalar unknowns and + 740+(if sin.use_Xi_in then 1 else (if sin.use_X_in then 0 else 1))+(if not sin.use_p_in then 1 else 0)+2*sin.nPorts+(if not sin.use_T_in then 1 else 0)+ (if sou.use_Xi_in then 1 else (if sou.use_X_in then 0 else 1))+(if not sou.use_m_flow_in then 1 else 0)+2*sou.nPorts+(if not sou.use_T_in then 1 else 0)+(if sin1.use_Xi_in then 1 else (if sin1.use_X_in then 0 else 1))+(if not sin1.use_p_in then 1 else 0)+2*sin1.nPorts+(if not sin1.use_T_in then 1 else 0)+(if sou1.use_Xi_in then 1 else (if sou1.use_X_in then 0 else 1))+(if not sou1.use_m_flow_in then 1 else 0)+2*sou1.nPorts+(if not sou1.use_T_in then 1 else 0)+(if sin2.use_Xi_in then 1 else (if sin2.use_X_in then 0 else 1)) +(if not sin2.use_p_in then 1 else 0)+2*sin2.nPorts+(if not sin2.use_T_in then 1 else 0)+(if sou2.use_Xi_in then 1 else (if sou2.use_X_in then 0 else 1)) +(if not sou2.use_m_flow_in then 1 else 0)+2*sou2.nPorts+(if not sou2.use_T_in then 1 else 0)+(if sin3.use_Xi_in then 1 else (if sin3.use_X_in then 0 else 1))+(if not sin3.use_p_in then 1 else 0)+2*sin3.nPorts+(if not sin3.use_T_in then 1 else 0)+(if sou3.use_Xi_in then 1 else (if sou3.use_X_in then 0 else 1))+(if not sou3.use_m_flow_in then 1 else 0)+2*sou3.nPorts+(if not sou3.use_T_in then 1 else 0)+(if not pip.vol.dynBal.use_mWat_flow then 1 else 0)+3*pip.vol.dynBal.nPorts+(if not pip1.vol.dynBal.use_mWat_flow then 1 else 0)+3*pip1.vol.dynBal.nPorts+(if not pip2.vol.dynBal.use_mWat_flow then 1 else 0)+3*pip2.vol.dynBal.nPorts+(if not pip3.vol.dynBal.use_mWat_flow then 1 else 0)+3*pip3.vol.dynBal.nPorts +scalar equations. +However, exploiting the given numerical settings of parameters gives the same number of unknowns and equations: + 804 +Check of AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.DHCPipe successful. +Declaring variable: Boolean rCheck ; + +Modelica.Utilities.Streams.print(" { \"file\" : \"AixLib/Resources/Scripts/Dymola/Fluid/DistrictHeatingCooling/Pipes/Examples/DHCPipe.mos\",", "AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.DHCPipe.statistics.log"); +Modelica.Utilities.Streams.print(" \"model\" : \"AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.DHCPipe\",", "AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.DHCPipe.statistics.log"); +Modelica.Utilities.Streams.print(" \"check\" : {", "AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.DHCPipe.statistics.log"); +Modelica.Utilities.Streams.print(" \"command\" : \"checkModel(\\\"AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.DHCPipe\\\");\",", "AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.DHCPipe.statistics.log"); +Modelica.Utilities.Streams.print(" \"result\" : " + String(rCheck), "AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.DHCPipe.statistics.log"); +Modelica.Utilities.Streams.print(" },", "AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.DHCPipe.statistics.log"); + + +rScript=RunScript("modelica://AixLib/Resources/Scripts/Dymola/Fluid/DistrictHeatingCooling/Pipes/Examples/DHCPipe.mos"); +translateModel("AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.DHCPipe"); +Translation of AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.DHCPipe +Warning: Local "m_flow_small" conflict with inherited. Should be identical +Warning: Component m_flow_small(min = << Empty >>), + but previously m_flow_small(min = 0). + The components are not identical. + + For element m_flow_small found at + + File: /tmp/tmp-AixLib-3-vnnf4reh/AixLib/Fluid/DistrictHeatingCooling/Pipes/DHCPipe.mo, line 39 + Conflict with element from + File: /tmp/tmp-AixLib-3-vnnf4reh/AixLib/Fluid/Interfaces/PartialTwoPortInterface.mo, line 10 + Component context: pip + Component declared as DHCPipe pip in AixLib.Fluid.DistrictHeatingCooling.Pipes + File: /tmp/tmp-AixLib-3-vnnf4reh/AixLib/Fluid/DistrictHeatingCooling/Pipes/Examples/DHCPipe.mo, line 18 +Warning: Local "m_flow_small" conflict with inherited. Should be identical +Warning: Component m_flow_small(min = << Empty >>), + but previously m_flow_small(min = 0). + The components are not identical. + + For element m_flow_small found at + + File: /tmp/tmp-AixLib-3-vnnf4reh/AixLib/Fluid/DistrictHeatingCooling/Pipes/DHCPipe.mo, line 39 + Conflict with element from + File: /tmp/tmp-AixLib-3-vnnf4reh/AixLib/Fluid/Interfaces/PartialTwoPortInterface.mo, line 10 + Component context: pip1 + Component declared as DHCPipe pip1 in AixLib.Fluid.DistrictHeatingCooling.Pipes + File: /tmp/tmp-AixLib-3-vnnf4reh/AixLib/Fluid/DistrictHeatingCooling/Pipes/Examples/DHCPipe.mo, line 68 +Warning: Local "m_flow_small" conflict with inherited. Should be identical +Warning: Component m_flow_small(min = << Empty >>), + but previously m_flow_small(min = 0). + The components are not identical. + + For element m_flow_small found at + + File: /tmp/tmp-AixLib-3-vnnf4reh/AixLib/Fluid/DistrictHeatingCooling/Pipes/DHCPipe.mo, line 39 + Conflict with element from + File: /tmp/tmp-AixLib-3-vnnf4reh/AixLib/Fluid/Interfaces/PartialTwoPortInterface.mo, line 10 + Component context: pip2 + Component declared as DHCPipe pip2 in AixLib.Fluid.DistrictHeatingCooling.Pipes + File: /tmp/tmp-AixLib-3-vnnf4reh/AixLib/Fluid/DistrictHeatingCooling/Pipes/Examples/DHCPipe.mo, line 114 +Warning: Local "m_flow_small" conflict with inherited. Should be identical +Warning: Component m_flow_small(min = << Empty >>), + but previously m_flow_small(min = 0). + The components are not identical. + + For element m_flow_small found at + + File: /tmp/tmp-AixLib-3-vnnf4reh/AixLib/Fluid/DistrictHeatingCooling/Pipes/DHCPipe.mo, line 39 + Conflict with element from + File: /tmp/tmp-AixLib-3-vnnf4reh/AixLib/Fluid/Interfaces/PartialTwoPortInterface.mo, line 10 + Component context: pip3 + Component declared as DHCPipe pip3 in AixLib.Fluid.DistrictHeatingCooling.Pipes + File: /tmp/tmp-AixLib-3-vnnf4reh/AixLib/Fluid/DistrictHeatingCooling/Pipes/Examples/DHCPipe.mo, line 161 +The DAE has 804 scalar unknowns and 804 scalar equations. + +Statistics + +Original Model + Number of components: 144 + Variables: 2246 + Constants: 37 (37 scalars) + Parameters: 1101 (1073 scalars) + Unknowns: 1108 (828 scalars) + Differentiated variables: 33 scalars + Equations: 923 + Nontrivial: 790 +Translated Model + Constants: 721 scalars + Free parameters: 205 scalars + Parameter depending: 321 scalars + Continuous time states: 29 scalars + Time-varying variables: 177 scalars + Alias variables: 514 scalars + Number of mixed real/discrete systems of equations: 0 + Sizes of linear systems of equations: {2, 2} + Sizes after manipulation of the linear systems: {0, 0} + Sizes of nonlinear systems of equations: {6} + Sizes after manipulation of the nonlinear systems: {1} + Number of numerical Jacobians: 0 + +Selected continuous time states +Statically selected continuous time states +pip.Q_gai +pip.Q_los +pip.vol.dynBal.U +pip1.pipCor.del.x +pip1.pipCor.timDel.x +pip1.Q_gai +pip1.Q_los +pip1.vol.dynBal.U +pip2.cylHeaTra1.CylindricLoad1.heatCapacitor.T +pip2.cylHeaTra2.CylindricLoad1.heatCapacitor.T +pip2.cylHeaTra3.CylindricLoad1.heatCapacitor.T +pip2.pipCor.del.x +pip2.pipCor.timDel.x +pip2.Q_gai +pip2.Q_los +pip2.vol.dynBal.U +pip3.pipCor.del.x +pip3.pipCor.timDel.x +pip3.Q_gai +pip3.Q_los +pip3.vol.dynBal.U +senTemIn.T +senTemIn1.T +senTemIn2.T +senTemIn3.T +senTemOut.T +senTemOut1.T +senTemOut2.T +senTemOut3.T +Finished +Warning: WARNINGS have been issued. + = true +simulateModel("AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.DHCPipe", stopTime=3600, method="dassl", tolerance=1e-6, resultFile="AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.DHCPipe"); +Finished + = true + +Declaring variable: Boolean rScript ; + +savelog("AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.DHCPipe.translation.log"); = true + + +rCheck = checkModel("AixLib.Fluid.FixedResistances.Examples.CompareFixedResistances"); +Warning: Can not resolve link "AixLib.Fluid.FixedResistances.FixedResistanceDpM" in AixLib.Fluid.FixedResistances.Examples.CompareFixedResistances +Check of AixLib.Fluid.FixedResistances.Examples.CompareFixedResistances +The model has the same number of unknowns and equations: 60 +The model could not be deduced to be symbolically well-posed. +The model has + 60 +scalar unknowns and + 48+(if sou1.use_Xi_in then 1 else (if sou1.use_X_in then 0 else 1))+(if not sou1.use_p_in then 1 else 0)+2*sou1.nPorts+(if not sou1.use_T_in then 1 else 0) +(if sin1.use_Xi_in then 1 else (if sin1.use_X_in then 0 else 1))+(if not sin1.use_p_in then 1 else 0)+2*sin1.nPorts+(if not sin1.use_T_in then 1 else 0) +scalar equations. +However, exploiting the given numerical settings of parameters gives the same number of unknowns and equations: + 60 +Check of AixLib.Fluid.FixedResistances.Examples.CompareFixedResistances successful. +Declaring variable: Boolean rCheck ; + +Modelica.Utilities.Streams.print(" { \"file\" : \"AixLib/Resources/Scripts/Dymola/Fluid/FixedResistances/Examples/CompareFixedResistances.mos\",", "AixLib.Fluid.FixedResistances.Examples.CompareFixedResistances.statistics.log"); +Modelica.Utilities.Streams.print(" \"model\" : \"AixLib.Fluid.FixedResistances.Examples.CompareFixedResistances\",", "AixLib.Fluid.FixedResistances.Examples.CompareFixedResistances.statistics.log"); +Modelica.Utilities.Streams.print(" \"check\" : {", "AixLib.Fluid.FixedResistances.Examples.CompareFixedResistances.statistics.log"); +Modelica.Utilities.Streams.print(" \"command\" : \"checkModel(\\\"AixLib.Fluid.FixedResistances.Examples.CompareFixedResistances\\\");\",", "AixLib.Fluid.FixedResistances.Examples.CompareFixedResistances.statistics.log"); +Modelica.Utilities.Streams.print(" \"result\" : " + String(rCheck), "AixLib.Fluid.FixedResistances.Examples.CompareFixedResistances.statistics.log"); +Modelica.Utilities.Streams.print(" },", "AixLib.Fluid.FixedResistances.Examples.CompareFixedResistances.statistics.log"); + + +rScript=RunScript("modelica://AixLib/Resources/Scripts/Dymola/Fluid/FixedResistances/Examples/CompareFixedResistances.mos"); +simulateModel("AixLib.Fluid.FixedResistances.Examples.CompareFixedResistances", stopTime=3600, method="dassl", tolerance=1e-006, resultFile="AixLib.Fluid.FixedResistances.Examples.CompareFixedResistances"); +Translation of AixLib.Fluid.FixedResistances.Examples.CompareFixedResistances +The DAE has 60 scalar unknowns and 60 scalar equations. + +Statistics + +Original Model + Number of components: 12 + Variables: 181 + Constants: 6 (6 scalars) + Parameters: 87 (85 scalars) + Unknowns: 88 (60 scalars) + Equations: 88 + Nontrivial: 81 +Translated Model + Constants: 66 scalars + Free parameters: 22 scalars + Parameter depending: 9 scalars + Time-varying variables: 7 scalars + Alias variables: 47 scalars + Number of mixed real/discrete systems of equations: 0 + Sizes of linear systems of equations: { } + Sizes after manipulation of the linear systems: { } + Sizes of nonlinear systems of equations: { } + Sizes after manipulation of the nonlinear systems: { } + Number of numerical Jacobians: 0 + +Selected continuous time states +Finished +Finished + = true + +Declaring variable: Boolean rScript ; + +savelog("AixLib.Fluid.FixedResistances.Examples.CompareFixedResistances.translation.log"); = true + + +rCheck = checkModel("AixLib.Fluid.Movers.DpControlledMovers.Examples.DpConst"); +Check of AixLib.Fluid.Movers.DpControlledMovers.Examples.DpConst +The model has the same number of unknowns and equations: 250 +The model could not be deduced to be symbolically well-posed. +The model has + 248+vol.dynBal.nPorts +scalar unknowns and + 237+(if sou.use_Xi_in then 1 else (if sou.use_X_in then 0 else 1))+(if not sou.use_p_in then 1 else 0)+2*sou.nPorts+(if not sou.use_T_in then 1 else 0)+ (if not dpControlled_dp.mov.vol.steBal.use_mWat_flow then 1 else 0)+(if not vol.dynBal.use_mWat_flow then 1 else 0)+3*vol.dynBal.nPorts +scalar equations. +However, exploiting the given numerical settings of parameters gives the same number of unknowns and equations: + 250 +Check of AixLib.Fluid.Movers.DpControlledMovers.Examples.DpConst successful. +Declaring variable: Boolean rCheck ; + +Modelica.Utilities.Streams.print(" { \"file\" : \"AixLib/Resources/Scripts/Dymola/Fluid/Movers/DpControlledMovers/Examples/DpConst.mos\",", "AixLib.Fluid.Movers.DpControlledMovers.Examples.DpConst.statistics.log"); +Modelica.Utilities.Streams.print(" \"model\" : \"AixLib.Fluid.Movers.DpControlledMovers.Examples.DpConst\",", "AixLib.Fluid.Movers.DpControlledMovers.Examples.DpConst.statistics.log"); +Modelica.Utilities.Streams.print(" \"check\" : {", "AixLib.Fluid.Movers.DpControlledMovers.Examples.DpConst.statistics.log"); +Modelica.Utilities.Streams.print(" \"command\" : \"checkModel(\\\"AixLib.Fluid.Movers.DpControlledMovers.Examples.DpConst\\\");\",", "AixLib.Fluid.Movers.DpControlledMovers.Examples.DpConst.statistics.log"); +Modelica.Utilities.Streams.print(" \"result\" : " + String(rCheck), "AixLib.Fluid.Movers.DpControlledMovers.Examples.DpConst.statistics.log"); +Modelica.Utilities.Streams.print(" },", "AixLib.Fluid.Movers.DpControlledMovers.Examples.DpConst.statistics.log"); + + +rScript=RunScript("modelica://AixLib/Resources/Scripts/Dymola/Fluid/Movers/DpControlledMovers/Examples/DpConst.mos"); +simulateModel("AixLib.Fluid.Movers.DpControlledMovers.Examples.DpConst", startTime=0, stopTime=3600, tolerance=1e-6, method="dassl", resultFile="AixLib.Fluid.Movers.DpControlledMovers.Examples.DpConst"); +Translation of AixLib.Fluid.Movers.DpControlledMovers.Examples.DpConst +The DAE has 250 scalar unknowns and 250 scalar equations. + +Statistics + +Original Model + Number of components: 82 + Variables: 814 + Constants: 19 (19 scalars) + Parameters: 465 (949 scalars) + Unknowns: 330 (265 scalars) + Differentiated variables: 7 scalars + Equations: 284 + Nontrivial: 236 +Translated Model + Constants: 686 scalars + Free parameters: 51 scalars + Parameter depending: 271 scalars + Outputs: 1 scalars + Continuous time states: 5 scalars + Time-varying variables: 61 scalars + Alias variables: 164 scalars + Number of mixed real/discrete systems of equations: 0 + Sizes of linear systems of equations: { } + Sizes after manipulation of the linear systems: { } + Sizes of nonlinear systems of equations: {3, 1} + Sizes after manipulation of the nonlinear systems: {1, 1} + Number of numerical Jacobians: 0 + Initialization problem + Sizes of nonlinear systems of equations: {3, 1, 1} + Sizes after manipulation of the nonlinear systems: {1, 0, 1} + Sizes of simplified homotopy nonlinear systems of equations: {3, 1} + Sizes after manipulation of the simplified homotopy nonlinear systems: {1, 0} + Number of numerical Jacobians: 0 + +Selected continuous time states +Statically selected continuous time states +dpControlled_dp.mov.filter.s[1] +dpControlled_dp.mov.filter.s[2] +integrator.y +val.filter.s[1] +val.filter.s[2] +Finished +Finished + = true + + + +Declaring variable: Boolean rScript ; + +savelog("AixLib.Fluid.Movers.DpControlledMovers.Examples.DpConst.translation.log"); = true + + +rCheck = checkModel("AixLib.Fluid.Movers.PumpsPolynomialBased.Examples.PumpSpeedControlledDpV"); +Warning: Can not resolve link "Zugabe.Zugabe_DB.Pump.Examples" in AixLib.Fluid.Movers.PumpsPolynomialBased.Examples.PumpSpeedControlledDpV +Check of AixLib.Fluid.Movers.PumpsPolynomialBased.Examples.PumpSpeedControlledDpV +The model has the same number of unknowns and equations: 220 +The model could not be deduced to be symbolically well-posed. +The model has + 208+2*(size(pump.maxMinTable.columns, 1)+pump.deMultiplex2.n1+pump.deMultiplex2.n2) +pump.criticalDamping.n+pump.vol.dynBal.nPorts +scalar unknowns and + 198+2*size(pump.maxMinTable.columns, 1)+pump.deMultiplex2.n1+pump.deMultiplex2.n2 +pump.criticalDamping.n+(if vessle.use_Xi_in then 1 else (if vessle.use_X_in then 0 else 1))+(if not vessle.use_p_in then 1 else 0)+2*vessle.nPorts+(if not vessle.use_T_in then 1 else 0)+(if not pump.vol.dynBal.use_mWat_flow then 1 else 0)+3*pump.vol.dynBal.nPorts +scalar equations. +However, exploiting the given numerical settings of parameters gives the same number of unknowns and equations: + 220 +Check of AixLib.Fluid.Movers.PumpsPolynomialBased.Examples.PumpSpeedControlledDpV successful. +Declaring variable: Boolean rCheck ; + +Modelica.Utilities.Streams.print(" { \"file\" : \"AixLib/Resources/Scripts/Dymola/Fluid/Movers/PumpsPolynomialBased/Examples/PumpSpeedControlledDpV.mos\",", "AixLib.Fluid.Movers.PumpsPolynomialBased.Examples.PumpSpeedControlledDpV.statistics.log"); +Modelica.Utilities.Streams.print(" \"model\" : \"AixLib.Fluid.Movers.PumpsPolynomialBased.Examples.PumpSpeedControlledDpV\",", "AixLib.Fluid.Movers.PumpsPolynomialBased.Examples.PumpSpeedControlledDpV.statistics.log"); +Modelica.Utilities.Streams.print(" \"check\" : {", "AixLib.Fluid.Movers.PumpsPolynomialBased.Examples.PumpSpeedControlledDpV.statistics.log"); +Modelica.Utilities.Streams.print(" \"command\" : \"checkModel(\\\"AixLib.Fluid.Movers.PumpsPolynomialBased.Examples.PumpSpeedControlledDpV\\\");\",", "AixLib.Fluid.Movers.PumpsPolynomialBased.Examples.PumpSpeedControlledDpV.statistics.log"); +Modelica.Utilities.Streams.print(" \"result\" : " + String(rCheck), "AixLib.Fluid.Movers.PumpsPolynomialBased.Examples.PumpSpeedControlledDpV.statistics.log"); +Modelica.Utilities.Streams.print(" },", "AixLib.Fluid.Movers.PumpsPolynomialBased.Examples.PumpSpeedControlledDpV.statistics.log"); + + +rScript=RunScript("modelica://AixLib/Resources/Scripts/Dymola/Fluid/Movers/PumpsPolynomialBased/Examples/PumpSpeedControlledDpV.mos"); +simulateModel("AixLib.Fluid.Movers.PumpsPolynomialBased.Examples.PumpSpeedControlledDpV", tolerance=1e-6, stopTime=600.0, method="dassl", resultFile="AixLib.Fluid.Movers.PumpsPolynomialBased.Examples.PumpSpeedControlledDpV"); +Translation of AixLib.Fluid.Movers.PumpsPolynomialBased.Examples.PumpSpeedControlledDpV +The DAE has 220 scalar unknowns and 220 scalar equations. + +Statistics + +Original Model + Number of components: 58 + Variables: 526 + Constants: 16 (16 scalars) + Parameters: 242 (586 scalars) + Unknowns: 268 (224 scalars) + Differentiated variables: 8 scalars + Equations: 228 + Nontrivial: 195 +Translated Model + Constants: 150 scalars + Free parameters: 365 scalars + Parameter depending: 115 scalars + Outputs: 4 scalars + Continuous time states: 6 scalars + Time-varying variables: 50 scalars + Alias variables: 146 scalars + Number of mixed real/discrete systems of equations: 0 + Sizes of linear systems of equations: { } + Sizes after manipulation of the linear systems: { } + Sizes of nonlinear systems of equations: {1} + Sizes after manipulation of the nonlinear systems: {0} + Number of numerical Jacobians: 0 + Initialization problem + Sizes of nonlinear systems of equations: {1} + Sizes after manipulation of the nonlinear systems: {1} + Number of numerical Jacobians: 0 + +Selected continuous time states +Statically selected continuous time states +ctrlDpVarN.PID.D.x +ctrlDpVarN.PID.I.y +pump.criticalDamping.x[1] +pump.criticalDamping.x[2] +simpleValve.filter.s[1] +simpleValve.filter.s[2] +Finished +Finished + = true + +Declaring variable: Boolean rScript ; + +savelog("AixLib.Fluid.Movers.PumpsPolynomialBased.Examples.PumpSpeedControlledDpV.translation.log"); \ No newline at end of file diff --git a/docs/correct_HTML_issue1147_GenericBoiler/regression/Fluid/unitTests-dymola.log b/docs/correct_HTML_issue1147_GenericBoiler/regression/Fluid/unitTests-dymola.log new file mode 100644 index 0000000000..a1aa8fe674 --- /dev/null +++ b/docs/correct_HTML_issue1147_GenericBoiler/regression/Fluid/unitTests-dymola.log @@ -0,0 +1,14 @@ +Regression tests are only run for the following package: + AixLib.Fluid +*** Error: AixLib_Fluid_BoilerCHP_Examples_CHPSystem.txt: Errors during result verification. + Did not find variable combinedHeatPower.senTSup.T in old results. +*** Error: AixLib_Fluid_Examples_GeothermalHeatPump_GeothermalHeatPump.txt: Errors during result verification. + Absolute error = 2.768e+03 at t = 86400.0 for heatPumpPower + Absolute error = 2.786e-01 at t = 78624.0 for heatStorage.layer[1].T + Absolute error = 1.200e+00 at t = 78624.0 for heatStorage.layer[5].T +Comparison files output by funnel are stored in the directory 'funnel_comp' of size 1.1 MB. +Run 'python -c "import buildingspy.development.regressiontest as t; t.Tester(tool=\"dymola\").report()"' +to access a summary of the comparison results. + +Script that runs unit tests had 0 warnings and 2 errors. + diff --git a/docs/correct_HTML_issue1147_GenericBoiler/regression/Systems/comparison-dymola.log b/docs/correct_HTML_issue1147_GenericBoiler/regression/Systems/comparison-dymola.log new file mode 100644 index 0000000000..5d81edd0f2 --- /dev/null +++ b/docs/correct_HTML_issue1147_GenericBoiler/regression/Systems/comparison-dymola.log @@ -0,0 +1,1019 @@ +[ + { + "comparison": { + "file_name": "AixLib.Systems.ModularAHU.Validation.AHU2_Heater.mat", + "funnel_dirs": [ + "funnel_comp/AixLib.Systems.ModularAHU.Validation.AHU2_Heater.mat_registerModule.registerBus.TAirInMea", + "funnel_comp/AixLib.Systems.ModularAHU.Validation.AHU2_Heater.mat_registerModule.registerBus.TAirOutMea", + "funnel_comp/AixLib.Systems.ModularAHU.Validation.AHU2_Heater.mat_combiTimeTable.y[6]", + "funnel_comp/AixLib.Systems.ModularAHU.Validation.AHU2_Heater.mat_combiTimeTable.y[5]", + "funnel_comp/AixLib.Systems.ModularAHU.Validation.AHU2_Heater.mat_combiTimeTable.y[3]", + "funnel_comp/AixLib.Systems.ModularAHU.Validation.AHU2_Heater.mat_combiTimeTable.y[4]", + "funnel_comp/AixLib.Systems.ModularAHU.Validation.AHU2_Heater.mat_registerModule.registerBus.hydraulicBus.TFwrdOutMea", + "funnel_comp/AixLib.Systems.ModularAHU.Validation.AHU2_Heater.mat_registerModule.registerBus.hydraulicBus.TRtrnInMea", + "funnel_comp/AixLib.Systems.ModularAHU.Validation.AHU2_Heater.mat_combiTimeTable.y[9]", + "funnel_comp/AixLib.Systems.ModularAHU.Validation.AHU2_Heater.mat_combiTimeTable.y[8]", + "funnel_comp/AixLib.Systems.ModularAHU.Validation.AHU2_Heater.mat_Simulation_VF_in_m3h.y", + "funnel_comp/AixLib.Systems.ModularAHU.Validation.AHU2_Heater.mat_Simulation_VF_out_m3h.y" + ], + "success_rate": 1.0, + "t_err_max": [ + 0.0, + 0.0, + 0.0, + 0.0, + 0.0, + 0.0, + 0.0, + 0.0, + 0.0, + 0.0, + 0.0, + 0.0 + ], + "test_passed": [ + 1, + 1, + 1, + 1, + 1, + 1, + 1, + 1, + 1, + 1, + 1, + 1 + ], + "var_groups": [ + 0, + 0, + 0, + 0, + 1, + 1, + 1, + 1, + 2, + 2, + 2, + 2 + ], + "variables": [ + "registerModule.registerBus.TAirInMea", + "registerModule.registerBus.TAirOutMea", + "combiTimeTable.y[6]", + "combiTimeTable.y[5]", + "combiTimeTable.y[3]", + "combiTimeTable.y[4]", + "registerModule.registerBus.hydraulicBus.TFwrdOutMea", + "registerModule.registerBus.hydraulicBus.TRtrnInMea", + "combiTimeTable.y[9]", + "combiTimeTable.y[8]", + "Simulation_VF_in_m3h.y", + "Simulation_VF_out_m3h.y" + ], + "warnings": [ + null, + null, + null, + null, + null, + null, + null, + null, + null, + null, + null, + null + ] + }, + "model": "AixLib.Systems.ModularAHU.Validation.AHU2_Heater", + "simulation": { + "elapsed_time": 0.836, + "final_time": 4320, + "jacobians": 4262, + "start_time": 0, + "state_events": 0, + "success": true + } + }, + { + "comparison": { + "file_name": "AixLib.Systems.HydraulicModules.Example.Throttle.mat", + "funnel_dirs": [ + "funnel_comp/AixLib.Systems.HydraulicModules.Example.Throttle.mat_hydraulicBus.TFwrdInMea", + "funnel_comp/AixLib.Systems.HydraulicModules.Example.Throttle.mat_hydraulicBus.TFwrdOutMea", + "funnel_comp/AixLib.Systems.HydraulicModules.Example.Throttle.mat_hydraulicBus.TRtrnInMea", + "funnel_comp/AixLib.Systems.HydraulicModules.Example.Throttle.mat_hydraulicBus.TRtrnOutMea", + "funnel_comp/AixLib.Systems.HydraulicModules.Example.Throttle.mat_hydraulicBus.VFlowInMea", + "funnel_comp/AixLib.Systems.HydraulicModules.Example.Throttle.mat_hydraulicBus.VFlowOutMea" + ], + "success_rate": 1.0, + "t_err_max": [ + 0.0, + 0.0, + 0.0, + 0.0, + 0.0, + 0.0 + ], + "test_passed": [ + 1, + 1, + 1, + 1, + 1, + 1 + ], + "var_groups": [ + 0, + 0, + 0, + 0, + 1, + 1 + ], + "variables": [ + "hydraulicBus.TFwrdInMea", + "hydraulicBus.TFwrdOutMea", + "hydraulicBus.TRtrnInMea", + "hydraulicBus.TRtrnOutMea", + "hydraulicBus.VFlowInMea", + "hydraulicBus.VFlowOutMea" + ], + "warnings": [ + null, + null, + null, + null, + null, + null + ] + }, + "model": "AixLib.Systems.HydraulicModules.Example.Throttle", + "simulation": { + "elapsed_time": 0.0565, + "final_time": 1000, + "jacobians": 43, + "start_time": 0, + "state_events": 0, + "success": true + } + }, + { + "comparison": { + "file_name": "AixLib.Systems.ModularEnergySystems.ModularBoiler.Examples.ModularBoilerHeatingCurve.mat", + "funnel_dirs": [ + "funnel_comp/AixLib.Systems.ModularEnergySystems.ModularBoiler.Examples.ModularBoilerHeatingCurve.mat_boilerControlBus.TSupMea", + 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b/docs/correct_HTML_issue1147_GenericBoiler/regression/Systems/funnel_comp/AixLib.Systems.ModularEnergySystems.ModularBoiler.Examples.ModularBoilerSimple.mat_boilerControlBus.fuelPower/reference.csv new file mode 100644 index 0000000000..ae81923c1f --- /dev/null +++ b/docs/correct_HTML_issue1147_GenericBoiler/regression/Systems/funnel_comp/AixLib.Systems.ModularEnergySystems.ModularBoiler.Examples.ModularBoilerSimple.mat_boilerControlBus.fuelPower/reference.csv @@ -0,0 +1,102 @@ +x,y +0,54272.54296875 +840,28462.59765625 +1680,30491.70703125 +2520,31591.62890625 +3360,32481.60546875 +4200,33109.546875 +5040,33438.75390625 +5880.000000000001,33450.015625 +6720,33142.6640625 +7560,32534.6171875 +8400,31661.416015625 +9240,30574.1796875 +10080,29336.751953125 +10920,28022.078125 +11760,26708.03125 +12600,25472.849609375 +13440,24390.44921875 +14280,23523.880859375 +15120,22927.251953125 +15960,22637.845703125 +16800,22673.17578125 +17640,23031.091796875 +18480,23689.88671875 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b/docs/correct_HTML_issue1147_GenericBoiler/regression/Systems/funnel_comp/AixLib.Systems.ModularEnergySystems.ModularBoiler.Examples.ModularBoilerSimple.mat_boilerControlBus.fuelPower/test.csv new file mode 100644 index 0000000000..ae81923c1f --- /dev/null +++ b/docs/correct_HTML_issue1147_GenericBoiler/regression/Systems/funnel_comp/AixLib.Systems.ModularEnergySystems.ModularBoiler.Examples.ModularBoilerSimple.mat_boilerControlBus.fuelPower/test.csv @@ -0,0 +1,102 @@ +x,y +0,54272.54296875 +840,28462.59765625 +1680,30491.70703125 +2520,31591.62890625 +3360,32481.60546875 +4200,33109.546875 +5040,33438.75390625 +5880.000000000001,33450.015625 +6720,33142.6640625 +7560,32534.6171875 +8400,31661.416015625 +9240,30574.1796875 +10080,29336.751953125 +10920,28022.078125 +11760,26708.03125 +12600,25472.849609375 +13440,24390.44921875 +14280,23523.880859375 +15120,22927.251953125 +15960,22637.845703125 +16800,22673.17578125 +17640,23031.091796875 +18480,23689.88671875 +19320,24607.69140625 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b/docs/correct_HTML_issue1147_GenericBoiler/regression/Systems/simulator-dymola.log @@ -0,0 +1,2320 @@ + = true + + +rCheck = checkModel("AixLib.Systems.ModularEnergySystems.ModularBoiler.Examples.ModularBoilerHeatingCurve"); +Check of AixLib.Systems.ModularEnergySystems.ModularBoiler.Examples.ModularBoilerHeatingCurve +The model has the same number of unknowns and equations: 602 +The model could not be deduced to be symbolically well-posed. +The model has + 572+modularBoiler.boilerGeneric.vol.dynBal.nPorts+2*modularBoiler.boilerGeneric.offDesignOperation.multiplex4.n1 +2*modularBoiler.boilerGeneric.offDesignOperation.multiplex4.n2+2* modularBoiler.boilerGeneric.offDesignOperation.multiplex4.n3+2* modularBoiler.boilerGeneric.offDesignOperation.multiplex4.n4+modularBoiler.boilerGeneric.offDesignOperation.boilerEffciency.nin +2*modularBoiler.boilerGeneric.designOperation.multiplex4.n1+2* modularBoiler.boilerGeneric.designOperation.multiplex4.n2+2*modularBoiler.boilerGeneric.designOperation.multiplex4.n3 +2*modularBoiler.boilerGeneric.designOperation.multiplex4.n4+modularBoiler.boilerGeneric.designOperation.boilerEffciency.nin +modularBoiler.pump.vol.dynBal.nPorts+vol.dynBal.nPorts +scalar unknowns and + 560+2*(modularBoiler.boilerGeneric.offDesignOperation.multiplex4.n1+ modularBoiler.boilerGeneric.offDesignOperation.multiplex4.n2+modularBoiler.boilerGeneric.offDesignOperation.multiplex4.n3 +modularBoiler.boilerGeneric.offDesignOperation.multiplex4.n4+modularBoiler.boilerGeneric.designOperation.multiplex4.n1 +modularBoiler.boilerGeneric.designOperation.multiplex4.n2+modularBoiler.boilerGeneric.designOperation.multiplex4.n3 +modularBoiler.boilerGeneric.designOperation.multiplex4.n4)+(if bou.use_Xi_in then 1 else (if bou.use_X_in then 0 else 1))+(if not bou.use_p_in then 1 else 0)+2*bou.nPorts+(if not bou.use_T_in then 1 else 0)+(if not modularBoiler.boilerGeneric.vol.dynBal.use_mWat_flow then 1 else 0)+3* modularBoiler.boilerGeneric.vol.dynBal.nPorts+(if not modularBoiler.pump.vol.dynBal.use_mWat_flow then 1 else 0)+3*modularBoiler.pump.vol.dynBal.nPorts+(if not vol.dynBal.use_mWat_flow then 1 else 0)+3*vol.dynBal.nPorts +scalar equations. +However, exploiting the given numerical settings of parameters gives the same number of unknowns and equations: + 602 +Check of AixLib.Systems.ModularEnergySystems.ModularBoiler.Examples.ModularBoilerHeatingCurve successful. +Declaring variable: Boolean rCheck ; + +Modelica.Utilities.Streams.print(" { \"file\" : \"AixLib/Resources/Scripts/Dymola/Systems/ModularEnergySystems/Examples/ModularBoilerHeatingCurve.mos\",", "AixLib.Systems.ModularEnergySystems.ModularBoiler.Examples.ModularBoilerHeatingCurve.statistics.log"); +Modelica.Utilities.Streams.print(" \"model\" : \"AixLib.Systems.ModularEnergySystems.ModularBoiler.Examples.ModularBoilerHeatingCurve\",", "AixLib.Systems.ModularEnergySystems.ModularBoiler.Examples.ModularBoilerHeatingCurve.statistics.log"); +Modelica.Utilities.Streams.print(" \"check\" : {", "AixLib.Systems.ModularEnergySystems.ModularBoiler.Examples.ModularBoilerHeatingCurve.statistics.log"); +Modelica.Utilities.Streams.print(" \"command\" : \"checkModel(\\\"AixLib.Systems.ModularEnergySystems.ModularBoiler.Examples.ModularBoilerHeatingCurve\\\");\",", "AixLib.Systems.ModularEnergySystems.ModularBoiler.Examples.ModularBoilerHeatingCurve.statistics.log"); +Modelica.Utilities.Streams.print(" \"result\" : " + String(rCheck), "AixLib.Systems.ModularEnergySystems.ModularBoiler.Examples.ModularBoilerHeatingCurve.statistics.log"); +Modelica.Utilities.Streams.print(" },", "AixLib.Systems.ModularEnergySystems.ModularBoiler.Examples.ModularBoilerHeatingCurve.statistics.log"); + + +rScript=RunScript("modelica://AixLib/Resources/Scripts/Dymola/Systems/ModularEnergySystems/Examples/ModularBoilerHeatingCurve.mos"); +simulateModel("AixLib.Systems.ModularEnergySystems.ModularBoiler.Examples.ModularBoilerHeatingCurve", tolerance=1e-06, stopTime=84000, method="dassl", resultFile="AixLib.Systems.ModularEnergySystems.ModularBoiler.Examples.ModularBoilerHeatingCurve"); +Translation of AixLib.Systems.ModularEnergySystems.ModularBoiler.Examples.ModularBoilerHeatingCurve +The DAE has 602 scalar unknowns and 602 scalar equations. + +Statistics + +Original Model + Number of components: 166 + Variables: 1361 + Constants: 26 (118 scalars) + Parameters: 662 (1186 scalars) + Unknowns: 673 (621 scalars) + Differentiated variables: 14 scalars + Equations: 604 + Nontrivial: 502 +Translated Model + Constants: 535 scalars + Free parameters: 327 scalars + Parameter depending: 512 scalars + Outputs: 9 scalars + Continuous time states: 10 scalars + Time-varying variables: 163 scalars + Alias variables: 388 scalars + Number of mixed real/discrete systems of equations: 0 + Sizes of linear systems of equations: {4} + Sizes after manipulation of the linear systems: {0} + Sizes of nonlinear systems of equations: {5} + Sizes after manipulation of the nonlinear systems: {1} + Number of numerical Jacobians: 0 + Initialization problem + Sizes of nonlinear systems of equations: {5} + Sizes after manipulation of the nonlinear systems: {1} + Number of numerical Jacobians: 0 + +Selected continuous time states +Statically selected continuous time states +modularBoiler.boilerControl.internalFirRatControl.PID.I.y +modularBoiler.boilerGeneric.senTRet.T +modularBoiler.boilerGeneric.senTSup.T +modularBoiler.boilerGeneric.vol.dynBal.U +modularBoiler.pump.filter.s[1] +modularBoiler.pump.filter.s[2] +modularBoiler.pump.vol.dynBal.U +modularBoiler.senTRet.T +modularBoiler.senTSup.T +vol.dynBal.U +Finished +Finished + = true + +Declaring variable: Boolean rScript ; + +savelog("AixLib.Systems.ModularEnergySystems.ModularBoiler.Examples.ModularBoilerHeatingCurve.translation.log"); = true + + +rCheck = checkModel("AixLib.Systems.ModularAHU.Examples.GenericAHU"); +Check of AixLib.Systems.ModularAHU.Examples.GenericAHU +The model has the same number of unknowns and equations: 9000 +The model could not be deduced to be symbolically well-posed. +The model has + 8800+genericAHU.preheater.hydraulicModule.valve.vol.dynBal.nPorts+ genericAHU.preheater.hydraulicModule.pipe1.simplePipe.vol[1].dynBal.nPorts+ genericAHU.preheater.hydraulicModule.pipe1.simplePipe.vol[2].dynBal.nPorts+ genericAHU.preheater.hydraulicModule.pipe1.simplePipe.vol[3].dynBal.nPorts+ genericAHU.preheater.hydraulicModule.pipe2.simplePipe.vol[1].dynBal.nPorts+ genericAHU.preheater.hydraulicModule.pipe2.simplePipe.vol[2].dynBal.nPorts+ genericAHU.preheater.hydraulicModule.pipe2.simplePipe.vol[3].dynBal.nPorts+ genericAHU.preheater.hydraulicModule.pipe3.simplePipe.vol[1].dynBal.nPorts+ genericAHU.preheater.hydraulicModule.pipe3.simplePipe.vol[2].dynBal.nPorts+ genericAHU.preheater.hydraulicModule.pipe3.simplePipe.vol[3].dynBal.nPorts+ genericAHU.preheater.hydraulicModule.pipe4.simplePipe.vol[1].dynBal.nPorts+ genericAHU.preheater.hydraulicModule.pipe4.simplePipe.vol[2].dynBal.nPorts+ genericAHU.preheater.hydraulicModule.pipe4.simplePipe.vol[3].dynBal.nPorts+ genericAHU.preheater.hydraulicModule.pipe5.simplePipe.vol[1].dynBal.nPorts+ genericAHU.preheater.hydraulicModule.pipe5.simplePipe.vol[2].dynBal.nPorts+ genericAHU.preheater.hydraulicModule.pipe5.simplePipe.vol[3].dynBal.nPorts+ genericAHU.preheater.hydraulicModule.pipe6.simplePipe.vol[1].dynBal.nPorts+ genericAHU.preheater.hydraulicModule.pipe6.simplePipe.vol[2].dynBal.nPorts+ genericAHU.preheater.hydraulicModule.pipe6.simplePipe.vol[3].dynBal.nPorts+ genericAHU.preheater.hydraulicModule.junc456.dynBal.nPorts+genericAHU.preheater.hydraulicModule.PumpInterface.pump.vol.dynBal.nPorts +2*genericAHU.preheater.dynamicHX.vol1[1].dynBal.nPorts+2*genericAHU.preheater.dynamicHX.vol1[2].dynBal.nPorts +genericAHU.preheater.dynamicHX.vol2[1].dynBal.nPorts+genericAHU.preheater.dynamicHX.vol2[2].dynBal.nPorts +genericAHU.cooler.hydraulicModule.valve.vol.dynBal.nPorts+genericAHU.cooler.hydraulicModule.pipe1.simplePipe.vol[1].dynBal.nPorts +genericAHU.cooler.hydraulicModule.pipe1.simplePipe.vol[2].dynBal.nPorts+ genericAHU.cooler.hydraulicModule.pipe1.simplePipe.vol[3].dynBal.nPorts+ genericAHU.cooler.hydraulicModule.pipe2.simplePipe.vol[1].dynBal.nPorts+ genericAHU.cooler.hydraulicModule.pipe2.simplePipe.vol[2].dynBal.nPorts+ genericAHU.cooler.hydraulicModule.pipe2.simplePipe.vol[3].dynBal.nPorts+ genericAHU.cooler.hydraulicModule.pipe3.simplePipe.vol[1].dynBal.nPorts+ genericAHU.cooler.hydraulicModule.pipe3.simplePipe.vol[2].dynBal.nPorts+ genericAHU.cooler.hydraulicModule.pipe3.simplePipe.vol[3].dynBal.nPorts+ genericAHU.cooler.hydraulicModule.pipe4.simplePipe.vol[1].dynBal.nPorts+ genericAHU.cooler.hydraulicModule.pipe4.simplePipe.vol[2].dynBal.nPorts+ genericAHU.cooler.hydraulicModule.pipe4.simplePipe.vol[3].dynBal.nPorts+ genericAHU.cooler.hydraulicModule.pipe5.simplePipe.vol[1].dynBal.nPorts+ genericAHU.cooler.hydraulicModule.pipe5.simplePipe.vol[2].dynBal.nPorts+ genericAHU.cooler.hydraulicModule.pipe5.simplePipe.vol[3].dynBal.nPorts+ genericAHU.cooler.hydraulicModule.pipe6.simplePipe.vol[1].dynBal.nPorts+ genericAHU.cooler.hydraulicModule.pipe6.simplePipe.vol[2].dynBal.nPorts+ genericAHU.cooler.hydraulicModule.pipe6.simplePipe.vol[3].dynBal.nPorts+ genericAHU.cooler.hydraulicModule.junc456.dynBal.nPorts+genericAHU.cooler.hydraulicModule.PumpInterface.pump.vol.dynBal.nPorts +2*genericAHU.cooler.dynamicHX.vol1[1].dynBal.nPorts+2*genericAHU.cooler.dynamicHX.vol1[2].dynBal.nPorts +genericAHU.cooler.dynamicHX.vol2[1].dynBal.nPorts+genericAHU.cooler.dynamicHX.vol2[2].dynBal.nPorts +genericAHU.heater.hydraulicModule.valve.vol.dynBal.nPorts+genericAHU.heater.hydraulicModule.pipe1.simplePipe.vol[1].dynBal.nPorts +genericAHU.heater.hydraulicModule.pipe1.simplePipe.vol[2].dynBal.nPorts+ genericAHU.heater.hydraulicModule.pipe1.simplePipe.vol[3].dynBal.nPorts+ genericAHU.heater.hydraulicModule.pipe2.simplePipe.vol[1].dynBal.nPorts+ genericAHU.heater.hydraulicModule.pipe2.simplePipe.vol[2].dynBal.nPorts+ genericAHU.heater.hydraulicModule.pipe2.simplePipe.vol[3].dynBal.nPorts+ genericAHU.heater.hydraulicModule.pipe3.simplePipe.vol[1].dynBal.nPorts+ genericAHU.heater.hydraulicModule.pipe3.simplePipe.vol[2].dynBal.nPorts+ genericAHU.heater.hydraulicModule.pipe3.simplePipe.vol[3].dynBal.nPorts+ genericAHU.heater.hydraulicModule.pipe4.simplePipe.vol[1].dynBal.nPorts+ genericAHU.heater.hydraulicModule.pipe4.simplePipe.vol[2].dynBal.nPorts+ genericAHU.heater.hydraulicModule.pipe4.simplePipe.vol[3].dynBal.nPorts+ genericAHU.heater.hydraulicModule.pipe5.simplePipe.vol[1].dynBal.nPorts+ genericAHU.heater.hydraulicModule.pipe5.simplePipe.vol[2].dynBal.nPorts+ genericAHU.heater.hydraulicModule.pipe5.simplePipe.vol[3].dynBal.nPorts+ genericAHU.heater.hydraulicModule.pipe6.simplePipe.vol[1].dynBal.nPorts+ genericAHU.heater.hydraulicModule.pipe6.simplePipe.vol[2].dynBal.nPorts+ genericAHU.heater.hydraulicModule.pipe6.simplePipe.vol[3].dynBal.nPorts+ genericAHU.heater.hydraulicModule.junc456.dynBal.nPorts+genericAHU.heater.hydraulicModule.PumpInterface.pump.vol.dynBal.nPorts +2*genericAHU.heater.dynamicHX.vol1[1].dynBal.nPorts+2*genericAHU.heater.dynamicHX.vol1[2].dynBal.nPorts +genericAHU.heater.dynamicHX.vol2[1].dynBal.nPorts+genericAHU.heater.dynamicHX.vol2[2].dynBal.nPorts +2*genericAHU.dynamicHX.vol1[1].dynBal.nPorts+2*genericAHU.dynamicHX.vol1[2].dynBal.nPorts +2*genericAHU.dynamicHX.vol2[1].dynBal.nPorts+2*genericAHU.dynamicHX.vol2[2].dynBal.nPorts +2*genericAHU.fanSup.vol.dynBal.nPorts+2*genericAHU.fanRet.vol.dynBal.nPorts+2 *genericAHU.humidifier.vol.dynBal.nPorts+2*genericAHU.humidifierRet.vol.dynBal.nPorts +scalar unknowns and + 8285+(if not genericAHU.humidifier.steamHumidifier then 1 else 0)+(if boundaryOutsideAir.use_Xi_in then 2 else (if boundaryOutsideAir.use_X_in then 1 else 3))+boundaryOutsideAir.nPorts+(if not boundaryOutsideAir.use_p_in then 1 else 0)+boundaryOutsideAir.nPorts+(if not boundaryOutsideAir.use_T_in then 1 else 0)+boundaryOutsideAir.nPorts+(if boundarySupplyAir.use_Xi_in then 2 else (if boundarySupplyAir.use_X_in then 1 else 3))+boundarySupplyAir.nPorts+ (if not boundarySupplyAir.use_p_in then 1 else 0)+boundarySupplyAir.nPorts+( if not boundarySupplyAir.use_T_in then 1 else 0)+boundarySupplyAir.nPorts+( if boundaryExhaustAir.use_Xi_in then 2 else (if boundaryExhaustAir.use_X_in then 1 else 3))+boundaryExhaustAir.nPorts+(if not boundaryExhaustAir.use_p_in then 1 else 0)+boundaryExhaustAir.nPorts+(if not boundaryExhaustAir.use_T_in then 1 else 0)+boundaryExhaustAir.nPorts+(if boundaryReturnAir.use_Xi_in then 2 else (if boundaryReturnAir.use_X_in then 1 else 3))+boundaryReturnAir.nPorts +(if not boundaryReturnAir.use_p_in then 1 else 0)+boundaryReturnAir.nPorts+( if not boundaryReturnAir.use_T_in then 1 else 0)+boundaryReturnAir.nPorts+( if SourcePreheater.use_Xi_in then 1 else (if SourcePreheater.use_X_in then 0 else 1))+(if not SourcePreheater.use_p_in then 1 else 0)+SourcePreheater.nPorts +(if not SourcePreheater.use_T_in then 1 else 0)+SourcePreheater.nPorts+(if SinkPreheater.use_Xi_in then 1 else (if SinkPreheater.use_X_in then 0 else 1)) +(if not SinkPreheater.use_p_in then 1 else 0)+SinkPreheater.nPorts+(if not SinkPreheater.use_T_in then 1 else 0)+SinkPreheater.nPorts+(if SourceCooler.use_Xi_in then 1 else (if SourceCooler.use_X_in then 0 else 1))+( if not SourceCooler.use_p_in then 1 else 0)+SourceCooler.nPorts+(if not SourceCooler.use_T_in then 1 else 0)+SourceCooler.nPorts+(if SinkCooler.use_Xi_in then 1 else (if SinkCooler.use_X_in then 0 else 1))+(if not SinkCooler.use_p_in then 1 else 0)+SinkCooler.nPorts+(if not SinkCooler.use_T_in then 1 else 0)+ SinkCooler.nPorts+(if SourceHeater.use_Xi_in then 1 else (if SourceHeater.use_X_in then 0 else 1))+(if not SourceHeater.use_p_in then 1 else 0)+ SourceHeater.nPorts+(if not SourceHeater.use_T_in then 1 else 0)+ SourceHeater.nPorts+(if SinkHeater.use_Xi_in then 1 else (if SinkHeater.use_X_in then 0 else 1))+(if not SinkHeater.use_p_in then 1 else 0)+SinkHeater.nPorts +(if not SinkHeater.use_T_in then 1 else 0)+SinkHeater.nPorts+(if not genericAHU.preheater.hydraulicModule.pipe1.simplePipe.vol[1].dynBal.use_mWat_flow then 1 else 0)+genericAHU.preheater.hydraulicModule.pipe1.simplePipe.vol[1].dynBal.nPorts +2*genericAHU.preheater.hydraulicModule.pipe1.simplePipe.vol[1].dynBal.nPorts+ (if not genericAHU.preheater.hydraulicModule.pipe1.simplePipe.vol[2].dynBal.use_mWat_flow then 1 else 0)+genericAHU.preheater.hydraulicModule.pipe1.simplePipe.vol[2].dynBal.nPorts +2*genericAHU.preheater.hydraulicModule.pipe1.simplePipe.vol[2].dynBal.nPorts+ (if not genericAHU.preheater.hydraulicModule.pipe1.simplePipe.vol[3].dynBal.use_mWat_flow then 1 else 0)+genericAHU.preheater.hydraulicModule.pipe1.simplePipe.vol[3].dynBal.nPorts +2*genericAHU.preheater.hydraulicModule.pipe1.simplePipe.vol[3].dynBal.nPorts+ (if not genericAHU.preheater.hydraulicModule.pipe2.simplePipe.vol[1].dynBal.use_mWat_flow then 1 else 0)+genericAHU.preheater.hydraulicModule.pipe2.simplePipe.vol[1].dynBal.nPorts +2*genericAHU.preheater.hydraulicModule.pipe2.simplePipe.vol[1].dynBal.nPorts+ (if not genericAHU.preheater.hydraulicModule.pipe2.simplePipe.vol[2].dynBal.use_mWat_flow then 1 else 0)+genericAHU.preheater.hydraulicModule.pipe2.simplePipe.vol[2].dynBal.nPorts +2*genericAHU.preheater.hydraulicModule.pipe2.simplePipe.vol[2].dynBal.nPorts+ (if not genericAHU.preheater.hydraulicModule.pipe2.simplePipe.vol[3].dynBal.use_mWat_flow then 1 else 0)+genericAHU.preheater.hydraulicModule.pipe2.simplePipe.vol[3].dynBal.nPorts +2*genericAHU.preheater.hydraulicModule.pipe2.simplePipe.vol[3].dynBal.nPorts+ (if not genericAHU.preheater.hydraulicModule.pipe3.simplePipe.vol[1].dynBal.use_mWat_flow then 1 else 0)+genericAHU.preheater.hydraulicModule.pipe3.simplePipe.vol[1].dynBal.nPorts +2*genericAHU.preheater.hydraulicModule.pipe3.simplePipe.vol[1].dynBal.nPorts+ (if not genericAHU.preheater.hydraulicModule.pipe3.simplePipe.vol[2].dynBal.use_mWat_flow then 1 else 0)+genericAHU.preheater.hydraulicModule.pipe3.simplePipe.vol[2].dynBal.nPorts +2*genericAHU.preheater.hydraulicModule.pipe3.simplePipe.vol[2].dynBal.nPorts+ (if not genericAHU.preheater.hydraulicModule.pipe3.simplePipe.vol[3].dynBal.use_mWat_flow then 1 else 0)+genericAHU.preheater.hydraulicModule.pipe3.simplePipe.vol[3].dynBal.nPorts +2*genericAHU.preheater.hydraulicModule.pipe3.simplePipe.vol[3].dynBal.nPorts+ (if not genericAHU.preheater.hydraulicModule.pipe4.simplePipe.vol[1].dynBal.use_mWat_flow then 1 else 0)+genericAHU.preheater.hydraulicModule.pipe4.simplePipe.vol[1].dynBal.nPorts +2*genericAHU.preheater.hydraulicModule.pipe4.simplePipe.vol[1].dynBal.nPorts+ (if not genericAHU.preheater.hydraulicModule.pipe4.simplePipe.vol[2].dynBal.use_mWat_flow then 1 else 0)+genericAHU.preheater.hydraulicModule.pipe4.simplePipe.vol[2].dynBal.nPorts +2*genericAHU.preheater.hydraulicModule.pipe4.simplePipe.vol[2].dynBal.nPorts+ (if not genericAHU.preheater.hydraulicModule.pipe4.simplePipe.vol[3].dynBal.use_mWat_flow then 1 else 0)+genericAHU.preheater.hydraulicModule.pipe4.simplePipe.vol[3].dynBal.nPorts +2*genericAHU.preheater.hydraulicModule.pipe4.simplePipe.vol[3].dynBal.nPorts+ (if not genericAHU.preheater.hydraulicModule.pipe5.simplePipe.vol[1].dynBal.use_mWat_flow then 1 else 0)+genericAHU.preheater.hydraulicModule.pipe5.simplePipe.vol[1].dynBal.nPorts +2*genericAHU.preheater.hydraulicModule.pipe5.simplePipe.vol[1].dynBal.nPorts+ (if not genericAHU.preheater.hydraulicModule.pipe5.simplePipe.vol[2].dynBal.use_mWat_flow then 1 else 0)+genericAHU.preheater.hydraulicModule.pipe5.simplePipe.vol[2].dynBal.nPorts +2*genericAHU.preheater.hydraulicModule.pipe5.simplePipe.vol[2].dynBal.nPorts+ (if not genericAHU.preheater.hydraulicModule.pipe5.simplePipe.vol[3].dynBal.use_mWat_flow then 1 else 0)+genericAHU.preheater.hydraulicModule.pipe5.simplePipe.vol[3].dynBal.nPorts +2*genericAHU.preheater.hydraulicModule.pipe5.simplePipe.vol[3].dynBal.nPorts+ (if not genericAHU.preheater.hydraulicModule.pipe6.simplePipe.vol[1].dynBal.use_mWat_flow then 1 else 0)+genericAHU.preheater.hydraulicModule.pipe6.simplePipe.vol[1].dynBal.nPorts +2*genericAHU.preheater.hydraulicModule.pipe6.simplePipe.vol[1].dynBal.nPorts+ (if not genericAHU.preheater.hydraulicModule.pipe6.simplePipe.vol[2].dynBal.use_mWat_flow then 1 else 0)+genericAHU.preheater.hydraulicModule.pipe6.simplePipe.vol[2].dynBal.nPorts +2*genericAHU.preheater.hydraulicModule.pipe6.simplePipe.vol[2].dynBal.nPorts+ (if not genericAHU.preheater.hydraulicModule.pipe6.simplePipe.vol[3].dynBal.use_mWat_flow then 1 else 0)+genericAHU.preheater.hydraulicModule.pipe6.simplePipe.vol[3].dynBal.nPorts +2*genericAHU.preheater.hydraulicModule.pipe6.simplePipe.vol[3].dynBal.nPorts+ (if not genericAHU.preheater.hydraulicModule.junc456.dynBal.use_mWat_flow then 1 else 0)+genericAHU.preheater.hydraulicModule.junc456.dynBal.nPorts+2* genericAHU.preheater.hydraulicModule.junc456.dynBal.nPorts+(if not genericAHU.preheater.hydraulicModule.PumpInterface.pump.vol.dynBal.use_mWat_flow then 1 else 0)+genericAHU.preheater.hydraulicModule.PumpInterface.pump.vol.dynBal.nPorts +2*genericAHU.preheater.hydraulicModule.PumpInterface.pump.vol.dynBal.nPorts+( if not genericAHU.preheater.dynamicHX.vol1[1].dynBal.use_mWat_flow then 1 else 0)+2*genericAHU.preheater.dynamicHX.vol1[1].dynBal.nPorts+3* genericAHU.preheater.dynamicHX.vol1[1].dynBal.nPorts+(if not genericAHU.preheater.dynamicHX.vol1[2].dynBal.use_mWat_flow then 1 else 0)+2*genericAHU.preheater.dynamicHX.vol1[2].dynBal.nPorts+3* genericAHU.preheater.dynamicHX.vol1[2].dynBal.nPorts+(if not genericAHU.preheater.dynamicHX.vol2[1].dynBal.use_mWat_flow then 1 else 0)+genericAHU.preheater.dynamicHX.vol2[1].dynBal.nPorts+2* genericAHU.preheater.dynamicHX.vol2[1].dynBal.nPorts+(if not genericAHU.preheater.dynamicHX.vol2[2].dynBal.use_mWat_flow then 1 else 0)+genericAHU.preheater.dynamicHX.vol2[2].dynBal.nPorts+2* genericAHU.preheater.dynamicHX.vol2[2].dynBal.nPorts+(if not genericAHU.cooler.hydraulicModule.pipe1.simplePipe.vol[1].dynBal.use_mWat_flow then 1 else 0)+genericAHU.cooler.hydraulicModule.pipe1.simplePipe.vol[1].dynBal.nPorts +2*genericAHU.cooler.hydraulicModule.pipe1.simplePipe.vol[1].dynBal.nPorts+( if not genericAHU.cooler.hydraulicModule.pipe1.simplePipe.vol[2].dynBal.use_mWat_flow then 1 else 0)+genericAHU.cooler.hydraulicModule.pipe1.simplePipe.vol[2].dynBal.nPorts +2*genericAHU.cooler.hydraulicModule.pipe1.simplePipe.vol[2].dynBal.nPorts+( if not genericAHU.cooler.hydraulicModule.pipe1.simplePipe.vol[3].dynBal.use_mWat_flow then 1 else 0)+genericAHU.cooler.hydraulicModule.pipe1.simplePipe.vol[3].dynBal.nPorts +2*genericAHU.cooler.hydraulicModule.pipe1.simplePipe.vol[3].dynBal.nPorts+( if not genericAHU.cooler.hydraulicModule.pipe2.simplePipe.vol[1].dynBal.use_mWat_flow then 1 else 0)+genericAHU.cooler.hydraulicModule.pipe2.simplePipe.vol[1].dynBal.nPorts +2*genericAHU.cooler.hydraulicModule.pipe2.simplePipe.vol[1].dynBal.nPorts+( if not genericAHU.cooler.hydraulicModule.pipe2.simplePipe.vol[2].dynBal.use_mWat_flow then 1 else 0)+genericAHU.cooler.hydraulicModule.pipe2.simplePipe.vol[2].dynBal.nPorts +2*genericAHU.cooler.hydraulicModule.pipe2.simplePipe.vol[2].dynBal.nPorts+( if not genericAHU.cooler.hydraulicModule.pipe2.simplePipe.vol[3].dynBal.use_mWat_flow then 1 else 0)+genericAHU.cooler.hydraulicModule.pipe2.simplePipe.vol[3].dynBal.nPorts +2*genericAHU.cooler.hydraulicModule.pipe2.simplePipe.vol[3].dynBal.nPorts+( if not genericAHU.cooler.hydraulicModule.pipe3.simplePipe.vol[1].dynBal.use_mWat_flow then 1 else 0)+genericAHU.cooler.hydraulicModule.pipe3.simplePipe.vol[1].dynBal.nPorts +2*genericAHU.cooler.hydraulicModule.pipe3.simplePipe.vol[1].dynBal.nPorts+( if not genericAHU.cooler.hydraulicModule.pipe3.simplePipe.vol[2].dynBal.use_mWat_flow then 1 else 0)+genericAHU.cooler.hydraulicModule.pipe3.simplePipe.vol[2].dynBal.nPorts +2*genericAHU.cooler.hydraulicModule.pipe3.simplePipe.vol[2].dynBal.nPorts+( if not genericAHU.cooler.hydraulicModule.pipe3.simplePipe.vol[3].dynBal.use_mWat_flow then 1 else 0)+genericAHU.cooler.hydraulicModule.pipe3.simplePipe.vol[3].dynBal.nPorts +2*genericAHU.cooler.hydraulicModule.pipe3.simplePipe.vol[3].dynBal.nPorts+( if not genericAHU.cooler.hydraulicModule.pipe4.simplePipe.vol[1].dynBal.use_mWat_flow then 1 else 0)+genericAHU.cooler.hydraulicModule.pipe4.simplePipe.vol[1].dynBal.nPorts +2*genericAHU.cooler.hydraulicModule.pipe4.simplePipe.vol[1].dynBal.nPorts+( if not genericAHU.cooler.hydraulicModule.pipe4.simplePipe.vol[2].dynBal.use_mWat_flow then 1 else 0)+genericAHU.cooler.hydraulicModule.pipe4.simplePipe.vol[2].dynBal.nPorts +2*genericAHU.cooler.hydraulicModule.pipe4.simplePipe.vol[2].dynBal.nPorts+( if not genericAHU.cooler.hydraulicModule.pipe4.simplePipe.vol[3].dynBal.use_mWat_flow then 1 else 0)+genericAHU.cooler.hydraulicModule.pipe4.simplePipe.vol[3].dynBal.nPorts +2*genericAHU.cooler.hydraulicModule.pipe4.simplePipe.vol[3].dynBal.nPorts+( if not genericAHU.cooler.hydraulicModule.pipe5.simplePipe.vol[1].dynBal.use_mWat_flow then 1 else 0)+genericAHU.cooler.hydraulicModule.pipe5.simplePipe.vol[1].dynBal.nPorts +2*genericAHU.cooler.hydraulicModule.pipe5.simplePipe.vol[1].dynBal.nPorts+( if not genericAHU.cooler.hydraulicModule.pipe5.simplePipe.vol[2].dynBal.use_mWat_flow then 1 else 0)+genericAHU.cooler.hydraulicModule.pipe5.simplePipe.vol[2].dynBal.nPorts +2*genericAHU.cooler.hydraulicModule.pipe5.simplePipe.vol[2].dynBal.nPorts+( if not genericAHU.cooler.hydraulicModule.pipe5.simplePipe.vol[3].dynBal.use_mWat_flow then 1 else 0)+genericAHU.cooler.hydraulicModule.pipe5.simplePipe.vol[3].dynBal.nPorts +2*genericAHU.cooler.hydraulicModule.pipe5.simplePipe.vol[3].dynBal.nPorts+( if not genericAHU.cooler.hydraulicModule.pipe6.simplePipe.vol[1].dynBal.use_mWat_flow then 1 else 0)+genericAHU.cooler.hydraulicModule.pipe6.simplePipe.vol[1].dynBal.nPorts +2*genericAHU.cooler.hydraulicModule.pipe6.simplePipe.vol[1].dynBal.nPorts+( if not genericAHU.cooler.hydraulicModule.pipe6.simplePipe.vol[2].dynBal.use_mWat_flow then 1 else 0)+genericAHU.cooler.hydraulicModule.pipe6.simplePipe.vol[2].dynBal.nPorts +2*genericAHU.cooler.hydraulicModule.pipe6.simplePipe.vol[2].dynBal.nPorts+( if not genericAHU.cooler.hydraulicModule.pipe6.simplePipe.vol[3].dynBal.use_mWat_flow then 1 else 0)+genericAHU.cooler.hydraulicModule.pipe6.simplePipe.vol[3].dynBal.nPorts +2*genericAHU.cooler.hydraulicModule.pipe6.simplePipe.vol[3].dynBal.nPorts+( if not genericAHU.cooler.hydraulicModule.junc456.dynBal.use_mWat_flow then 1 else 0)+genericAHU.cooler.hydraulicModule.junc456.dynBal.nPorts+2* genericAHU.cooler.hydraulicModule.junc456.dynBal.nPorts+(if not genericAHU.cooler.hydraulicModule.PumpInterface.pump.vol.dynBal.use_mWat_flow then 1 else 0)+genericAHU.cooler.hydraulicModule.PumpInterface.pump.vol.dynBal.nPorts +2*genericAHU.cooler.hydraulicModule.PumpInterface.pump.vol.dynBal.nPorts+(if not genericAHU.cooler.dynamicHX.vol1[1].dynBal.use_mWat_flow then 1 else 0)+2 *genericAHU.cooler.dynamicHX.vol1[1].dynBal.nPorts+3*genericAHU.cooler.dynamicHX.vol1[1].dynBal.nPorts +(if not genericAHU.cooler.dynamicHX.vol1[2].dynBal.use_mWat_flow then 1 else 0)+2*genericAHU.cooler.dynamicHX.vol1[2].dynBal.nPorts+3* genericAHU.cooler.dynamicHX.vol1[2].dynBal.nPorts+(if not genericAHU.cooler.dynamicHX.vol2[1].dynBal.use_mWat_flow then 1 else 0)+genericAHU.cooler.dynamicHX.vol2[1].dynBal.nPorts+2* genericAHU.cooler.dynamicHX.vol2[1].dynBal.nPorts+(if not genericAHU.cooler.dynamicHX.vol2[2].dynBal.use_mWat_flow then 1 else 0)+genericAHU.cooler.dynamicHX.vol2[2].dynBal.nPorts+2* genericAHU.cooler.dynamicHX.vol2[2].dynBal.nPorts+(if not genericAHU.heater.hydraulicModule.pipe1.simplePipe.vol[1].dynBal.use_mWat_flow then 1 else 0)+genericAHU.heater.hydraulicModule.pipe1.simplePipe.vol[1].dynBal.nPorts +2*genericAHU.heater.hydraulicModule.pipe1.simplePipe.vol[1].dynBal.nPorts+( if not genericAHU.heater.hydraulicModule.pipe1.simplePipe.vol[2].dynBal.use_mWat_flow then 1 else 0)+genericAHU.heater.hydraulicModule.pipe1.simplePipe.vol[2].dynBal.nPorts +2*genericAHU.heater.hydraulicModule.pipe1.simplePipe.vol[2].dynBal.nPorts+( if not genericAHU.heater.hydraulicModule.pipe1.simplePipe.vol[3].dynBal.use_mWat_flow then 1 else 0)+genericAHU.heater.hydraulicModule.pipe1.simplePipe.vol[3].dynBal.nPorts +2*genericAHU.heater.hydraulicModule.pipe1.simplePipe.vol[3].dynBal.nPorts+( if not genericAHU.heater.hydraulicModule.pipe2.simplePipe.vol[1].dynBal.use_mWat_flow then 1 else 0)+genericAHU.heater.hydraulicModule.pipe2.simplePipe.vol[1].dynBal.nPorts +2*genericAHU.heater.hydraulicModule.pipe2.simplePipe.vol[1].dynBal.nPorts+( if not genericAHU.heater.hydraulicModule.pipe2.simplePipe.vol[2].dynBal.use_mWat_flow then 1 else 0)+genericAHU.heater.hydraulicModule.pipe2.simplePipe.vol[2].dynBal.nPorts +2*genericAHU.heater.hydraulicModule.pipe2.simplePipe.vol[2].dynBal.nPorts+( if not genericAHU.heater.hydraulicModule.pipe2.simplePipe.vol[3].dynBal.use_mWat_flow then 1 else 0)+genericAHU.heater.hydraulicModule.pipe2.simplePipe.vol[3].dynBal.nPorts +2*genericAHU.heater.hydraulicModule.pipe2.simplePipe.vol[3].dynBal.nPorts+( if not genericAHU.heater.hydraulicModule.pipe3.simplePipe.vol[1].dynBal.use_mWat_flow then 1 else 0)+genericAHU.heater.hydraulicModule.pipe3.simplePipe.vol[1].dynBal.nPorts +2*genericAHU.heater.hydraulicModule.pipe3.simplePipe.vol[1].dynBal.nPorts+( if not genericAHU.heater.hydraulicModule.pipe3.simplePipe.vol[2].dynBal.use_mWat_flow then 1 else 0)+genericAHU.heater.hydraulicModule.pipe3.simplePipe.vol[2].dynBal.nPorts +2*genericAHU.heater.hydraulicModule.pipe3.simplePipe.vol[2].dynBal.nPorts+( if not genericAHU.heater.hydraulicModule.pipe3.simplePipe.vol[3].dynBal.use_mWat_flow then 1 else 0)+genericAHU.heater.hydraulicModule.pipe3.simplePipe.vol[3].dynBal.nPorts +2*genericAHU.heater.hydraulicModule.pipe3.simplePipe.vol[3].dynBal.nPorts+( if not genericAHU.heater.hydraulicModule.pipe4.simplePipe.vol[1].dynBal.use_mWat_flow then 1 else 0)+genericAHU.heater.hydraulicModule.pipe4.simplePipe.vol[1].dynBal.nPorts +2*genericAHU.heater.hydraulicModule.pipe4.simplePipe.vol[1].dynBal.nPorts+( if not genericAHU.heater.hydraulicModule.pipe4.simplePipe.vol[2].dynBal.use_mWat_flow then 1 else 0)+genericAHU.heater.hydraulicModule.pipe4.simplePipe.vol[2].dynBal.nPorts +2*genericAHU.heater.hydraulicModule.pipe4.simplePipe.vol[2].dynBal.nPorts+( if not genericAHU.heater.hydraulicModule.pipe4.simplePipe.vol[3].dynBal.use_mWat_flow then 1 else 0)+genericAHU.heater.hydraulicModule.pipe4.simplePipe.vol[3].dynBal.nPorts +2*genericAHU.heater.hydraulicModule.pipe4.simplePipe.vol[3].dynBal.nPorts+( if not genericAHU.heater.hydraulicModule.pipe5.simplePipe.vol[1].dynBal.use_mWat_flow then 1 else 0)+genericAHU.heater.hydraulicModule.pipe5.simplePipe.vol[1].dynBal.nPorts +2*genericAHU.heater.hydraulicModule.pipe5.simplePipe.vol[1].dynBal.nPorts+( if not genericAHU.heater.hydraulicModule.pipe5.simplePipe.vol[2].dynBal.use_mWat_flow then 1 else 0)+genericAHU.heater.hydraulicModule.pipe5.simplePipe.vol[2].dynBal.nPorts +2*genericAHU.heater.hydraulicModule.pipe5.simplePipe.vol[2].dynBal.nPorts+( if not genericAHU.heater.hydraulicModule.pipe5.simplePipe.vol[3].dynBal.use_mWat_flow then 1 else 0)+genericAHU.heater.hydraulicModule.pipe5.simplePipe.vol[3].dynBal.nPorts +2*genericAHU.heater.hydraulicModule.pipe5.simplePipe.vol[3].dynBal.nPorts+( if not genericAHU.heater.hydraulicModule.pipe6.simplePipe.vol[1].dynBal.use_mWat_flow then 1 else 0)+genericAHU.heater.hydraulicModule.pipe6.simplePipe.vol[1].dynBal.nPorts +2*genericAHU.heater.hydraulicModule.pipe6.simplePipe.vol[1].dynBal.nPorts+( if not genericAHU.heater.hydraulicModule.pipe6.simplePipe.vol[2].dynBal.use_mWat_flow then 1 else 0)+genericAHU.heater.hydraulicModule.pipe6.simplePipe.vol[2].dynBal.nPorts +2*genericAHU.heater.hydraulicModule.pipe6.simplePipe.vol[2].dynBal.nPorts+( if not genericAHU.heater.hydraulicModule.pipe6.simplePipe.vol[3].dynBal.use_mWat_flow then 1 else 0)+genericAHU.heater.hydraulicModule.pipe6.simplePipe.vol[3].dynBal.nPorts +2*genericAHU.heater.hydraulicModule.pipe6.simplePipe.vol[3].dynBal.nPorts+( if not genericAHU.heater.hydraulicModule.junc456.dynBal.use_mWat_flow then 1 else 0)+genericAHU.heater.hydraulicModule.junc456.dynBal.nPorts+2* genericAHU.heater.hydraulicModule.junc456.dynBal.nPorts+(if not genericAHU.heater.hydraulicModule.PumpInterface.pump.vol.dynBal.use_mWat_flow then 1 else 0)+genericAHU.heater.hydraulicModule.PumpInterface.pump.vol.dynBal.nPorts +2*genericAHU.heater.hydraulicModule.PumpInterface.pump.vol.dynBal.nPorts+(if not genericAHU.heater.dynamicHX.vol1[1].dynBal.use_mWat_flow then 1 else 0)+2 *genericAHU.heater.dynamicHX.vol1[1].dynBal.nPorts+3*genericAHU.heater.dynamicHX.vol1[1].dynBal.nPorts +(if not genericAHU.heater.dynamicHX.vol1[2].dynBal.use_mWat_flow then 1 else 0)+2*genericAHU.heater.dynamicHX.vol1[2].dynBal.nPorts+3* genericAHU.heater.dynamicHX.vol1[2].dynBal.nPorts+(if not genericAHU.heater.dynamicHX.vol2[1].dynBal.use_mWat_flow then 1 else 0)+genericAHU.heater.dynamicHX.vol2[1].dynBal.nPorts+2* genericAHU.heater.dynamicHX.vol2[1].dynBal.nPorts+(if not genericAHU.heater.dynamicHX.vol2[2].dynBal.use_mWat_flow then 1 else 0)+genericAHU.heater.dynamicHX.vol2[2].dynBal.nPorts+2* genericAHU.heater.dynamicHX.vol2[2].dynBal.nPorts+(if not genericAHU.dynamicHX.vol1[1].dynBal.use_mWat_flow then 1 else 0)+2*genericAHU.dynamicHX.vol1[1].dynBal.nPorts+3* genericAHU.dynamicHX.vol1[1].dynBal.nPorts+(if not genericAHU.dynamicHX.vol1[2].dynBal.use_mWat_flow then 1 else 0)+2*genericAHU.dynamicHX.vol1[2].dynBal.nPorts+3* genericAHU.dynamicHX.vol1[2].dynBal.nPorts+(if not genericAHU.dynamicHX.vol2[1].dynBal.use_mWat_flow then 1 else 0)+2*genericAHU.dynamicHX.vol2[1].dynBal.nPorts+3* genericAHU.dynamicHX.vol2[1].dynBal.nPorts+(if not genericAHU.dynamicHX.vol2[2].dynBal.use_mWat_flow then 1 else 0)+2*genericAHU.dynamicHX.vol2[2].dynBal.nPorts+3* genericAHU.dynamicHX.vol2[2].dynBal.nPorts+(if not genericAHU.fanSup.vol.dynBal.use_mWat_flow then 1 else 0)+2*genericAHU.fanSup.vol.dynBal.nPorts+3*genericAHU.fanSup.vol.dynBal.nPorts +(if not genericAHU.fanRet.vol.dynBal.use_mWat_flow then 1 else 0)+2* genericAHU.fanRet.vol.dynBal.nPorts+3*genericAHU.fanRet.vol.dynBal.nPorts+2* genericAHU.humidifier.vol.dynBal.nPorts+3*genericAHU.humidifier.vol.dynBal.nPorts +2*genericAHU.humidifierRet.vol.dynBal.nPorts+3*genericAHU.humidifierRet.vol.dynBal.nPorts +(if not genericAHU.preheater.hydraulicModule.valve.vol.dynBal.use_mWat_flow then 1 else 0)+genericAHU.preheater.hydraulicModule.valve.vol.dynBal.nPorts+2 *genericAHU.preheater.hydraulicModule.valve.vol.dynBal.nPorts+(if not genericAHU.cooler.hydraulicModule.valve.vol.dynBal.use_mWat_flow then 1 else 0) +genericAHU.cooler.hydraulicModule.valve.vol.dynBal.nPorts+2*genericAHU.cooler.hydraulicModule.valve.vol.dynBal.nPorts +(if not genericAHU.heater.hydraulicModule.valve.vol.dynBal.use_mWat_flow then 1 else 0)+genericAHU.heater.hydraulicModule.valve.vol.dynBal.nPorts+2* genericAHU.heater.hydraulicModule.valve.vol.dynBal.nPorts +scalar equations. +However, exploiting the given numerical settings of parameters gives the same number of unknowns and equations: + 9000 +Check of AixLib.Systems.ModularAHU.Examples.GenericAHU successful. +Declaring variable: Boolean rCheck ; + +Modelica.Utilities.Streams.print(" { \"file\" : \"AixLib/Resources/Scripts/Dymola/Systems/ModularAHU/Examples/GenericAHU.mos\",", "AixLib.Systems.ModularAHU.Examples.GenericAHU.statistics.log"); +Modelica.Utilities.Streams.print(" \"model\" : \"AixLib.Systems.ModularAHU.Examples.GenericAHU\",", "AixLib.Systems.ModularAHU.Examples.GenericAHU.statistics.log"); +Modelica.Utilities.Streams.print(" \"check\" : {", "AixLib.Systems.ModularAHU.Examples.GenericAHU.statistics.log"); +Modelica.Utilities.Streams.print(" \"command\" : \"checkModel(\\\"AixLib.Systems.ModularAHU.Examples.GenericAHU\\\");\",", "AixLib.Systems.ModularAHU.Examples.GenericAHU.statistics.log"); +Modelica.Utilities.Streams.print(" \"result\" : " + String(rCheck), "AixLib.Systems.ModularAHU.Examples.GenericAHU.statistics.log"); +Modelica.Utilities.Streams.print(" },", "AixLib.Systems.ModularAHU.Examples.GenericAHU.statistics.log"); + + +rScript=RunScript("modelica://AixLib/Resources/Scripts/Dymola/Systems/ModularAHU/Examples/GenericAHU.mos"); +simulateModel("AixLib.Systems.ModularAHU.Examples.GenericAHU", stopTime=7200, method="dassl", tolerance=1e-6, resultFile="AixLib.Systems.ModularAHU.Examples.GenericAHU"); +Translation of AixLib.Systems.ModularAHU.Examples.GenericAHU +The DAE has 9000 scalar unknowns and 9000 scalar equations. +Redundant consistent initial conditions. +Removed the following equations which are redundant and consistent: + genericAHU.preheater.dynamicHX.vol1[2].p_start = genericAHU.preheater.dynamicHX.p1_start; + genericAHU.cooler.dynamicHX.vol1[1].p_start = genericAHU.cooler.dynamicHX.p1_start; + genericAHU.heater.dynamicHX.vol1[2].p_start = genericAHU.heater.dynamicHX.p1_start; + genericAHU.dynamicHX.vol1[1].p_start = genericAHU.dynamicHX.p1_start; + genericAHU.dynamicHX.vol2[1].p_start = genericAHU.dynamicHX.p2_start; + genericAHU.fanSup.vol.p_start = genericAHU.fanSup.p_start; + genericAHU.humidifier.vol.p_start = genericAHU.humidifier.p_start; + if (genericAHU.dynamicHX.vol1[2].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (genericAHU.dynamicHX.vol1[2].dynBal.initialize_p) then + genericAHU.dynamicHX.vol1[2].dynBal.medium.p = genericAHU.dynamicHX.vol1[2].dynBal.p_start; + end if; + else + if (genericAHU.dynamicHX.vol1[2].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. SteadyStateInitial) then + if (genericAHU.dynamicHX.vol1[2].dynBal.initialize_p) then + der(genericAHU.dynamicHX.vol1[2].dynBal.medium.p) = 0; + end if; + end if; + end if; + +This required evaluation of +the interactive parameters + boundaryExhaustAir.p(start = 101325) + boundarySupplyAir.p(start = 101325) + genericAHU.dynamicHX.p1_start(start = 101325) + genericAHU.fanSup.dp_start(start = 0) + genericAHU.fanSup.p_start(start = 101325) + genericAHU.humidifier.p_start(start = 101325) + +The redundancies involve +initial equations: + genericAHU.fanSup.filter.y = genericAHU.fanSup.filter.y_start; + genericAHU.preheater.dynamicHX.vol1[1].dynBal.medium.p = genericAHU.preheater.dynamicHX.vol1[1].dynBal.p_start; + genericAHU.preheater.dynamicHX.vol1[2].dynBal.medium.p = genericAHU.preheater.dynamicHX.vol1[2].dynBal.p_start; + genericAHU.cooler.dynamicHX.vol1[1].dynBal.medium.p = genericAHU.cooler.dynamicHX.vol1[1].dynBal.p_start; + genericAHU.cooler.dynamicHX.vol1[2].dynBal.medium.p = genericAHU.cooler.dynamicHX.vol1[2].dynBal.p_start; + genericAHU.heater.dynamicHX.vol1[1].dynBal.medium.p = genericAHU.heater.dynamicHX.vol1[1].dynBal.p_start; + genericAHU.heater.dynamicHX.vol1[2].dynBal.medium.p = genericAHU.heater.dynamicHX.vol1[2].dynBal.p_start; + genericAHU.dynamicHX.vol1[1].dynBal.medium.p = genericAHU.dynamicHX.vol1[1].dynBal.p_start; + genericAHU.dynamicHX.vol1[2].dynBal.medium.p = genericAHU.dynamicHX.vol1[2].dynBal.p_start; + genericAHU.dynamicHX.vol2[1].dynBal.medium.p = genericAHU.dynamicHX.vol2[1].dynBal.p_start; + genericAHU.dynamicHX.vol2[2].dynBal.medium.p = genericAHU.dynamicHX.vol2[2].dynBal.p_start; + genericAHU.fanSup.vol.dynBal.medium.p = genericAHU.fanSup.vol.dynBal.p_start; + genericAHU.humidifier.vol.dynBal.medium.p = genericAHU.humidifier.vol.dynBal.p_start; + + +Statistics + +Original Model + Number of components: 1899 + Variables: 23029 + Constants: 457 (457 scalars) + Parameters: 10980 (11860 scalars) + Unknowns: 11592 (9419 scalars) + Differentiated variables: 337 scalars + Equations: 8571 + Nontrivial: 6714 +Translated Model + Constants: 8236 scalars + Free parameters: 846 scalars + Parameter depending: 4221 scalars + Continuous time states: 260 scalars + Time-varying variables: 2222 scalars + Alias variables: 6211 scalars + Number of mixed real/discrete systems of equations: 0 + Sizes of linear systems of equations: {3, 3, 3, 3, 5, 2, 5, 2, 5, 2, 5, 2, 5, 2, 5, 2, 5, 2, 5, 2, 5, 2, 5, 2, 5, 2, 5, 2, 5, 2, 5, 2, 5, 2, 5, 2, 5, 2, 5, 2} + Sizes after manipulation of the linear systems: {0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0} + Sizes of nonlinear systems of equations: {1, 1, 1, 3, 1, 4, 1, 1, 1, 21, 21, 21} + Sizes after manipulation of the nonlinear systems: {0, 0, 0, 1, 0, 1, 0, 0, 0, 2, 2, 2} + Number of numerical Jacobians: 0 + Initialization problem + Sizes of nonlinear systems of equations: {1, 1, 1, 3, 1, 4, 1, 1, 21, 1, 21, 1, 21, 1} + Sizes after manipulation of the nonlinear systems: {0, 0, 0, 1, 0, 1, 0, 0, 4, 0, 4, 0, 4, 0} + Sizes of simplified homotopy nonlinear systems of equations: {3, 1, 4, 1, 21, 1, 21, 1, 21, 1} + Sizes after manipulation of the simplified homotopy nonlinear systems: {1, 0, 1, 0, 3, 0, 3, 0, 3, 0} + Number of numerical Jacobians: 0 + +Sparse solvers enabled: false +Enabled for integrator Jacobian: false +Model sparse and large enough: true. +Sparse solvers are available for dassl, lsodar, cvode, ida, radau, esdirk*, sdirk*. +Enable sparse solvers by setting Advanced.Translation.SparseActivate. +Selected continuous time states +Statically selected continuous time states +ctrAHUBasic.ctrCo.PID.D.x +ctrAHUBasic.ctrCo.PID.I.y +ctrAHUBasic.ctrPh.PID.D.x +ctrAHUBasic.ctrPh.PID.I.y +ctrAHUBasic.ctrRh.PID.D.x +ctrAHUBasic.ctrRh.PID.I.y +ctrAHUBasic.PID_VflowRet.D.x +ctrAHUBasic.PID_VflowRet.I.y +ctrAHUBasic.PID_VflowSup.D.x +ctrAHUBasic.PID_VflowSup.I.y +genericAHU.cooler.dynamicHX.heatCapacitor[1].T +genericAHU.cooler.dynamicHX.heatCapacitor[2].T +genericAHU.cooler.dynamicHX.vol1[1].dynBal.medium.Xi[1] +genericAHU.cooler.dynamicHX.vol1[1].dynBal.U +genericAHU.cooler.dynamicHX.vol1[2].dynBal.medium.Xi[1] +genericAHU.cooler.dynamicHX.vol1[2].dynBal.U +genericAHU.cooler.dynamicHX.vol2[1].dynBal.U +genericAHU.cooler.dynamicHX.vol2[2].dynBal.U +genericAHU.cooler.hydraulicModule.junc456.dynBal.U +genericAHU.cooler.hydraulicModule.pipe1.Insulation.CylindricLoad1.heatCapacitor.T +genericAHU.cooler.hydraulicModule.pipe1.simplePipe.PipeWall[1].CylindricLoad1.heatCapacitor.T +genericAHU.cooler.hydraulicModule.pipe1.simplePipe.PipeWall[2].CylindricLoad1.heatCapacitor.T +genericAHU.cooler.hydraulicModule.pipe1.simplePipe.PipeWall[3].CylindricLoad1.heatCapacitor.T +genericAHU.cooler.hydraulicModule.pipe1.simplePipe.vol[1].dynBal.U +genericAHU.cooler.hydraulicModule.pipe1.simplePipe.vol[2].dynBal.U +genericAHU.cooler.hydraulicModule.pipe1.simplePipe.vol[3].dynBal.U +genericAHU.cooler.hydraulicModule.pipe2.Insulation.CylindricLoad1.heatCapacitor.T +genericAHU.cooler.hydraulicModule.pipe2.simplePipe.PipeWall[1].CylindricLoad1.heatCapacitor.T +genericAHU.cooler.hydraulicModule.pipe2.simplePipe.PipeWall[2].CylindricLoad1.heatCapacitor.T +genericAHU.cooler.hydraulicModule.pipe2.simplePipe.PipeWall[3].CylindricLoad1.heatCapacitor.T +genericAHU.cooler.hydraulicModule.pipe2.simplePipe.vol[1].dynBal.U +genericAHU.cooler.hydraulicModule.pipe2.simplePipe.vol[2].dynBal.U +genericAHU.cooler.hydraulicModule.pipe2.simplePipe.vol[3].dynBal.U +genericAHU.cooler.hydraulicModule.pipe3.Insulation.CylindricLoad1.heatCapacitor.T +genericAHU.cooler.hydraulicModule.pipe3.simplePipe.PipeWall[1].CylindricLoad1.heatCapacitor.T +genericAHU.cooler.hydraulicModule.pipe3.simplePipe.PipeWall[2].CylindricLoad1.heatCapacitor.T +genericAHU.cooler.hydraulicModule.pipe3.simplePipe.PipeWall[3].CylindricLoad1.heatCapacitor.T +genericAHU.cooler.hydraulicModule.pipe3.simplePipe.vol[1].dynBal.U +genericAHU.cooler.hydraulicModule.pipe3.simplePipe.vol[2].dynBal.U +genericAHU.cooler.hydraulicModule.pipe3.simplePipe.vol[3].dynBal.U +genericAHU.cooler.hydraulicModule.pipe4.Insulation.CylindricLoad1.heatCapacitor.T +genericAHU.cooler.hydraulicModule.pipe4.simplePipe.PipeWall[1].CylindricLoad1.heatCapacitor.T +genericAHU.cooler.hydraulicModule.pipe4.simplePipe.PipeWall[2].CylindricLoad1.heatCapacitor.T +genericAHU.cooler.hydraulicModule.pipe4.simplePipe.PipeWall[3].CylindricLoad1.heatCapacitor.T +genericAHU.cooler.hydraulicModule.pipe4.simplePipe.vol[1].dynBal.U +genericAHU.cooler.hydraulicModule.pipe4.simplePipe.vol[2].dynBal.U +genericAHU.cooler.hydraulicModule.pipe4.simplePipe.vol[3].dynBal.U +genericAHU.cooler.hydraulicModule.pipe5.Insulation.CylindricLoad1.heatCapacitor.T +genericAHU.cooler.hydraulicModule.pipe5.simplePipe.PipeWall[1].CylindricLoad1.heatCapacitor.T +genericAHU.cooler.hydraulicModule.pipe5.simplePipe.PipeWall[2].CylindricLoad1.heatCapacitor.T +genericAHU.cooler.hydraulicModule.pipe5.simplePipe.PipeWall[3].CylindricLoad1.heatCapacitor.T +genericAHU.cooler.hydraulicModule.pipe5.simplePipe.vol[1].dynBal.U +genericAHU.cooler.hydraulicModule.pipe5.simplePipe.vol[2].dynBal.U +genericAHU.cooler.hydraulicModule.pipe5.simplePipe.vol[3].dynBal.U +genericAHU.cooler.hydraulicModule.pipe6.Insulation.CylindricLoad1.heatCapacitor.T +genericAHU.cooler.hydraulicModule.pipe6.simplePipe.PipeWall[1].CylindricLoad1.heatCapacitor.T +genericAHU.cooler.hydraulicModule.pipe6.simplePipe.PipeWall[2].CylindricLoad1.heatCapacitor.T +genericAHU.cooler.hydraulicModule.pipe6.simplePipe.PipeWall[3].CylindricLoad1.heatCapacitor.T +genericAHU.cooler.hydraulicModule.pipe6.simplePipe.vol[1].dynBal.U +genericAHU.cooler.hydraulicModule.pipe6.simplePipe.vol[2].dynBal.U +genericAHU.cooler.hydraulicModule.pipe6.simplePipe.vol[3].dynBal.U +genericAHU.cooler.hydraulicModule.PT1_a1.y +genericAHU.cooler.hydraulicModule.PT1_a2.y +genericAHU.cooler.hydraulicModule.PT1_b1.y +genericAHU.cooler.hydraulicModule.PT1_b2.y +genericAHU.cooler.hydraulicModule.PumpInterface.pump.filter.s[1] +genericAHU.cooler.hydraulicModule.PumpInterface.pump.filter.s[2] +genericAHU.cooler.hydraulicModule.PumpInterface.pump.vol.dynBal.U +genericAHU.cooler.hydraulicModule.senT_a1.T +genericAHU.cooler.hydraulicModule.senT_a2.T +genericAHU.cooler.hydraulicModule.senT_b1.T +genericAHU.cooler.hydraulicModule.senT_b2.T +genericAHU.cooler.hydraulicModule.valve.filter.s[1] +genericAHU.cooler.hydraulicModule.valve.vol.dynBal.U +genericAHU.cooler.port_a1.p +genericAHU.cooler.port_b1.p +genericAHU.cooler.PT1_airIn.y +genericAHU.cooler.PT1_airOut.y +genericAHU.cooler.senT_airIn.T +genericAHU.cooler.senT_airOut.T +genericAHU.dampBypass.filter.s[1] +genericAHU.dampBypass.filter.s[2] +genericAHU.dampHX.filter.s[1] +genericAHU.dampHX.filter.s[2] +genericAHU.dampHX.port_a.p +genericAHU.dynamicHX.heatCapacitor[1].T +genericAHU.dynamicHX.heatCapacitor[2].T +genericAHU.dynamicHX.vol1[1].dynBal.medium.Xi[1] +genericAHU.dynamicHX.vol1[1].dynBal.U +genericAHU.dynamicHX.vol1[2].dynBal.medium.Xi[1] +genericAHU.dynamicHX.vol1[2].dynBal.U +genericAHU.dynamicHX.vol2[1].dynBal.medium.Xi[1] +genericAHU.dynamicHX.vol2[1].dynBal.U +genericAHU.dynamicHX.vol2[2].dynBal.medium.Xi[1] +genericAHU.dynamicHX.vol2[2].dynBal.U +genericAHU.fanRet.filter.s[1] +genericAHU.fanRet.filter.s[2] +genericAHU.fanRet.vol.dynBal.m +genericAHU.fanRet.vol.dynBal.medium.Xi[1] +genericAHU.fanRet.vol.dynBal.U +genericAHU.fanSup.filter.s[1] +genericAHU.fanSup.filter.s[2] +genericAHU.fanSup.vol.dynBal.medium.Xi[1] +genericAHU.fanSup.vol.dynBal.U +genericAHU.flapRet.filter.s[1] +genericAHU.flapRet.filter.s[2] +genericAHU.flapSup.filter.s[1] +genericAHU.flapSup.filter.s[2] +genericAHU.heater.dynamicHX.heatCapacitor[1].T +genericAHU.heater.dynamicHX.heatCapacitor[2].T +genericAHU.heater.dynamicHX.vol1[1].dynBal.medium.Xi[1] +genericAHU.heater.dynamicHX.vol1[1].dynBal.U +genericAHU.heater.dynamicHX.vol1[2].dynBal.medium.Xi[1] +genericAHU.heater.dynamicHX.vol1[2].dynBal.U +genericAHU.heater.dynamicHX.vol2[1].dynBal.U +genericAHU.heater.dynamicHX.vol2[2].dynBal.U +genericAHU.heater.hydraulicModule.junc456.dynBal.U +genericAHU.heater.hydraulicModule.pipe1.Insulation.CylindricLoad1.heatCapacitor.T +genericAHU.heater.hydraulicModule.pipe1.simplePipe.PipeWall[1].CylindricLoad1.heatCapacitor.T +genericAHU.heater.hydraulicModule.pipe1.simplePipe.PipeWall[2].CylindricLoad1.heatCapacitor.T +genericAHU.heater.hydraulicModule.pipe1.simplePipe.PipeWall[3].CylindricLoad1.heatCapacitor.T +genericAHU.heater.hydraulicModule.pipe1.simplePipe.vol[1].dynBal.U +genericAHU.heater.hydraulicModule.pipe1.simplePipe.vol[2].dynBal.U +genericAHU.heater.hydraulicModule.pipe1.simplePipe.vol[3].dynBal.U +genericAHU.heater.hydraulicModule.pipe2.Insulation.CylindricLoad1.heatCapacitor.T +genericAHU.heater.hydraulicModule.pipe2.simplePipe.PipeWall[1].CylindricLoad1.heatCapacitor.T +genericAHU.heater.hydraulicModule.pipe2.simplePipe.PipeWall[2].CylindricLoad1.heatCapacitor.T +genericAHU.heater.hydraulicModule.pipe2.simplePipe.PipeWall[3].CylindricLoad1.heatCapacitor.T +genericAHU.heater.hydraulicModule.pipe2.simplePipe.vol[1].dynBal.U +genericAHU.heater.hydraulicModule.pipe2.simplePipe.vol[2].dynBal.U +genericAHU.heater.hydraulicModule.pipe2.simplePipe.vol[3].dynBal.U +genericAHU.heater.hydraulicModule.pipe3.Insulation.CylindricLoad1.heatCapacitor.T +genericAHU.heater.hydraulicModule.pipe3.simplePipe.PipeWall[1].CylindricLoad1.heatCapacitor.T +genericAHU.heater.hydraulicModule.pipe3.simplePipe.PipeWall[2].CylindricLoad1.heatCapacitor.T +genericAHU.heater.hydraulicModule.pipe3.simplePipe.PipeWall[3].CylindricLoad1.heatCapacitor.T +genericAHU.heater.hydraulicModule.pipe3.simplePipe.vol[1].dynBal.U +genericAHU.heater.hydraulicModule.pipe3.simplePipe.vol[2].dynBal.U +genericAHU.heater.hydraulicModule.pipe3.simplePipe.vol[3].dynBal.U +genericAHU.heater.hydraulicModule.pipe4.Insulation.CylindricLoad1.heatCapacitor.T +genericAHU.heater.hydraulicModule.pipe4.simplePipe.PipeWall[1].CylindricLoad1.heatCapacitor.T +genericAHU.heater.hydraulicModule.pipe4.simplePipe.PipeWall[2].CylindricLoad1.heatCapacitor.T +genericAHU.heater.hydraulicModule.pipe4.simplePipe.PipeWall[3].CylindricLoad1.heatCapacitor.T +genericAHU.heater.hydraulicModule.pipe4.simplePipe.vol[1].dynBal.U +genericAHU.heater.hydraulicModule.pipe4.simplePipe.vol[2].dynBal.U +genericAHU.heater.hydraulicModule.pipe4.simplePipe.vol[3].dynBal.U +genericAHU.heater.hydraulicModule.pipe5.Insulation.CylindricLoad1.heatCapacitor.T +genericAHU.heater.hydraulicModule.pipe5.simplePipe.PipeWall[1].CylindricLoad1.heatCapacitor.T +genericAHU.heater.hydraulicModule.pipe5.simplePipe.PipeWall[2].CylindricLoad1.heatCapacitor.T +genericAHU.heater.hydraulicModule.pipe5.simplePipe.PipeWall[3].CylindricLoad1.heatCapacitor.T +genericAHU.heater.hydraulicModule.pipe5.simplePipe.vol[1].dynBal.U +genericAHU.heater.hydraulicModule.pipe5.simplePipe.vol[2].dynBal.U +genericAHU.heater.hydraulicModule.pipe5.simplePipe.vol[3].dynBal.U +genericAHU.heater.hydraulicModule.pipe6.Insulation.CylindricLoad1.heatCapacitor.T +genericAHU.heater.hydraulicModule.pipe6.simplePipe.PipeWall[1].CylindricLoad1.heatCapacitor.T +genericAHU.heater.hydraulicModule.pipe6.simplePipe.PipeWall[2].CylindricLoad1.heatCapacitor.T +genericAHU.heater.hydraulicModule.pipe6.simplePipe.PipeWall[3].CylindricLoad1.heatCapacitor.T +genericAHU.heater.hydraulicModule.pipe6.simplePipe.vol[1].dynBal.U +genericAHU.heater.hydraulicModule.pipe6.simplePipe.vol[2].dynBal.U +genericAHU.heater.hydraulicModule.pipe6.simplePipe.vol[3].dynBal.U +genericAHU.heater.hydraulicModule.PT1_a1.y +genericAHU.heater.hydraulicModule.PT1_a2.y +genericAHU.heater.hydraulicModule.PT1_b1.y +genericAHU.heater.hydraulicModule.PT1_b2.y +genericAHU.heater.hydraulicModule.PumpInterface.pump.filter.s[1] +genericAHU.heater.hydraulicModule.PumpInterface.pump.filter.s[2] +genericAHU.heater.hydraulicModule.PumpInterface.pump.vol.dynBal.U +genericAHU.heater.hydraulicModule.senT_a1.T +genericAHU.heater.hydraulicModule.senT_a2.T +genericAHU.heater.hydraulicModule.senT_b1.T +genericAHU.heater.hydraulicModule.senT_b2.T +genericAHU.heater.hydraulicModule.valve.filter.s[1] +genericAHU.heater.hydraulicModule.valve.vol.dynBal.U +genericAHU.heater.port_b1.p +genericAHU.heater.PT1_airIn.y +genericAHU.heater.PT1_airOut.y +genericAHU.heater.senT_airIn.T +genericAHU.heater.senT_airOut.T +genericAHU.humidifier.vol.dynBal.medium.Xi[1] +genericAHU.humidifier.vol.dynBal.U +genericAHU.humidifierRet.vol.dynBal.m +genericAHU.humidifierRet.vol.dynBal.medium.Xi[1] +genericAHU.humidifierRet.vol.dynBal.U +genericAHU.preheater.dynamicHX.heatCapacitor[1].T +genericAHU.preheater.dynamicHX.heatCapacitor[2].T +genericAHU.preheater.dynamicHX.vol1[1].dynBal.medium.Xi[1] +genericAHU.preheater.dynamicHX.vol1[1].dynBal.U +genericAHU.preheater.dynamicHX.vol1[2].dynBal.medium.Xi[1] +genericAHU.preheater.dynamicHX.vol1[2].dynBal.U +genericAHU.preheater.dynamicHX.vol2[1].dynBal.U +genericAHU.preheater.dynamicHX.vol2[2].dynBal.U +genericAHU.preheater.hydraulicModule.junc456.dynBal.U +genericAHU.preheater.hydraulicModule.pipe1.Insulation.CylindricLoad1.heatCapacitor.T +genericAHU.preheater.hydraulicModule.pipe1.simplePipe.PipeWall[1].CylindricLoad1.heatCapacitor.T +genericAHU.preheater.hydraulicModule.pipe1.simplePipe.PipeWall[2].CylindricLoad1.heatCapacitor.T +genericAHU.preheater.hydraulicModule.pipe1.simplePipe.PipeWall[3].CylindricLoad1.heatCapacitor.T +genericAHU.preheater.hydraulicModule.pipe1.simplePipe.vol[1].dynBal.U +genericAHU.preheater.hydraulicModule.pipe1.simplePipe.vol[2].dynBal.U +genericAHU.preheater.hydraulicModule.pipe1.simplePipe.vol[3].dynBal.U +genericAHU.preheater.hydraulicModule.pipe2.Insulation.CylindricLoad1.heatCapacitor.T +genericAHU.preheater.hydraulicModule.pipe2.simplePipe.PipeWall[1].CylindricLoad1.heatCapacitor.T +genericAHU.preheater.hydraulicModule.pipe2.simplePipe.PipeWall[2].CylindricLoad1.heatCapacitor.T +genericAHU.preheater.hydraulicModule.pipe2.simplePipe.PipeWall[3].CylindricLoad1.heatCapacitor.T +genericAHU.preheater.hydraulicModule.pipe2.simplePipe.vol[1].dynBal.U +genericAHU.preheater.hydraulicModule.pipe2.simplePipe.vol[2].dynBal.U +genericAHU.preheater.hydraulicModule.pipe2.simplePipe.vol[3].dynBal.U +genericAHU.preheater.hydraulicModule.pipe3.Insulation.CylindricLoad1.heatCapacitor.T +genericAHU.preheater.hydraulicModule.pipe3.simplePipe.PipeWall[1].CylindricLoad1.heatCapacitor.T +genericAHU.preheater.hydraulicModule.pipe3.simplePipe.PipeWall[2].CylindricLoad1.heatCapacitor.T +genericAHU.preheater.hydraulicModule.pipe3.simplePipe.PipeWall[3].CylindricLoad1.heatCapacitor.T +genericAHU.preheater.hydraulicModule.pipe3.simplePipe.vol[1].dynBal.U +genericAHU.preheater.hydraulicModule.pipe3.simplePipe.vol[2].dynBal.U +genericAHU.preheater.hydraulicModule.pipe3.simplePipe.vol[3].dynBal.U +genericAHU.preheater.hydraulicModule.pipe4.Insulation.CylindricLoad1.heatCapacitor.T +genericAHU.preheater.hydraulicModule.pipe4.simplePipe.PipeWall[1].CylindricLoad1.heatCapacitor.T +genericAHU.preheater.hydraulicModule.pipe4.simplePipe.PipeWall[2].CylindricLoad1.heatCapacitor.T +genericAHU.preheater.hydraulicModule.pipe4.simplePipe.PipeWall[3].CylindricLoad1.heatCapacitor.T +genericAHU.preheater.hydraulicModule.pipe4.simplePipe.vol[1].dynBal.U +genericAHU.preheater.hydraulicModule.pipe4.simplePipe.vol[2].dynBal.U +genericAHU.preheater.hydraulicModule.pipe4.simplePipe.vol[3].dynBal.U +genericAHU.preheater.hydraulicModule.pipe5.Insulation.CylindricLoad1.heatCapacitor.T +genericAHU.preheater.hydraulicModule.pipe5.simplePipe.PipeWall[1].CylindricLoad1.heatCapacitor.T +genericAHU.preheater.hydraulicModule.pipe5.simplePipe.PipeWall[2].CylindricLoad1.heatCapacitor.T +genericAHU.preheater.hydraulicModule.pipe5.simplePipe.PipeWall[3].CylindricLoad1.heatCapacitor.T +genericAHU.preheater.hydraulicModule.pipe5.simplePipe.vol[1].dynBal.U +genericAHU.preheater.hydraulicModule.pipe5.simplePipe.vol[2].dynBal.U +genericAHU.preheater.hydraulicModule.pipe5.simplePipe.vol[3].dynBal.U +genericAHU.preheater.hydraulicModule.pipe6.Insulation.CylindricLoad1.heatCapacitor.T +genericAHU.preheater.hydraulicModule.pipe6.simplePipe.PipeWall[1].CylindricLoad1.heatCapacitor.T +genericAHU.preheater.hydraulicModule.pipe6.simplePipe.PipeWall[2].CylindricLoad1.heatCapacitor.T +genericAHU.preheater.hydraulicModule.pipe6.simplePipe.PipeWall[3].CylindricLoad1.heatCapacitor.T +genericAHU.preheater.hydraulicModule.pipe6.simplePipe.vol[1].dynBal.U +genericAHU.preheater.hydraulicModule.pipe6.simplePipe.vol[2].dynBal.U +genericAHU.preheater.hydraulicModule.pipe6.simplePipe.vol[3].dynBal.U +genericAHU.preheater.hydraulicModule.PT1_a1.y +genericAHU.preheater.hydraulicModule.PT1_a2.y +genericAHU.preheater.hydraulicModule.PT1_b1.y +genericAHU.preheater.hydraulicModule.PT1_b2.y +genericAHU.preheater.hydraulicModule.PumpInterface.pump.filter.s[1] +genericAHU.preheater.hydraulicModule.PumpInterface.pump.filter.s[2] +genericAHU.preheater.hydraulicModule.PumpInterface.pump.vol.dynBal.U +genericAHU.preheater.hydraulicModule.senT_a1.T +genericAHU.preheater.hydraulicModule.senT_a2.T +genericAHU.preheater.hydraulicModule.senT_b1.T +genericAHU.preheater.hydraulicModule.senT_b2.T +genericAHU.preheater.hydraulicModule.valve.filter.s[1] +genericAHU.preheater.hydraulicModule.valve.vol.dynBal.U +genericAHU.preheater.PT1_airIn.y +genericAHU.preheater.PT1_airOut.y +genericAHU.preheater.senT_airIn.T +genericAHU.preheater.senT_airOut.T +genericAHU.PT1_airIn.y +genericAHU.PT1_airIn1.y +genericAHU.PT1_airIn2.y +genericAHU.PT1_airIn3.y +genericAHU.senRelHumSup.phi +genericAHU.senRelHumSup1.phi +genericAHU.senTExh.T +genericAHU.senTOda.T +genericAHU.senTRet.T +genericAHU.senTSup.T +Finished +Finished + = true + + +Declaring variable: Boolean rScript ; + +savelog("AixLib.Systems.ModularAHU.Examples.GenericAHU.translation.log"); = true + + +rCheck = checkModel("AixLib.Systems.ModularAHU.Validation.AHU2_Heater"); +Check of AixLib.Systems.ModularAHU.Validation.AHU2_Heater +The model has the same number of unknowns and equations: 2418 +The model could not be deduced to be symbolically well-posed. +The model has + 2341+max([size(combiTimeTable.columns, 1); size(combiTimeTable.offset, 1)])+ registerModule.hydraulicModule.valve.vol.dynBal.nPorts+registerModule.hydraulicModule.pipe1.plugFlowPipe.vol_b.dynBal.nPorts +registerModule.hydraulicModule.pipe1.plugFlowPipe.vol_a.dynBal.nPorts+ registerModule.hydraulicModule.pipe2.plugFlowPipe.vol_b.dynBal.nPorts+ registerModule.hydraulicModule.pipe2.plugFlowPipe.vol_a.dynBal.nPorts+ registerModule.hydraulicModule.pipe3.plugFlowPipe.vol_b.dynBal.nPorts+ registerModule.hydraulicModule.pipe3.plugFlowPipe.vol_a.dynBal.nPorts+ registerModule.hydraulicModule.pipe4.plugFlowPipe.vol_b.dynBal.nPorts+ registerModule.hydraulicModule.pipe4.plugFlowPipe.vol_a.dynBal.nPorts+ registerModule.hydraulicModule.pipe5.plugFlowPipe.vol_b.dynBal.nPorts+ registerModule.hydraulicModule.pipe5.plugFlowPipe.vol_a.dynBal.nPorts+ registerModule.hydraulicModule.pipe6.plugFlowPipe.vol_b.dynBal.nPorts+ registerModule.hydraulicModule.pipe6.plugFlowPipe.vol_a.dynBal.nPorts+ registerModule.hydraulicModule.junc456.dynBal.nPorts+2*size(registerModule.hydraulicModule.PumpInterface.physics.maxMinTable.columns, 1)+2*registerModule.hydraulicModule.PumpInterface.physics.deMultiplex2.n1+2* registerModule.hydraulicModule.PumpInterface.physics.deMultiplex2.n2+ registerModule.hydraulicModule.PumpInterface.physics.criticalDamping.n+ registerModule.hydraulicModule.PumpInterface.physics.vol.dynBal.nPorts+2* registerModule.dynamicHX.vol1[1].dynBal.nPorts+2*registerModule.dynamicHX.vol1[2].dynBal.nPorts +2*registerModule.dynamicHX.vol1[3].dynBal.nPorts+2*registerModule.dynamicHX.vol1[4].dynBal.nPorts +registerModule.dynamicHX.vol2[1].dynBal.nPorts+registerModule.dynamicHX.vol2[2].dynBal.nPorts +registerModule.dynamicHX.vol2[3].dynBal.nPorts+registerModule.dynamicHX.vol2[4].dynBal.nPorts +scalar unknowns and + 2193+(if boundaryWaterSource.use_Xi_in then 1 else (if boundaryWaterSource.use_X_in then 0 else 1))+(if not boundaryWaterSource.use_p_in then 1 else 0)+2* boundaryWaterSource.nPorts+(if not boundaryWaterSource.use_T_in then 1 else 0) +(if boundaryWaterSink.use_Xi_in then 1 else (if boundaryWaterSink.use_X_in then 0 else 1))+(if not boundaryWaterSink.use_p_in then 1 else 0)+2* boundaryWaterSink.nPorts+(if not boundaryWaterSink.use_T_in then 1 else 0)+( if boundaryAirSource.use_Xi_in then 2 else (if boundaryAirSource.use_X_in then 1 else 3))+3*boundaryAirSource.nPorts+(if not boundaryAirSource.use_m_flow_in then 1 else 0)+(if not boundaryAirSource.use_T_in then 1 else 0)+(if boundaryAirSink.use_Xi_in then 2 else (if boundaryAirSink.use_X_in then 1 else 3))+3*boundaryAirSink.nPorts+(if not boundaryAirSink.use_p_in then 1 else 0)+(if not boundaryAirSink.use_T_in then 1 else 0)+max([size( combiTimeTable.columns, 1); size(combiTimeTable.offset, 1)])+2*size( registerModule.hydraulicModule.PumpInterface.physics.maxMinTable.columns, 1)+ registerModule.hydraulicModule.PumpInterface.physics.deMultiplex2.n1+ registerModule.hydraulicModule.PumpInterface.physics.deMultiplex2.n2+ registerModule.hydraulicModule.PumpInterface.physics.criticalDamping.n+(if not registerModule.hydraulicModule.pipe1.plugFlowPipe.vol_b.dynBal.use_mWat_flow then 1 else 0)+3*registerModule.hydraulicModule.pipe1.plugFlowPipe.vol_b.dynBal.nPorts +(if not registerModule.hydraulicModule.pipe1.plugFlowPipe.vol_a.dynBal.use_mWat_flow then 1 else 0)+3*registerModule.hydraulicModule.pipe1.plugFlowPipe.vol_a.dynBal.nPorts +(if not registerModule.hydraulicModule.pipe2.plugFlowPipe.vol_b.dynBal.use_mWat_flow then 1 else 0)+3*registerModule.hydraulicModule.pipe2.plugFlowPipe.vol_b.dynBal.nPorts +(if not registerModule.hydraulicModule.pipe2.plugFlowPipe.vol_a.dynBal.use_mWat_flow then 1 else 0)+3*registerModule.hydraulicModule.pipe2.plugFlowPipe.vol_a.dynBal.nPorts +(if not registerModule.hydraulicModule.pipe3.plugFlowPipe.vol_b.dynBal.use_mWat_flow then 1 else 0)+3*registerModule.hydraulicModule.pipe3.plugFlowPipe.vol_b.dynBal.nPorts +(if not registerModule.hydraulicModule.pipe3.plugFlowPipe.vol_a.dynBal.use_mWat_flow then 1 else 0)+3*registerModule.hydraulicModule.pipe3.plugFlowPipe.vol_a.dynBal.nPorts +(if not registerModule.hydraulicModule.pipe4.plugFlowPipe.vol_b.dynBal.use_mWat_flow then 1 else 0)+3*registerModule.hydraulicModule.pipe4.plugFlowPipe.vol_b.dynBal.nPorts +(if not registerModule.hydraulicModule.pipe4.plugFlowPipe.vol_a.dynBal.use_mWat_flow then 1 else 0)+3*registerModule.hydraulicModule.pipe4.plugFlowPipe.vol_a.dynBal.nPorts +(if not registerModule.hydraulicModule.pipe5.plugFlowPipe.vol_b.dynBal.use_mWat_flow then 1 else 0)+3*registerModule.hydraulicModule.pipe5.plugFlowPipe.vol_b.dynBal.nPorts +(if not registerModule.hydraulicModule.pipe5.plugFlowPipe.vol_a.dynBal.use_mWat_flow then 1 else 0)+3*registerModule.hydraulicModule.pipe5.plugFlowPipe.vol_a.dynBal.nPorts +(if not registerModule.hydraulicModule.pipe6.plugFlowPipe.vol_b.dynBal.use_mWat_flow then 1 else 0)+3*registerModule.hydraulicModule.pipe6.plugFlowPipe.vol_b.dynBal.nPorts +(if not registerModule.hydraulicModule.pipe6.plugFlowPipe.vol_a.dynBal.use_mWat_flow then 1 else 0)+3*registerModule.hydraulicModule.pipe6.plugFlowPipe.vol_a.dynBal.nPorts +(if not registerModule.hydraulicModule.junc456.dynBal.use_mWat_flow then 1 else 0)+3*registerModule.hydraulicModule.junc456.dynBal.nPorts+(if not registerModule.hydraulicModule.PumpInterface.physics.vol.dynBal.use_mWat_flow then 1 else 0)+3*registerModule.hydraulicModule.PumpInterface.physics.vol.dynBal.nPorts +(if not registerModule.dynamicHX.vol1[1].dynBal.use_mWat_flow then 1 else 0) +5*registerModule.dynamicHX.vol1[1].dynBal.nPorts+(if not registerModule.dynamicHX.vol1[2].dynBal.use_mWat_flow then 1 else 0)+5*registerModule.dynamicHX.vol1[2].dynBal.nPorts+(if not registerModule.dynamicHX.vol1[3].dynBal.use_mWat_flow then 1 else 0)+5* registerModule.dynamicHX.vol1[3].dynBal.nPorts+(if not registerModule.dynamicHX.vol1[4].dynBal.use_mWat_flow then 1 else 0)+5*registerModule.dynamicHX.vol1[4].dynBal.nPorts+(if not registerModule.dynamicHX.vol2[1].dynBal.use_mWat_flow then 1 else 0)+3* registerModule.dynamicHX.vol2[1].dynBal.nPorts+(if not registerModule.dynamicHX.vol2[2].dynBal.use_mWat_flow then 1 else 0)+3*registerModule.dynamicHX.vol2[2].dynBal.nPorts+(if not registerModule.dynamicHX.vol2[3].dynBal.use_mWat_flow then 1 else 0)+3* registerModule.dynamicHX.vol2[3].dynBal.nPorts+(if not registerModule.dynamicHX.vol2[4].dynBal.use_mWat_flow then 1 else 0)+3*registerModule.dynamicHX.vol2[4].dynBal.nPorts+(if not registerModule.hydraulicModule.valve.vol.dynBal.use_mWat_flow then 1 else 0)+3 *registerModule.hydraulicModule.valve.vol.dynBal.nPorts +scalar equations. +However, exploiting the given numerical settings of parameters gives the same number of unknowns and equations: + 2418 +Check of AixLib.Systems.ModularAHU.Validation.AHU2_Heater successful. +Declaring variable: Boolean rCheck ; + +Modelica.Utilities.Streams.print(" { \"file\" : \"AixLib/Resources/Scripts/Dymola/Systems/ModularAHU/Validation/AHU2_Heater.mos\",", "AixLib.Systems.ModularAHU.Validation.AHU2_Heater.statistics.log"); +Modelica.Utilities.Streams.print(" \"model\" : \"AixLib.Systems.ModularAHU.Validation.AHU2_Heater\",", "AixLib.Systems.ModularAHU.Validation.AHU2_Heater.statistics.log"); +Modelica.Utilities.Streams.print(" \"check\" : {", "AixLib.Systems.ModularAHU.Validation.AHU2_Heater.statistics.log"); +Modelica.Utilities.Streams.print(" \"command\" : \"checkModel(\\\"AixLib.Systems.ModularAHU.Validation.AHU2_Heater\\\");\",", "AixLib.Systems.ModularAHU.Validation.AHU2_Heater.statistics.log"); +Modelica.Utilities.Streams.print(" \"result\" : " + String(rCheck), "AixLib.Systems.ModularAHU.Validation.AHU2_Heater.statistics.log"); +Modelica.Utilities.Streams.print(" },", "AixLib.Systems.ModularAHU.Validation.AHU2_Heater.statistics.log"); + + +rScript=RunScript("modelica://AixLib/Resources/Scripts/Dymola/Systems/ModularAHU/Validation/AHU2_Heater.mos"); +simulateModel("AixLib.Systems.ModularAHU.Validation.AHU2_Heater", tolerance=1e-6, outputInterval=1, stopTime=4320, resultFile="AixLib.Systems.ModularAHU.Validation.AHU2_Heater"); +Translation of AixLib.Systems.ModularAHU.Validation.AHU2_Heater +The DAE has 2418 scalar unknowns and 2418 scalar equations. + +Statistics + +Original Model + Number of components: 464 + Variables: 6155 + Constants: 125 (125 scalars) + Parameters: 2790 (12497 scalars) + Unknowns: 3240 (2521 scalars) + Differentiated variables: 86 scalars + Equations: 2514 + Nontrivial: 1950 +Translated Model + Constants: 2100 scalars + Free parameters: 5071 scalars + Parameter depending: 5769 scalars + Outputs: 17 scalars + Continuous time states: 62 scalars + Time-varying variables: 627 scalars + Alias variables: 1576 scalars + Number of mixed real/discrete systems of equations: 0 + Sizes of linear systems of equations: {2, 2, 2, 2, 2, 2} + Sizes after manipulation of the linear systems: {0, 0, 0, 0, 0, 0} + Sizes of nonlinear systems of equations: {18, 6, 6, 6, 6, 6, 6} + Sizes after manipulation of the nonlinear systems: {2, 1, 1, 1, 1, 1, 1} + Number of numerical Jacobians: 0 + Initialization problem + Sizes of nonlinear systems of equations: {18, 1} + Sizes after manipulation of the nonlinear systems: {4, 0} + Sizes of simplified homotopy nonlinear systems of equations: {18, 1} + Sizes after manipulation of the simplified homotopy nonlinear systems: {3, 0} + Number of numerical Jacobians: 0 + +Selected continuous time states +Statically selected continuous time states +registerModule.dynamicHX.heatCapacitor[1].T +registerModule.dynamicHX.heatCapacitor[2].T +registerModule.dynamicHX.heatCapacitor[3].T +registerModule.dynamicHX.heatCapacitor[4].T +registerModule.dynamicHX.vol1[1].dynBal.medium.Xi[1] +registerModule.dynamicHX.vol1[1].dynBal.U +registerModule.dynamicHX.vol1[2].dynBal.medium.Xi[1] +registerModule.dynamicHX.vol1[2].dynBal.U +registerModule.dynamicHX.vol1[3].dynBal.medium.Xi[1] +registerModule.dynamicHX.vol1[3].dynBal.U +registerModule.dynamicHX.vol1[4].dynBal.medium.Xi[1] +registerModule.dynamicHX.vol1[4].dynBal.U +registerModule.dynamicHX.vol2[1].dynBal.U +registerModule.dynamicHX.vol2[2].dynBal.U +registerModule.dynamicHX.vol2[3].dynBal.U +registerModule.dynamicHX.vol2[4].dynBal.U +registerModule.hydraulicModule.junc456.dynBal.U +registerModule.hydraulicModule.pipe1.Insulation.CylindricLoad1.heatCapacitor.T +registerModule.hydraulicModule.pipe1.plugFlowPipe.del.x +registerModule.hydraulicModule.pipe1.plugFlowPipe.timDel.x +registerModule.hydraulicModule.pipe1.plugFlowPipe.vol_a.dynBal.U +registerModule.hydraulicModule.pipe1.plugFlowPipe.vol_b.dynBal.U +registerModule.hydraulicModule.pipe2.Insulation.CylindricLoad1.heatCapacitor.T +registerModule.hydraulicModule.pipe2.plugFlowPipe.del.x +registerModule.hydraulicModule.pipe2.plugFlowPipe.timDel.x +registerModule.hydraulicModule.pipe2.plugFlowPipe.vol_a.dynBal.U +registerModule.hydraulicModule.pipe2.plugFlowPipe.vol_b.dynBal.U +registerModule.hydraulicModule.pipe3.Insulation.CylindricLoad1.heatCapacitor.T +registerModule.hydraulicModule.pipe3.plugFlowPipe.del.x +registerModule.hydraulicModule.pipe3.plugFlowPipe.timDel.x +registerModule.hydraulicModule.pipe3.plugFlowPipe.vol_a.dynBal.U +registerModule.hydraulicModule.pipe3.plugFlowPipe.vol_b.dynBal.U +registerModule.hydraulicModule.pipe4.Insulation.CylindricLoad1.heatCapacitor.T +registerModule.hydraulicModule.pipe4.plugFlowPipe.del.x +registerModule.hydraulicModule.pipe4.plugFlowPipe.timDel.x +registerModule.hydraulicModule.pipe4.plugFlowPipe.vol_a.dynBal.U +registerModule.hydraulicModule.pipe4.plugFlowPipe.vol_b.dynBal.U +registerModule.hydraulicModule.pipe5.Insulation.CylindricLoad1.heatCapacitor.T +registerModule.hydraulicModule.pipe5.plugFlowPipe.del.x +registerModule.hydraulicModule.pipe5.plugFlowPipe.timDel.x +registerModule.hydraulicModule.pipe5.plugFlowPipe.vol_a.dynBal.U +registerModule.hydraulicModule.pipe5.plugFlowPipe.vol_b.dynBal.U +registerModule.hydraulicModule.pipe6.Insulation.CylindricLoad1.heatCapacitor.T +registerModule.hydraulicModule.pipe6.plugFlowPipe.del.x +registerModule.hydraulicModule.pipe6.plugFlowPipe.timDel.x +registerModule.hydraulicModule.pipe6.plugFlowPipe.vol_a.dynBal.U +registerModule.hydraulicModule.pipe6.plugFlowPipe.vol_b.dynBal.U +registerModule.hydraulicModule.PT1_a1.y +registerModule.hydraulicModule.PT1_a2.y +registerModule.hydraulicModule.PT1_b1.y +registerModule.hydraulicModule.PT1_b2.y +registerModule.hydraulicModule.PumpInterface.physics.criticalDamping.x[1] +registerModule.hydraulicModule.PumpInterface.physics.criticalDamping.x[2] +registerModule.hydraulicModule.senT_a1.T +registerModule.hydraulicModule.senT_a2.T +registerModule.hydraulicModule.senT_b1.T +registerModule.hydraulicModule.senT_b2.T +registerModule.hydraulicModule.valve.vol.dynBal.U +registerModule.PT1_airIn.y +registerModule.PT1_airOut.y +registerModule.senT_airIn.T +registerModule.senT_airOut.T +Finished +Finished + = true + +Declaring variable: Boolean rScript ; + +savelog("AixLib.Systems.ModularAHU.Validation.AHU2_Heater.translation.log"); = true + + +rCheck = checkModel("AixLib.Systems.HydraulicModules.Example.Throttle"); +Check of AixLib.Systems.HydraulicModules.Example.Throttle +The model has the same number of unknowns and equations: 962 +The model could not be deduced to be symbolically well-posed. +The model has + 944+Throttle.pipe1.simplePipe.vol[1].dynBal.nPorts+Throttle.pipe1.simplePipe.vol[2].dynBal.nPorts +Throttle.pipe1.simplePipe.vol[3].dynBal.nPorts+Throttle.pipe2.simplePipe.vol[1].dynBal.nPorts +Throttle.pipe2.simplePipe.vol[2].dynBal.nPorts+Throttle.pipe2.simplePipe.vol[3].dynBal.nPorts +Throttle.pipe3.simplePipe.vol[1].dynBal.nPorts+Throttle.pipe3.simplePipe.vol[2].dynBal.nPorts +Throttle.pipe3.simplePipe.vol[3].dynBal.nPorts +scalar unknowns and + 889+(if boundary.use_Xi_in then 1 else (if boundary.use_X_in then 0 else 1))+( if not boundary.use_p_in then 1 else 0)+2*boundary.nPorts+(if not boundary.use_T_in then 1 else 0)+(if boundary1.use_Xi_in then 1 else (if boundary1.use_X_in then 0 else 1))+(if not boundary1.use_p_in then 1 else 0)+2 *boundary1.nPorts+(if not boundary1.use_T_in then 1 else 0)+(if not Throttle.pipe1.simplePipe.vol[1].dynBal.use_mWat_flow then 1 else 0)+3* Throttle.pipe1.simplePipe.vol[1].dynBal.nPorts+(if not Throttle.pipe1.simplePipe.vol[2].dynBal.use_mWat_flow then 1 else 0)+3*Throttle.pipe1.simplePipe.vol[2].dynBal.nPorts+(if not Throttle.pipe1.simplePipe.vol[3].dynBal.use_mWat_flow then 1 else 0)+3* Throttle.pipe1.simplePipe.vol[3].dynBal.nPorts+(if not Throttle.pipe2.simplePipe.vol[1].dynBal.use_mWat_flow then 1 else 0)+3*Throttle.pipe2.simplePipe.vol[1].dynBal.nPorts+(if not Throttle.pipe2.simplePipe.vol[2].dynBal.use_mWat_flow then 1 else 0)+3* Throttle.pipe2.simplePipe.vol[2].dynBal.nPorts+(if not Throttle.pipe2.simplePipe.vol[3].dynBal.use_mWat_flow then 1 else 0)+3*Throttle.pipe2.simplePipe.vol[3].dynBal.nPorts+(if not Throttle.pipe3.simplePipe.vol[1].dynBal.use_mWat_flow then 1 else 0)+3* Throttle.pipe3.simplePipe.vol[1].dynBal.nPorts+(if not Throttle.pipe3.simplePipe.vol[2].dynBal.use_mWat_flow then 1 else 0)+3*Throttle.pipe3.simplePipe.vol[2].dynBal.nPorts+(if not Throttle.pipe3.simplePipe.vol[3].dynBal.use_mWat_flow then 1 else 0)+3* Throttle.pipe3.simplePipe.vol[3].dynBal.nPorts +scalar equations. +However, exploiting the given numerical settings of parameters gives the same number of unknowns and equations: + 962 +Check of AixLib.Systems.HydraulicModules.Example.Throttle successful. +Declaring variable: Boolean rCheck ; + +Modelica.Utilities.Streams.print(" { \"file\" : \"AixLib/Resources/Scripts/Dymola/Systems/HydraulicModules/Examples/Throttle.mos\",", "AixLib.Systems.HydraulicModules.Example.Throttle.statistics.log"); +Modelica.Utilities.Streams.print(" \"model\" : \"AixLib.Systems.HydraulicModules.Example.Throttle\",", "AixLib.Systems.HydraulicModules.Example.Throttle.statistics.log"); +Modelica.Utilities.Streams.print(" \"check\" : {", "AixLib.Systems.HydraulicModules.Example.Throttle.statistics.log"); +Modelica.Utilities.Streams.print(" \"command\" : \"checkModel(\\\"AixLib.Systems.HydraulicModules.Example.Throttle\\\");\",", "AixLib.Systems.HydraulicModules.Example.Throttle.statistics.log"); +Modelica.Utilities.Streams.print(" \"result\" : " + String(rCheck), "AixLib.Systems.HydraulicModules.Example.Throttle.statistics.log"); +Modelica.Utilities.Streams.print(" },", "AixLib.Systems.HydraulicModules.Example.Throttle.statistics.log"); + + +rScript=RunScript("modelica://AixLib/Resources/Scripts/Dymola/Systems/HydraulicModules/Examples/Throttle.mos"); +simulateModel("AixLib.Systems.HydraulicModules.Example.Throttle", tolerance=1e-6, stopTime=1000, resultFile="AixLib.Systems.HydraulicModules.Example.Throttle"); +Translation of AixLib.Systems.HydraulicModules.Example.Throttle +The DAE has 962 scalar unknowns and 962 scalar equations. + +Statistics + +Original Model + Number of components: 204 + Variables: 2610 + Constants: 50 (50 scalars) + Parameters: 1264 (1222 scalars) + Unknowns: 1296 (996 scalars) + Differentiated variables: 39 scalars + Equations: 948 + Nontrivial: 749 +Translated Model + Constants: 917 scalars + Free parameters: 69 scalars + Parameter depending: 396 scalars + Outputs: 8 scalars + Continuous time states: 30 scalars + Time-varying variables: 210 scalars + Alias variables: 676 scalars + Number of mixed real/discrete systems of equations: 0 + Sizes of linear systems of equations: {5, 2, 5, 2, 5, 2} + Sizes after manipulation of the linear systems: {0, 0, 0, 0, 0, 0} + Sizes of nonlinear systems of equations: {9} + Sizes after manipulation of the nonlinear systems: {1} + Number of numerical Jacobians: 0 + Initialization problem + Sizes of nonlinear systems of equations: {9, 1} + Sizes after manipulation of the nonlinear systems: {1, 0} + Sizes of simplified homotopy nonlinear systems of equations: {9, 1} + Sizes after manipulation of the simplified homotopy nonlinear systems: {1, 0} + Number of numerical Jacobians: 0 + +Selected continuous time states +Statically selected continuous time states +Throttle.pipe1.Insulation.CylindricLoad1.heatCapacitor.T +Throttle.pipe1.simplePipe.PipeWall[1].CylindricLoad1.heatCapacitor.T +Throttle.pipe1.simplePipe.PipeWall[2].CylindricLoad1.heatCapacitor.T +Throttle.pipe1.simplePipe.PipeWall[3].CylindricLoad1.heatCapacitor.T +Throttle.pipe1.simplePipe.vol[1].dynBal.U +Throttle.pipe1.simplePipe.vol[2].dynBal.U +Throttle.pipe1.simplePipe.vol[3].dynBal.U +Throttle.pipe2.Insulation.CylindricLoad1.heatCapacitor.T +Throttle.pipe2.simplePipe.PipeWall[1].CylindricLoad1.heatCapacitor.T +Throttle.pipe2.simplePipe.PipeWall[2].CylindricLoad1.heatCapacitor.T +Throttle.pipe2.simplePipe.PipeWall[3].CylindricLoad1.heatCapacitor.T +Throttle.pipe2.simplePipe.vol[1].dynBal.U +Throttle.pipe2.simplePipe.vol[2].dynBal.U +Throttle.pipe2.simplePipe.vol[3].dynBal.U +Throttle.pipe3.Insulation.CylindricLoad1.heatCapacitor.T +Throttle.pipe3.simplePipe.PipeWall[1].CylindricLoad1.heatCapacitor.T +Throttle.pipe3.simplePipe.PipeWall[2].CylindricLoad1.heatCapacitor.T +Throttle.pipe3.simplePipe.PipeWall[3].CylindricLoad1.heatCapacitor.T +Throttle.pipe3.simplePipe.vol[1].dynBal.U +Throttle.pipe3.simplePipe.vol[2].dynBal.U +Throttle.pipe3.simplePipe.vol[3].dynBal.U +Throttle.PT1_a1.y +Throttle.PT1_a2.y +Throttle.PT1_b1.y +Throttle.PT1_b2.y +Throttle.senT_a1.T +Throttle.senT_a2.T +Throttle.senT_b1.T +Throttle.senT_b2.T +Throttle.valve.filter.s[1] +Finished +Finished + = true + + +Declaring variable: Boolean rScript ; + +savelog("AixLib.Systems.HydraulicModules.Example.Throttle.translation.log"); = true + + +rCheck = checkModel("AixLib.Systems.HydraulicModules.Example.Injection"); +Check of AixLib.Systems.HydraulicModules.Example.Injection +The model has the same number of unknowns and equations: 3023 +The model could not be deduced to be symbolically well-posed. +The model has + 2955+Injection.valve.vol.dynBal.nPorts+Injection.pipe1.simplePipe.vol[1].dynBal.nPorts +Injection.pipe1.simplePipe.vol[2].dynBal.nPorts+Injection.pipe1.simplePipe.vol[3].dynBal.nPorts +Injection.pipe2.simplePipe.vol[1].dynBal.nPorts+Injection.pipe2.simplePipe.vol[2].dynBal.nPorts +Injection.pipe2.simplePipe.vol[3].dynBal.nPorts+Injection.pipe3.simplePipe.vol[1].dynBal.nPorts +Injection.pipe3.simplePipe.vol[2].dynBal.nPorts+Injection.pipe3.simplePipe.vol[3].dynBal.nPorts +Injection.pipe4.simplePipe.vol[1].dynBal.nPorts+Injection.pipe4.simplePipe.vol[2].dynBal.nPorts +Injection.pipe4.simplePipe.vol[3].dynBal.nPorts+Injection.pipe5.simplePipe.vol[1].dynBal.nPorts +Injection.pipe5.simplePipe.vol[2].dynBal.nPorts+Injection.pipe5.simplePipe.vol[3].dynBal.nPorts +Injection.pipe6.simplePipe.vol[1].dynBal.nPorts+Injection.pipe6.simplePipe.vol[2].dynBal.nPorts +Injection.pipe6.simplePipe.vol[3].dynBal.nPorts+Injection.pipe7.simplePipe.vol[1].dynBal.nPorts +Injection.pipe7.simplePipe.vol[2].dynBal.nPorts+Injection.pipe7.simplePipe.vol[3].dynBal.nPorts +Injection.pipe8.simplePipe.vol[1].dynBal.nPorts+Injection.pipe8.simplePipe.vol[2].dynBal.nPorts +Injection.pipe8.simplePipe.vol[3].dynBal.nPorts+Injection.pipe9.simplePipe.vol[1].dynBal.nPorts +Injection.pipe9.simplePipe.vol[2].dynBal.nPorts+Injection.pipe9.simplePipe.vol[3].dynBal.nPorts +Injection.junc3v6.dynBal.nPorts+Injection.PumpInterface.pump.vol.dynBal.nPorts +Injection.junc15j.dynBal.nPorts+Injection.juncjp6.dynBal.nPorts +scalar unknowns and + 2777+(if boundary.use_Xi_in then 1 else (if boundary.use_X_in then 0 else 1))+( if not boundary.use_p_in then 1 else 0)+2*boundary.nPorts+(if not boundary.use_T_in then 1 else 0)+(if boundary1.use_Xi_in then 1 else (if boundary1.use_X_in then 0 else 1))+(if not boundary1.use_p_in then 1 else 0)+2 *boundary1.nPorts+(if not boundary1.use_T_in then 1 else 0)+(if not Injection.pipe1.simplePipe.vol[1].dynBal.use_mWat_flow then 1 else 0)+3* Injection.pipe1.simplePipe.vol[1].dynBal.nPorts+(if not Injection.pipe1.simplePipe.vol[2].dynBal.use_mWat_flow then 1 else 0)+3*Injection.pipe1.simplePipe.vol[2].dynBal.nPorts+(if not Injection.pipe1.simplePipe.vol[3].dynBal.use_mWat_flow then 1 else 0)+3* Injection.pipe1.simplePipe.vol[3].dynBal.nPorts+(if not Injection.pipe2.simplePipe.vol[1].dynBal.use_mWat_flow then 1 else 0)+3*Injection.pipe2.simplePipe.vol[1].dynBal.nPorts+(if not Injection.pipe2.simplePipe.vol[2].dynBal.use_mWat_flow then 1 else 0)+3* Injection.pipe2.simplePipe.vol[2].dynBal.nPorts+(if not Injection.pipe2.simplePipe.vol[3].dynBal.use_mWat_flow then 1 else 0)+3*Injection.pipe2.simplePipe.vol[3].dynBal.nPorts+(if not Injection.pipe3.simplePipe.vol[1].dynBal.use_mWat_flow then 1 else 0)+3* Injection.pipe3.simplePipe.vol[1].dynBal.nPorts+(if not Injection.pipe3.simplePipe.vol[2].dynBal.use_mWat_flow then 1 else 0)+3*Injection.pipe3.simplePipe.vol[2].dynBal.nPorts+(if not Injection.pipe3.simplePipe.vol[3].dynBal.use_mWat_flow then 1 else 0)+3* Injection.pipe3.simplePipe.vol[3].dynBal.nPorts+(if not Injection.pipe4.simplePipe.vol[1].dynBal.use_mWat_flow then 1 else 0)+3*Injection.pipe4.simplePipe.vol[1].dynBal.nPorts+(if not Injection.pipe4.simplePipe.vol[2].dynBal.use_mWat_flow then 1 else 0)+3* Injection.pipe4.simplePipe.vol[2].dynBal.nPorts+(if not Injection.pipe4.simplePipe.vol[3].dynBal.use_mWat_flow then 1 else 0)+3*Injection.pipe4.simplePipe.vol[3].dynBal.nPorts+(if not Injection.pipe5.simplePipe.vol[1].dynBal.use_mWat_flow then 1 else 0)+3* Injection.pipe5.simplePipe.vol[1].dynBal.nPorts+(if not Injection.pipe5.simplePipe.vol[2].dynBal.use_mWat_flow then 1 else 0)+3*Injection.pipe5.simplePipe.vol[2].dynBal.nPorts+(if not Injection.pipe5.simplePipe.vol[3].dynBal.use_mWat_flow then 1 else 0)+3* Injection.pipe5.simplePipe.vol[3].dynBal.nPorts+(if not Injection.pipe6.simplePipe.vol[1].dynBal.use_mWat_flow then 1 else 0)+3*Injection.pipe6.simplePipe.vol[1].dynBal.nPorts+(if not Injection.pipe6.simplePipe.vol[2].dynBal.use_mWat_flow then 1 else 0)+3* Injection.pipe6.simplePipe.vol[2].dynBal.nPorts+(if not Injection.pipe6.simplePipe.vol[3].dynBal.use_mWat_flow then 1 else 0)+3*Injection.pipe6.simplePipe.vol[3].dynBal.nPorts+(if not Injection.pipe7.simplePipe.vol[1].dynBal.use_mWat_flow then 1 else 0)+3* Injection.pipe7.simplePipe.vol[1].dynBal.nPorts+(if not Injection.pipe7.simplePipe.vol[2].dynBal.use_mWat_flow then 1 else 0)+3*Injection.pipe7.simplePipe.vol[2].dynBal.nPorts+(if not Injection.pipe7.simplePipe.vol[3].dynBal.use_mWat_flow then 1 else 0)+3* Injection.pipe7.simplePipe.vol[3].dynBal.nPorts+(if not Injection.pipe8.simplePipe.vol[1].dynBal.use_mWat_flow then 1 else 0)+3*Injection.pipe8.simplePipe.vol[1].dynBal.nPorts+(if not Injection.pipe8.simplePipe.vol[2].dynBal.use_mWat_flow then 1 else 0)+3* Injection.pipe8.simplePipe.vol[2].dynBal.nPorts+(if not Injection.pipe8.simplePipe.vol[3].dynBal.use_mWat_flow then 1 else 0)+3*Injection.pipe8.simplePipe.vol[3].dynBal.nPorts+(if not Injection.pipe9.simplePipe.vol[1].dynBal.use_mWat_flow then 1 else 0)+3* Injection.pipe9.simplePipe.vol[1].dynBal.nPorts+(if not Injection.pipe9.simplePipe.vol[2].dynBal.use_mWat_flow then 1 else 0)+3*Injection.pipe9.simplePipe.vol[2].dynBal.nPorts+(if not Injection.pipe9.simplePipe.vol[3].dynBal.use_mWat_flow then 1 else 0)+3* Injection.pipe9.simplePipe.vol[3].dynBal.nPorts+(if not Injection.junc3v6.dynBal.use_mWat_flow then 1 else 0)+3*Injection.junc3v6.dynBal.nPorts+(if not Injection.PumpInterface.pump.vol.dynBal.use_mWat_flow then 1 else 0)+3*Injection.PumpInterface.pump.vol.dynBal.nPorts+(if not Injection.junc15j.dynBal.use_mWat_flow then 1 else 0)+3*Injection.junc15j.dynBal.nPorts +(if not Injection.juncjp6.dynBal.use_mWat_flow then 1 else 0)+3* Injection.juncjp6.dynBal.nPorts+(if not Injection.valve.vol.dynBal.use_mWat_flow then 1 else 0)+3*Injection.valve.vol.dynBal.nPorts +scalar equations. +However, exploiting the given numerical settings of parameters gives the same number of unknowns and equations: + 3023 +Check of AixLib.Systems.HydraulicModules.Example.Injection successful. +Declaring variable: Boolean rCheck ; + +Modelica.Utilities.Streams.print(" { \"file\" : \"AixLib/Resources/Scripts/Dymola/Systems/HydraulicModules/Examples/Injection.mos\",", "AixLib.Systems.HydraulicModules.Example.Injection.statistics.log"); +Modelica.Utilities.Streams.print(" \"model\" : \"AixLib.Systems.HydraulicModules.Example.Injection\",", "AixLib.Systems.HydraulicModules.Example.Injection.statistics.log"); +Modelica.Utilities.Streams.print(" \"check\" : {", "AixLib.Systems.HydraulicModules.Example.Injection.statistics.log"); +Modelica.Utilities.Streams.print(" \"command\" : \"checkModel(\\\"AixLib.Systems.HydraulicModules.Example.Injection\\\");\",", "AixLib.Systems.HydraulicModules.Example.Injection.statistics.log"); +Modelica.Utilities.Streams.print(" \"result\" : " + String(rCheck), "AixLib.Systems.HydraulicModules.Example.Injection.statistics.log"); +Modelica.Utilities.Streams.print(" },", "AixLib.Systems.HydraulicModules.Example.Injection.statistics.log"); + + +rScript=RunScript("modelica://AixLib/Resources/Scripts/Dymola/Systems/HydraulicModules/Examples/Injection.mos"); +simulateModel("AixLib.Systems.HydraulicModules.Example.Injection", tolerance=1e-6, stopTime=800, resultFile="AixLib.Systems.HydraulicModules.Example.Injection"); +Translation of AixLib.Systems.HydraulicModules.Example.Injection +The DAE has 3023 scalar unknowns and 3023 scalar equations. + +Statistics + +Original Model + Number of components: 665 + Variables: 8147 + Constants: 161 (161 scalars) + Parameters: 3917 (4056 scalars) + Unknowns: 4069 (3142 scalars) + Differentiated variables: 111 scalars + Equations: 2963 + Nontrivial: 2268 +Translated Model + Constants: 2976 scalars + Free parameters: 199 scalars + Parameter depending: 1398 scalars + Outputs: 13 scalars + Continuous time states: 79 scalars + Time-varying variables: 671 scalars + Alias variables: 2115 scalars + Number of mixed real/discrete systems of equations: 0 + Sizes of linear systems of equations: {5, 2, 5, 2, 5, 2, 5, 2, 5, 2, 5, 2, 5, 2, 5, 2, 5, 2} + Sizes after manipulation of the linear systems: {0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0} + Sizes of nonlinear systems of equations: {27} + Sizes after manipulation of the nonlinear systems: {3} + Number of numerical Jacobians: 0 + Initialization problem + Sizes of nonlinear systems of equations: {27, 1} + Sizes after manipulation of the nonlinear systems: {4, 0} + Sizes of simplified homotopy nonlinear systems of equations: {27, 1} + Sizes after manipulation of the simplified homotopy nonlinear systems: {4, 0} + Number of numerical Jacobians: 0 + +Selected continuous time states +Statically selected continuous time states +Injection.junc3v6.dynBal.U +Injection.junc15j.dynBal.U +Injection.juncjp6.dynBal.U +Injection.pipe1.Insulation.CylindricLoad1.heatCapacitor.T +Injection.pipe1.simplePipe.PipeWall[1].CylindricLoad1.heatCapacitor.T +Injection.pipe1.simplePipe.PipeWall[2].CylindricLoad1.heatCapacitor.T +Injection.pipe1.simplePipe.PipeWall[3].CylindricLoad1.heatCapacitor.T +Injection.pipe1.simplePipe.vol[1].dynBal.U +Injection.pipe1.simplePipe.vol[2].dynBal.U +Injection.pipe1.simplePipe.vol[3].dynBal.U +Injection.pipe2.Insulation.CylindricLoad1.heatCapacitor.T +Injection.pipe2.simplePipe.PipeWall[1].CylindricLoad1.heatCapacitor.T +Injection.pipe2.simplePipe.PipeWall[2].CylindricLoad1.heatCapacitor.T +Injection.pipe2.simplePipe.PipeWall[3].CylindricLoad1.heatCapacitor.T +Injection.pipe2.simplePipe.vol[1].dynBal.U +Injection.pipe2.simplePipe.vol[2].dynBal.U +Injection.pipe2.simplePipe.vol[3].dynBal.U +Injection.pipe3.Insulation.CylindricLoad1.heatCapacitor.T +Injection.pipe3.simplePipe.PipeWall[1].CylindricLoad1.heatCapacitor.T +Injection.pipe3.simplePipe.PipeWall[2].CylindricLoad1.heatCapacitor.T +Injection.pipe3.simplePipe.PipeWall[3].CylindricLoad1.heatCapacitor.T +Injection.pipe3.simplePipe.vol[1].dynBal.U +Injection.pipe3.simplePipe.vol[2].dynBal.U +Injection.pipe3.simplePipe.vol[3].dynBal.U +Injection.pipe4.Insulation.CylindricLoad1.heatCapacitor.T +Injection.pipe4.simplePipe.PipeWall[1].CylindricLoad1.heatCapacitor.T +Injection.pipe4.simplePipe.PipeWall[2].CylindricLoad1.heatCapacitor.T +Injection.pipe4.simplePipe.PipeWall[3].CylindricLoad1.heatCapacitor.T +Injection.pipe4.simplePipe.vol[1].dynBal.U +Injection.pipe4.simplePipe.vol[2].dynBal.U +Injection.pipe4.simplePipe.vol[3].dynBal.U +Injection.pipe5.Insulation.CylindricLoad1.heatCapacitor.T +Injection.pipe5.simplePipe.PipeWall[1].CylindricLoad1.heatCapacitor.T +Injection.pipe5.simplePipe.PipeWall[2].CylindricLoad1.heatCapacitor.T +Injection.pipe5.simplePipe.PipeWall[3].CylindricLoad1.heatCapacitor.T +Injection.pipe5.simplePipe.vol[1].dynBal.U +Injection.pipe5.simplePipe.vol[2].dynBal.U +Injection.pipe5.simplePipe.vol[3].dynBal.U +Injection.pipe6.Insulation.CylindricLoad1.heatCapacitor.T +Injection.pipe6.simplePipe.PipeWall[1].CylindricLoad1.heatCapacitor.T +Injection.pipe6.simplePipe.PipeWall[2].CylindricLoad1.heatCapacitor.T +Injection.pipe6.simplePipe.PipeWall[3].CylindricLoad1.heatCapacitor.T +Injection.pipe6.simplePipe.vol[1].dynBal.U +Injection.pipe6.simplePipe.vol[2].dynBal.U +Injection.pipe6.simplePipe.vol[3].dynBal.U +Injection.pipe7.Insulation.CylindricLoad1.heatCapacitor.T +Injection.pipe7.simplePipe.PipeWall[1].CylindricLoad1.heatCapacitor.T +Injection.pipe7.simplePipe.PipeWall[2].CylindricLoad1.heatCapacitor.T +Injection.pipe7.simplePipe.PipeWall[3].CylindricLoad1.heatCapacitor.T +Injection.pipe7.simplePipe.vol[1].dynBal.U +Injection.pipe7.simplePipe.vol[2].dynBal.U +Injection.pipe7.simplePipe.vol[3].dynBal.U +Injection.pipe8.Insulation.CylindricLoad1.heatCapacitor.T +Injection.pipe8.simplePipe.PipeWall[1].CylindricLoad1.heatCapacitor.T +Injection.pipe8.simplePipe.PipeWall[2].CylindricLoad1.heatCapacitor.T +Injection.pipe8.simplePipe.PipeWall[3].CylindricLoad1.heatCapacitor.T +Injection.pipe8.simplePipe.vol[1].dynBal.U +Injection.pipe8.simplePipe.vol[2].dynBal.U +Injection.pipe8.simplePipe.vol[3].dynBal.U +Injection.pipe9.Insulation.CylindricLoad1.heatCapacitor.T +Injection.pipe9.simplePipe.PipeWall[1].CylindricLoad1.heatCapacitor.T +Injection.pipe9.simplePipe.PipeWall[2].CylindricLoad1.heatCapacitor.T +Injection.pipe9.simplePipe.PipeWall[3].CylindricLoad1.heatCapacitor.T +Injection.pipe9.simplePipe.vol[1].dynBal.U +Injection.pipe9.simplePipe.vol[2].dynBal.U +Injection.pipe9.simplePipe.vol[3].dynBal.U +Injection.PT1_a1.y +Injection.PT1_a2.y +Injection.PT1_b1.y +Injection.PT1_b2.y +Injection.PumpInterface.pump.filter.s[1] +Injection.PumpInterface.pump.filter.s[2] +Injection.PumpInterface.pump.vol.dynBal.U +Injection.senT_a1.T +Injection.senT_a2.T +Injection.senT_b1.T +Injection.senT_b2.T +Injection.valve.filter.s[1] +Injection.valve.vol.dynBal.U +Finished +Finished + = true + +Declaring variable: Boolean rScript ; + +savelog("AixLib.Systems.HydraulicModules.Example.Injection.translation.log"); = true + + +rCheck = checkModel("AixLib.Systems.ModularAHU.Examples.DemandControlledAHU"); +Check of AixLib.Systems.ModularAHU.Examples.DemandControlledAHU +The model has the same number of unknowns and equations: 11521 +The model could not be deduced to be symbolically well-posed. +The model has + 11048+genericAHU.preheater.hydraulicModule.valve.vol.dynBal.nPorts+ genericAHU.preheater.hydraulicModule.pipe1.plugFlowPipe.vol_b.dynBal.nPorts+ genericAHU.preheater.hydraulicModule.pipe1.plugFlowPipe.vol_a.dynBal.nPorts+ genericAHU.preheater.hydraulicModule.pipe2.plugFlowPipe.vol_b.dynBal.nPorts+ genericAHU.preheater.hydraulicModule.pipe2.plugFlowPipe.vol_a.dynBal.nPorts+ genericAHU.preheater.hydraulicModule.pipe3.plugFlowPipe.vol_b.dynBal.nPorts+ genericAHU.preheater.hydraulicModule.pipe3.plugFlowPipe.vol_a.dynBal.nPorts+ genericAHU.preheater.hydraulicModule.pipe4.plugFlowPipe.vol_b.dynBal.nPorts+ genericAHU.preheater.hydraulicModule.pipe4.plugFlowPipe.vol_a.dynBal.nPorts+ genericAHU.preheater.hydraulicModule.pipe5.plugFlowPipe.vol_b.dynBal.nPorts+ genericAHU.preheater.hydraulicModule.pipe5.plugFlowPipe.vol_a.dynBal.nPorts+ genericAHU.preheater.hydraulicModule.pipe6.plugFlowPipe.vol_b.dynBal.nPorts+ genericAHU.preheater.hydraulicModule.pipe6.plugFlowPipe.vol_a.dynBal.nPorts+ genericAHU.preheater.hydraulicModule.junc456.dynBal.nPorts+2*size( genericAHU.preheater.hydraulicModule.PumpInterface.physics.maxMinTable.columns, 1)+2*genericAHU.preheater.hydraulicModule.PumpInterface.physics.deMultiplex2.n1 +2*genericAHU.preheater.hydraulicModule.PumpInterface.physics.deMultiplex2.n2+ genericAHU.preheater.hydraulicModule.PumpInterface.physics.criticalDamping.n+ genericAHU.preheater.hydraulicModule.PumpInterface.physics.vol.dynBal.nPorts+3 *genericAHU.preheater.dynamicHX.vol1[1].dynBal.nPorts+3*genericAHU.preheater.dynamicHX.vol1[2].dynBal.nPorts +3*genericAHU.preheater.dynamicHX.vol1[3].dynBal.nPorts+3*genericAHU.preheater.dynamicHX.vol1[4].dynBal.nPorts +3*genericAHU.preheater.dynamicHX.vol1[5].dynBal.nPorts+genericAHU.preheater.dynamicHX.vol2[1].dynBal.nPorts +genericAHU.preheater.dynamicHX.vol2[2].dynBal.nPorts+genericAHU.preheater.dynamicHX.vol2[3].dynBal.nPorts +genericAHU.preheater.dynamicHX.vol2[4].dynBal.nPorts+genericAHU.preheater.dynamicHX.vol2[5].dynBal.nPorts +genericAHU.cooler.hydraulicModule.valve.vol.dynBal.nPorts+genericAHU.cooler.hydraulicModule.pipe1.plugFlowPipe.vol_b.dynBal.nPorts +genericAHU.cooler.hydraulicModule.pipe1.plugFlowPipe.vol_a.dynBal.nPorts+ genericAHU.cooler.hydraulicModule.pipe2.plugFlowPipe.vol_b.dynBal.nPorts+ genericAHU.cooler.hydraulicModule.pipe2.plugFlowPipe.vol_a.dynBal.nPorts+ genericAHU.cooler.hydraulicModule.pipe3.plugFlowPipe.vol_b.dynBal.nPorts+ genericAHU.cooler.hydraulicModule.pipe3.plugFlowPipe.vol_a.dynBal.nPorts+ genericAHU.cooler.hydraulicModule.pipe4.plugFlowPipe.vol_b.dynBal.nPorts+ genericAHU.cooler.hydraulicModule.pipe4.plugFlowPipe.vol_a.dynBal.nPorts+ genericAHU.cooler.hydraulicModule.pipe5.plugFlowPipe.vol_b.dynBal.nPorts+ genericAHU.cooler.hydraulicModule.pipe5.plugFlowPipe.vol_a.dynBal.nPorts+ genericAHU.cooler.hydraulicModule.pipe6.plugFlowPipe.vol_b.dynBal.nPorts+ genericAHU.cooler.hydraulicModule.pipe6.plugFlowPipe.vol_a.dynBal.nPorts+ genericAHU.cooler.hydraulicModule.junc456.dynBal.nPorts+2*size( genericAHU.cooler.hydraulicModule.PumpInterface.physics.maxMinTable.columns, 1) +2*genericAHU.cooler.hydraulicModule.PumpInterface.physics.deMultiplex2.n1+2* genericAHU.cooler.hydraulicModule.PumpInterface.physics.deMultiplex2.n2+ genericAHU.cooler.hydraulicModule.PumpInterface.physics.criticalDamping.n+ genericAHU.cooler.hydraulicModule.PumpInterface.physics.vol.dynBal.nPorts+3* genericAHU.cooler.dynamicHX.vol1[1].dynBal.nPorts+3*genericAHU.cooler.dynamicHX.vol1[2].dynBal.nPorts +3*genericAHU.cooler.dynamicHX.vol1[3].dynBal.nPorts+3*genericAHU.cooler.dynamicHX.vol1[4].dynBal.nPorts +genericAHU.cooler.dynamicHX.vol2[1].dynBal.nPorts+genericAHU.cooler.dynamicHX.vol2[2].dynBal.nPorts +genericAHU.cooler.dynamicHX.vol2[3].dynBal.nPorts+genericAHU.cooler.dynamicHX.vol2[4].dynBal.nPorts +genericAHU.heater.hydraulicModule.valve.vol.dynBal.nPorts+genericAHU.heater.hydraulicModule.pipe1.plugFlowPipe.vol_b.dynBal.nPorts +genericAHU.heater.hydraulicModule.pipe1.plugFlowPipe.vol_a.dynBal.nPorts+ genericAHU.heater.hydraulicModule.pipe2.plugFlowPipe.vol_b.dynBal.nPorts+ genericAHU.heater.hydraulicModule.pipe2.plugFlowPipe.vol_a.dynBal.nPorts+ genericAHU.heater.hydraulicModule.pipe3.plugFlowPipe.vol_b.dynBal.nPorts+ genericAHU.heater.hydraulicModule.pipe3.plugFlowPipe.vol_a.dynBal.nPorts+ genericAHU.heater.hydraulicModule.pipe4.plugFlowPipe.vol_b.dynBal.nPorts+ genericAHU.heater.hydraulicModule.pipe4.plugFlowPipe.vol_a.dynBal.nPorts+ genericAHU.heater.hydraulicModule.pipe5.plugFlowPipe.vol_b.dynBal.nPorts+ genericAHU.heater.hydraulicModule.pipe5.plugFlowPipe.vol_a.dynBal.nPorts+ genericAHU.heater.hydraulicModule.pipe6.plugFlowPipe.vol_b.dynBal.nPorts+ genericAHU.heater.hydraulicModule.pipe6.plugFlowPipe.vol_a.dynBal.nPorts+ genericAHU.heater.hydraulicModule.junc456.dynBal.nPorts+2*size( genericAHU.heater.hydraulicModule.PumpInterface.physics.maxMinTable.columns, 1) +2*genericAHU.heater.hydraulicModule.PumpInterface.physics.deMultiplex2.n1+2* genericAHU.heater.hydraulicModule.PumpInterface.physics.deMultiplex2.n2+ genericAHU.heater.hydraulicModule.PumpInterface.physics.criticalDamping.n+ genericAHU.heater.hydraulicModule.PumpInterface.physics.vol.dynBal.nPorts+3* genericAHU.heater.dynamicHX.vol1[1].dynBal.nPorts+3*genericAHU.heater.dynamicHX.vol1[2].dynBal.nPorts +3*genericAHU.heater.dynamicHX.vol1[3].dynBal.nPorts+3*genericAHU.heater.dynamicHX.vol1[4].dynBal.nPorts +genericAHU.heater.dynamicHX.vol2[1].dynBal.nPorts+genericAHU.heater.dynamicHX.vol2[2].dynBal.nPorts +genericAHU.heater.dynamicHX.vol2[3].dynBal.nPorts+genericAHU.heater.dynamicHX.vol2[4].dynBal.nPorts +3*genericAHU.dynamicHX.vol1[1].dynBal.nPorts+3*genericAHU.dynamicHX.vol1[2].dynBal.nPorts +3*genericAHU.dynamicHX.vol2[1].dynBal.nPorts+3*genericAHU.dynamicHX.vol2[2].dynBal.nPorts +3*genericAHU.fanSup.vol.dynBal.nPorts+3*genericAHU.fanRet.vol.dynBal.nPorts+3 *genericAHU.humidifier.vol.dynBal.nPorts+29*thermalZone.zoneParam.nOrientations +3*thermalZone.ROM.volMoiAir.dynBal.nPorts+thermalZone.humanTotHeaDependent.productHeatOutput.nu +thermalZone.humanTotHeaDependent.productMoistureOutput.nu+thermalZone.machinesSenHea.productHeatOutput.nu +thermalZone.lights.productHeatOutput.nu+thermalZone.ventCont.optimalTemp.nin+ thermalZone.ventCont.optimalTemp.nout+thermalZone.ventCont.dEMA.nout+ thermalZone.ventCont.dEMA.ExpAVG.n+thermalZone.ventCont.dEMA.ExpAVG1.n+ thermalZone.SumQLat2_flow.nu+max([size(internalGains.columns, 1); size( internalGains.offset, 1)]) +scalar unknowns and + 10574+size(genericAHU.preheater.hydraulicModule.PumpInterface.physics.maxMinTable.columns, 1)+genericAHU.preheater.hydraulicModule.PumpInterface.physics.deMultiplex2.n1 +genericAHU.preheater.hydraulicModule.PumpInterface.physics.deMultiplex2.n2+ genericAHU.preheater.hydraulicModule.PumpInterface.physics.criticalDamping.n-1 +size(genericAHU.cooler.hydraulicModule.PumpInterface.physics.maxMinTable.columns, 1)+genericAHU.cooler.hydraulicModule.PumpInterface.physics.deMultiplex2.n1+ genericAHU.cooler.hydraulicModule.PumpInterface.physics.deMultiplex2.n2+ genericAHU.cooler.hydraulicModule.PumpInterface.physics.criticalDamping.n-1+ size(genericAHU.heater.hydraulicModule.PumpInterface.physics.maxMinTable.columns, 1)+genericAHU.heater.hydraulicModule.PumpInterface.physics.deMultiplex2.n1+ genericAHU.heater.hydraulicModule.PumpInterface.physics.deMultiplex2.n2+ genericAHU.heater.hydraulicModule.PumpInterface.physics.criticalDamping.n-1+( if not genericAHU.humidifier.steamHumidifier then 1 else 0)+(if SourcePreheater.use_Xi_in then 1 else (if SourcePreheater.use_X_in then 0 else 1))+(if not SourcePreheater.use_p_in then 1 else 0)+SourcePreheater.nPorts +(if not SourcePreheater.use_T_in then 1 else 0)+SourcePreheater.nPorts+(if SinkPreheater.use_Xi_in then 1 else (if SinkPreheater.use_X_in then 0 else 1)) +(if not SinkPreheater.use_p_in then 1 else 0)+SinkPreheater.nPorts+(if not SinkPreheater.use_T_in then 1 else 0)+SinkPreheater.nPorts+(if SourceCooler.use_Xi_in then 1 else (if SourceCooler.use_X_in then 0 else 1))+( if not SourceCooler.use_p_in then 1 else 0)+SourceCooler.nPorts+(if not SourceCooler.use_T_in then 1 else 0)+SourceCooler.nPorts+(if SinkCooler.use_Xi_in then 1 else (if SinkCooler.use_X_in then 0 else 1))+(if not SinkCooler.use_p_in then 1 else 0)+SinkCooler.nPorts+(if not SinkCooler.use_T_in then 1 else 0)+ SinkCooler.nPorts+(if SourceHeater.use_Xi_in then 1 else (if SourceHeater.use_X_in then 0 else 1))+(if not SourceHeater.use_p_in then 1 else 0)+ SourceHeater.nPorts+(if not SourceHeater.use_T_in then 1 else 0)+ SourceHeater.nPorts+(if SinkHeater.use_Xi_in then 1 else (if SinkHeater.use_X_in then 0 else 1))+(if not SinkHeater.use_p_in then 1 else 0)+SinkHeater.nPorts +(if not SinkHeater.use_T_in then 1 else 0)+SinkHeater.nPorts+(if not out.x_pTphi.use_p_in then 1 else 0)+(if not out.use_C_in then 1 else 0)+3* out.nPorts+(if boundaryExhaustAir.use_Xi_in then 2 else (if boundaryExhaustAir.use_X_in then 1 else 3))+(if not boundaryExhaustAir.use_C_in then 1 else 0)+2* boundaryExhaustAir.nPorts+(if not boundaryExhaustAir.use_p_in then 1 else 0)+ boundaryExhaustAir.nPorts+(if not boundaryExhaustAir.use_T_in then 1 else 0)+ boundaryExhaustAir.nPorts+(if weaDat.pAtmSou == AixLib.BoundaryConditions.Types.DataSource. Parameter then 1 else 0)+(if weaDat.TDewPoiSou == AixLib.BoundaryConditions.Types.DataSource. Parameter then 1 else 0)+(if weaDat.TDryBulSou == AixLib.BoundaryConditions.Types.DataSource. Parameter then 1 else 0)+(if weaDat.TBlaSkySou == AixLib.BoundaryConditions.Types.DataSource. Parameter then 1 else 0)+(if weaDat.relHumSou == AixLib.BoundaryConditions.Types.DataSource. Parameter then 1 else 0)+(if weaDat.opaSkyCovSou == AixLib.BoundaryConditions.Types.DataSource. Parameter then 1 else 0)+(if weaDat.ceiHeiSou == AixLib.BoundaryConditions.Types.DataSource. Parameter then 1 else 0)+(if weaDat.totSkyCovSou == AixLib.BoundaryConditions.Types.DataSource. Parameter then 1 else 0)+(if weaDat.winSpeSou == AixLib.BoundaryConditions.Types.DataSource. Parameter then 1 else 0)+(if weaDat.winDirSou == AixLib.BoundaryConditions.Types.DataSource. Parameter then 1 else 0)+(if weaDat.HInfHorSou == AixLib.BoundaryConditions.Types.DataSource. Parameter then 1 else 0)+(if weaDat.HSou == AixLib.BoundaryConditions.Types.RadiationDataSource. Input_HDirNor_HDifHor then 2 else 1)+(if weaDat.HSou == AixLib.BoundaryConditions.Types.RadiationDataSource. Input_HDirNor_HGloHor then 2 else 1)+(if weaDat.HSou == AixLib.BoundaryConditions.Types.RadiationDataSource. Input_HGloHor_HDifHor then 2 else 1)+max([size(internalGains.columns, 1); size (internalGains.offset, 1)])+(if not genericAHU.preheater.hydraulicModule.pipe1.plugFlowPipe.vol_b.dynBal.use_mWat_flow then 1 else 0)+genericAHU.preheater.hydraulicModule.pipe1.plugFlowPipe.vol_b.dynBal.nPorts +2*genericAHU.preheater.hydraulicModule.pipe1.plugFlowPipe.vol_b.dynBal.nPorts +(if not genericAHU.preheater.hydraulicModule.pipe1.plugFlowPipe.vol_a.dynBal.use_mWat_flow then 1 else 0)+genericAHU.preheater.hydraulicModule.pipe1.plugFlowPipe.vol_a.dynBal.nPorts +2*genericAHU.preheater.hydraulicModule.pipe1.plugFlowPipe.vol_a.dynBal.nPorts +(if not genericAHU.preheater.hydraulicModule.pipe2.plugFlowPipe.vol_b.dynBal.use_mWat_flow then 1 else 0)+genericAHU.preheater.hydraulicModule.pipe2.plugFlowPipe.vol_b.dynBal.nPorts +2*genericAHU.preheater.hydraulicModule.pipe2.plugFlowPipe.vol_b.dynBal.nPorts +(if not genericAHU.preheater.hydraulicModule.pipe2.plugFlowPipe.vol_a.dynBal.use_mWat_flow then 1 else 0)+genericAHU.preheater.hydraulicModule.pipe2.plugFlowPipe.vol_a.dynBal.nPorts +2*genericAHU.preheater.hydraulicModule.pipe2.plugFlowPipe.vol_a.dynBal.nPorts +(if not genericAHU.preheater.hydraulicModule.pipe3.plugFlowPipe.vol_b.dynBal.use_mWat_flow then 1 else 0)+genericAHU.preheater.hydraulicModule.pipe3.plugFlowPipe.vol_b.dynBal.nPorts +2*genericAHU.preheater.hydraulicModule.pipe3.plugFlowPipe.vol_b.dynBal.nPorts +(if not genericAHU.preheater.hydraulicModule.pipe3.plugFlowPipe.vol_a.dynBal.use_mWat_flow then 1 else 0)+genericAHU.preheater.hydraulicModule.pipe3.plugFlowPipe.vol_a.dynBal.nPorts +2*genericAHU.preheater.hydraulicModule.pipe3.plugFlowPipe.vol_a.dynBal.nPorts +(if not genericAHU.preheater.hydraulicModule.pipe4.plugFlowPipe.vol_b.dynBal.use_mWat_flow then 1 else 0)+genericAHU.preheater.hydraulicModule.pipe4.plugFlowPipe.vol_b.dynBal.nPorts +2*genericAHU.preheater.hydraulicModule.pipe4.plugFlowPipe.vol_b.dynBal.nPorts +(if not genericAHU.preheater.hydraulicModule.pipe4.plugFlowPipe.vol_a.dynBal.use_mWat_flow then 1 else 0)+genericAHU.preheater.hydraulicModule.pipe4.plugFlowPipe.vol_a.dynBal.nPorts +2*genericAHU.preheater.hydraulicModule.pipe4.plugFlowPipe.vol_a.dynBal.nPorts +(if not genericAHU.preheater.hydraulicModule.pipe5.plugFlowPipe.vol_b.dynBal.use_mWat_flow then 1 else 0)+genericAHU.preheater.hydraulicModule.pipe5.plugFlowPipe.vol_b.dynBal.nPorts +2*genericAHU.preheater.hydraulicModule.pipe5.plugFlowPipe.vol_b.dynBal.nPorts +(if not genericAHU.preheater.hydraulicModule.pipe5.plugFlowPipe.vol_a.dynBal.use_mWat_flow then 1 else 0)+genericAHU.preheater.hydraulicModule.pipe5.plugFlowPipe.vol_a.dynBal.nPorts +2*genericAHU.preheater.hydraulicModule.pipe5.plugFlowPipe.vol_a.dynBal.nPorts +(if not genericAHU.preheater.hydraulicModule.pipe6.plugFlowPipe.vol_b.dynBal.use_mWat_flow then 1 else 0)+genericAHU.preheater.hydraulicModule.pipe6.plugFlowPipe.vol_b.dynBal.nPorts 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0)+3*genericAHU.preheater.dynamicHX.vol1[1].dynBal.nPorts+4* genericAHU.preheater.dynamicHX.vol1[1].dynBal.nPorts+(if not genericAHU.preheater.dynamicHX.vol1[2].dynBal.use_mWat_flow then 1 else 0)+(if not genericAHU.preheater.dynamicHX.vol1[2].dynBal.use_C_flow then 1 else 0)+3*genericAHU.preheater.dynamicHX.vol1[2].dynBal.nPorts+4* genericAHU.preheater.dynamicHX.vol1[2].dynBal.nPorts+(if not genericAHU.preheater.dynamicHX.vol1[3].dynBal.use_mWat_flow then 1 else 0)+(if not genericAHU.preheater.dynamicHX.vol1[3].dynBal.use_C_flow then 1 else 0)+3*genericAHU.preheater.dynamicHX.vol1[3].dynBal.nPorts+4* genericAHU.preheater.dynamicHX.vol1[3].dynBal.nPorts+(if not genericAHU.preheater.dynamicHX.vol1[4].dynBal.use_mWat_flow then 1 else 0)+(if not genericAHU.preheater.dynamicHX.vol1[4].dynBal.use_C_flow then 1 else 0)+3*genericAHU.preheater.dynamicHX.vol1[4].dynBal.nPorts+4* genericAHU.preheater.dynamicHX.vol1[4].dynBal.nPorts+(if not genericAHU.preheater.dynamicHX.vol1[5].dynBal.use_mWat_flow then 1 else 0)+(if not genericAHU.preheater.dynamicHX.vol1[5].dynBal.use_C_flow then 1 else 0)+3*genericAHU.preheater.dynamicHX.vol1[5].dynBal.nPorts+4* genericAHU.preheater.dynamicHX.vol1[5].dynBal.nPorts+(if not genericAHU.preheater.dynamicHX.vol2[1].dynBal.use_mWat_flow then 1 else 0)+genericAHU.preheater.dynamicHX.vol2[1].dynBal.nPorts+2* genericAHU.preheater.dynamicHX.vol2[1].dynBal.nPorts+(if not genericAHU.preheater.dynamicHX.vol2[2].dynBal.use_mWat_flow then 1 else 0)+genericAHU.preheater.dynamicHX.vol2[2].dynBal.nPorts+2* genericAHU.preheater.dynamicHX.vol2[2].dynBal.nPorts+(if not genericAHU.preheater.dynamicHX.vol2[3].dynBal.use_mWat_flow then 1 else 0)+genericAHU.preheater.dynamicHX.vol2[3].dynBal.nPorts+2* genericAHU.preheater.dynamicHX.vol2[3].dynBal.nPorts+(if not genericAHU.preheater.dynamicHX.vol2[4].dynBal.use_mWat_flow then 1 else 0)+genericAHU.preheater.dynamicHX.vol2[4].dynBal.nPorts+2* genericAHU.preheater.dynamicHX.vol2[4].dynBal.nPorts+(if not genericAHU.preheater.dynamicHX.vol2[5].dynBal.use_mWat_flow then 1 else 0)+genericAHU.preheater.dynamicHX.vol2[5].dynBal.nPorts+2* genericAHU.preheater.dynamicHX.vol2[5].dynBal.nPorts+(if not genericAHU.cooler.hydraulicModule.pipe1.plugFlowPipe.vol_b.dynBal.use_mWat_flow then 1 else 0)+genericAHU.cooler.hydraulicModule.pipe1.plugFlowPipe.vol_b.dynBal.nPorts +2*genericAHU.cooler.hydraulicModule.pipe1.plugFlowPipe.vol_b.dynBal.nPorts+( if not genericAHU.cooler.hydraulicModule.pipe1.plugFlowPipe.vol_a.dynBal.use_mWat_flow then 1 else 0)+genericAHU.cooler.hydraulicModule.pipe1.plugFlowPipe.vol_a.dynBal.nPorts +2*genericAHU.cooler.hydraulicModule.pipe1.plugFlowPipe.vol_a.dynBal.nPorts+( if not genericAHU.cooler.hydraulicModule.pipe2.plugFlowPipe.vol_b.dynBal.use_mWat_flow then 1 else 0)+genericAHU.cooler.hydraulicModule.pipe2.plugFlowPipe.vol_b.dynBal.nPorts +2*genericAHU.cooler.hydraulicModule.pipe2.plugFlowPipe.vol_b.dynBal.nPorts+( if not genericAHU.cooler.hydraulicModule.pipe2.plugFlowPipe.vol_a.dynBal.use_mWat_flow then 1 else 0)+genericAHU.cooler.hydraulicModule.pipe2.plugFlowPipe.vol_a.dynBal.nPorts +2*genericAHU.cooler.hydraulicModule.pipe2.plugFlowPipe.vol_a.dynBal.nPorts+( if not genericAHU.cooler.hydraulicModule.pipe3.plugFlowPipe.vol_b.dynBal.use_mWat_flow then 1 else 0)+genericAHU.cooler.hydraulicModule.pipe3.plugFlowPipe.vol_b.dynBal.nPorts +2*genericAHU.cooler.hydraulicModule.pipe3.plugFlowPipe.vol_b.dynBal.nPorts+( if not genericAHU.cooler.hydraulicModule.pipe3.plugFlowPipe.vol_a.dynBal.use_mWat_flow then 1 else 0)+genericAHU.cooler.hydraulicModule.pipe3.plugFlowPipe.vol_a.dynBal.nPorts +2*genericAHU.cooler.hydraulicModule.pipe3.plugFlowPipe.vol_a.dynBal.nPorts+( if not genericAHU.cooler.hydraulicModule.pipe4.plugFlowPipe.vol_b.dynBal.use_mWat_flow then 1 else 0)+genericAHU.cooler.hydraulicModule.pipe4.plugFlowPipe.vol_b.dynBal.nPorts +2*genericAHU.cooler.hydraulicModule.pipe4.plugFlowPipe.vol_b.dynBal.nPorts+( if not genericAHU.cooler.hydraulicModule.pipe4.plugFlowPipe.vol_a.dynBal.use_mWat_flow then 1 else 0)+genericAHU.cooler.hydraulicModule.pipe4.plugFlowPipe.vol_a.dynBal.nPorts +2*genericAHU.cooler.hydraulicModule.pipe4.plugFlowPipe.vol_a.dynBal.nPorts+( if not genericAHU.cooler.hydraulicModule.pipe5.plugFlowPipe.vol_b.dynBal.use_mWat_flow then 1 else 0)+genericAHU.cooler.hydraulicModule.pipe5.plugFlowPipe.vol_b.dynBal.nPorts +2*genericAHU.cooler.hydraulicModule.pipe5.plugFlowPipe.vol_b.dynBal.nPorts+( if not genericAHU.cooler.hydraulicModule.pipe5.plugFlowPipe.vol_a.dynBal.use_mWat_flow then 1 else 0)+genericAHU.cooler.hydraulicModule.pipe5.plugFlowPipe.vol_a.dynBal.nPorts +2*genericAHU.cooler.hydraulicModule.pipe5.plugFlowPipe.vol_a.dynBal.nPorts+( if not genericAHU.cooler.hydraulicModule.pipe6.plugFlowPipe.vol_b.dynBal.use_mWat_flow then 1 else 0)+genericAHU.cooler.hydraulicModule.pipe6.plugFlowPipe.vol_b.dynBal.nPorts +2*genericAHU.cooler.hydraulicModule.pipe6.plugFlowPipe.vol_b.dynBal.nPorts+( if not genericAHU.cooler.hydraulicModule.pipe6.plugFlowPipe.vol_a.dynBal.use_mWat_flow then 1 else 0)+genericAHU.cooler.hydraulicModule.pipe6.plugFlowPipe.vol_a.dynBal.nPorts +2*genericAHU.cooler.hydraulicModule.pipe6.plugFlowPipe.vol_a.dynBal.nPorts+( if not genericAHU.cooler.hydraulicModule.junc456.dynBal.use_mWat_flow then 1 else 0)+genericAHU.cooler.hydraulicModule.junc456.dynBal.nPorts+2* genericAHU.cooler.hydraulicModule.junc456.dynBal.nPorts+(if not genericAHU.cooler.hydraulicModule.PumpInterface.physics.vol.dynBal.use_mWat_flow then 1 else 0)+genericAHU.cooler.hydraulicModule.PumpInterface.physics.vol.dynBal.nPorts +2*genericAHU.cooler.hydraulicModule.PumpInterface.physics.vol.dynBal.nPorts+( if not genericAHU.cooler.dynamicHX.vol1[1].dynBal.use_mWat_flow then 1 else 0) +(if not genericAHU.cooler.dynamicHX.vol1[1].dynBal.use_C_flow then 1 else 0) +3*genericAHU.cooler.dynamicHX.vol1[1].dynBal.nPorts+4*genericAHU.cooler.dynamicHX.vol1[1].dynBal.nPorts +(if not genericAHU.cooler.dynamicHX.vol1[2].dynBal.use_mWat_flow then 1 else 0)+(if not genericAHU.cooler.dynamicHX.vol1[2].dynBal.use_C_flow then 1 else 0)+3*genericAHU.cooler.dynamicHX.vol1[2].dynBal.nPorts+4* genericAHU.cooler.dynamicHX.vol1[2].dynBal.nPorts+(if not genericAHU.cooler.dynamicHX.vol1[3].dynBal.use_mWat_flow then 1 else 0)+(if not genericAHU.cooler.dynamicHX.vol1[3].dynBal.use_C_flow then 1 else 0)+3*genericAHU.cooler.dynamicHX.vol1[3].dynBal.nPorts+4* genericAHU.cooler.dynamicHX.vol1[3].dynBal.nPorts+(if not genericAHU.cooler.dynamicHX.vol1[4].dynBal.use_mWat_flow then 1 else 0)+(if not genericAHU.cooler.dynamicHX.vol1[4].dynBal.use_C_flow then 1 else 0)+3*genericAHU.cooler.dynamicHX.vol1[4].dynBal.nPorts+4* genericAHU.cooler.dynamicHX.vol1[4].dynBal.nPorts+(if not genericAHU.cooler.dynamicHX.vol2[1].dynBal.use_mWat_flow then 1 else 0)+genericAHU.cooler.dynamicHX.vol2[1].dynBal.nPorts+2* genericAHU.cooler.dynamicHX.vol2[1].dynBal.nPorts+(if not genericAHU.cooler.dynamicHX.vol2[2].dynBal.use_mWat_flow then 1 else 0)+genericAHU.cooler.dynamicHX.vol2[2].dynBal.nPorts+2* genericAHU.cooler.dynamicHX.vol2[2].dynBal.nPorts+(if not genericAHU.cooler.dynamicHX.vol2[3].dynBal.use_mWat_flow then 1 else 0)+genericAHU.cooler.dynamicHX.vol2[3].dynBal.nPorts+2* genericAHU.cooler.dynamicHX.vol2[3].dynBal.nPorts+(if not genericAHU.cooler.dynamicHX.vol2[4].dynBal.use_mWat_flow then 1 else 0)+genericAHU.cooler.dynamicHX.vol2[4].dynBal.nPorts+2* genericAHU.cooler.dynamicHX.vol2[4].dynBal.nPorts+(if not genericAHU.heater.hydraulicModule.pipe1.plugFlowPipe.vol_b.dynBal.use_mWat_flow then 1 else 0)+genericAHU.heater.hydraulicModule.pipe1.plugFlowPipe.vol_b.dynBal.nPorts +2*genericAHU.heater.hydraulicModule.pipe1.plugFlowPipe.vol_b.dynBal.nPorts+( if not genericAHU.heater.hydraulicModule.pipe1.plugFlowPipe.vol_a.dynBal.use_mWat_flow then 1 else 0)+genericAHU.heater.hydraulicModule.pipe1.plugFlowPipe.vol_a.dynBal.nPorts +2*genericAHU.heater.hydraulicModule.pipe1.plugFlowPipe.vol_a.dynBal.nPorts+( if not genericAHU.heater.hydraulicModule.pipe2.plugFlowPipe.vol_b.dynBal.use_mWat_flow then 1 else 0)+genericAHU.heater.hydraulicModule.pipe2.plugFlowPipe.vol_b.dynBal.nPorts +2*genericAHU.heater.hydraulicModule.pipe2.plugFlowPipe.vol_b.dynBal.nPorts+( if not genericAHU.heater.hydraulicModule.pipe2.plugFlowPipe.vol_a.dynBal.use_mWat_flow then 1 else 0)+genericAHU.heater.hydraulicModule.pipe2.plugFlowPipe.vol_a.dynBal.nPorts +2*genericAHU.heater.hydraulicModule.pipe2.plugFlowPipe.vol_a.dynBal.nPorts+( if not genericAHU.heater.hydraulicModule.pipe3.plugFlowPipe.vol_b.dynBal.use_mWat_flow then 1 else 0)+genericAHU.heater.hydraulicModule.pipe3.plugFlowPipe.vol_b.dynBal.nPorts +2*genericAHU.heater.hydraulicModule.pipe3.plugFlowPipe.vol_b.dynBal.nPorts+( if not genericAHU.heater.hydraulicModule.pipe3.plugFlowPipe.vol_a.dynBal.use_mWat_flow then 1 else 0)+genericAHU.heater.hydraulicModule.pipe3.plugFlowPipe.vol_a.dynBal.nPorts +2*genericAHU.heater.hydraulicModule.pipe3.plugFlowPipe.vol_a.dynBal.nPorts+( if not genericAHU.heater.hydraulicModule.pipe4.plugFlowPipe.vol_b.dynBal.use_mWat_flow then 1 else 0)+genericAHU.heater.hydraulicModule.pipe4.plugFlowPipe.vol_b.dynBal.nPorts +2*genericAHU.heater.hydraulicModule.pipe4.plugFlowPipe.vol_b.dynBal.nPorts+( if not genericAHU.heater.hydraulicModule.pipe4.plugFlowPipe.vol_a.dynBal.use_mWat_flow then 1 else 0)+genericAHU.heater.hydraulicModule.pipe4.plugFlowPipe.vol_a.dynBal.nPorts +2*genericAHU.heater.hydraulicModule.pipe4.plugFlowPipe.vol_a.dynBal.nPorts+( if not genericAHU.heater.hydraulicModule.pipe5.plugFlowPipe.vol_b.dynBal.use_mWat_flow then 1 else 0)+genericAHU.heater.hydraulicModule.pipe5.plugFlowPipe.vol_b.dynBal.nPorts +2*genericAHU.heater.hydraulicModule.pipe5.plugFlowPipe.vol_b.dynBal.nPorts+( if not genericAHU.heater.hydraulicModule.pipe5.plugFlowPipe.vol_a.dynBal.use_mWat_flow then 1 else 0)+genericAHU.heater.hydraulicModule.pipe5.plugFlowPipe.vol_a.dynBal.nPorts +2*genericAHU.heater.hydraulicModule.pipe5.plugFlowPipe.vol_a.dynBal.nPorts+( if not genericAHU.heater.hydraulicModule.pipe6.plugFlowPipe.vol_b.dynBal.use_mWat_flow then 1 else 0)+genericAHU.heater.hydraulicModule.pipe6.plugFlowPipe.vol_b.dynBal.nPorts +2*genericAHU.heater.hydraulicModule.pipe6.plugFlowPipe.vol_b.dynBal.nPorts+( if not genericAHU.heater.hydraulicModule.pipe6.plugFlowPipe.vol_a.dynBal.use_mWat_flow then 1 else 0)+genericAHU.heater.hydraulicModule.pipe6.plugFlowPipe.vol_a.dynBal.nPorts +2*genericAHU.heater.hydraulicModule.pipe6.plugFlowPipe.vol_a.dynBal.nPorts+( if not genericAHU.heater.hydraulicModule.junc456.dynBal.use_mWat_flow then 1 else 0)+genericAHU.heater.hydraulicModule.junc456.dynBal.nPorts+2* genericAHU.heater.hydraulicModule.junc456.dynBal.nPorts+(if not genericAHU.heater.hydraulicModule.PumpInterface.physics.vol.dynBal.use_mWat_flow then 1 else 0)+genericAHU.heater.hydraulicModule.PumpInterface.physics.vol.dynBal.nPorts +2*genericAHU.heater.hydraulicModule.PumpInterface.physics.vol.dynBal.nPorts+( if not genericAHU.heater.dynamicHX.vol1[1].dynBal.use_mWat_flow then 1 else 0) +(if not genericAHU.heater.dynamicHX.vol1[1].dynBal.use_C_flow then 1 else 0) +3*genericAHU.heater.dynamicHX.vol1[1].dynBal.nPorts+4*genericAHU.heater.dynamicHX.vol1[1].dynBal.nPorts +(if not genericAHU.heater.dynamicHX.vol1[2].dynBal.use_mWat_flow then 1 else 0)+(if not genericAHU.heater.dynamicHX.vol1[2].dynBal.use_C_flow then 1 else 0)+3*genericAHU.heater.dynamicHX.vol1[2].dynBal.nPorts+4* genericAHU.heater.dynamicHX.vol1[2].dynBal.nPorts+(if not genericAHU.heater.dynamicHX.vol1[3].dynBal.use_mWat_flow then 1 else 0)+(if not genericAHU.heater.dynamicHX.vol1[3].dynBal.use_C_flow then 1 else 0)+3*genericAHU.heater.dynamicHX.vol1[3].dynBal.nPorts+4* genericAHU.heater.dynamicHX.vol1[3].dynBal.nPorts+(if not genericAHU.heater.dynamicHX.vol1[4].dynBal.use_mWat_flow then 1 else 0)+(if not genericAHU.heater.dynamicHX.vol1[4].dynBal.use_C_flow then 1 else 0)+3*genericAHU.heater.dynamicHX.vol1[4].dynBal.nPorts+4* genericAHU.heater.dynamicHX.vol1[4].dynBal.nPorts+(if not genericAHU.heater.dynamicHX.vol2[1].dynBal.use_mWat_flow then 1 else 0)+genericAHU.heater.dynamicHX.vol2[1].dynBal.nPorts+2* genericAHU.heater.dynamicHX.vol2[1].dynBal.nPorts+(if not genericAHU.heater.dynamicHX.vol2[2].dynBal.use_mWat_flow then 1 else 0)+genericAHU.heater.dynamicHX.vol2[2].dynBal.nPorts+2* genericAHU.heater.dynamicHX.vol2[2].dynBal.nPorts+(if not genericAHU.heater.dynamicHX.vol2[3].dynBal.use_mWat_flow then 1 else 0)+genericAHU.heater.dynamicHX.vol2[3].dynBal.nPorts+2* genericAHU.heater.dynamicHX.vol2[3].dynBal.nPorts+(if not genericAHU.heater.dynamicHX.vol2[4].dynBal.use_mWat_flow then 1 else 0)+genericAHU.heater.dynamicHX.vol2[4].dynBal.nPorts+2* genericAHU.heater.dynamicHX.vol2[4].dynBal.nPorts+(if not genericAHU.dynamicHX.vol1[1].dynBal.use_mWat_flow then 1 else 0)+(if not genericAHU.dynamicHX.vol1[1].dynBal.use_C_flow then 1 else 0)+3*genericAHU.dynamicHX.vol1[1].dynBal.nPorts+4*genericAHU.dynamicHX.vol1[1].dynBal.nPorts +(if not genericAHU.dynamicHX.vol1[2].dynBal.use_mWat_flow then 1 else 0)+( if not genericAHU.dynamicHX.vol1[2].dynBal.use_C_flow then 1 else 0)+3* genericAHU.dynamicHX.vol1[2].dynBal.nPorts+4*genericAHU.dynamicHX.vol1[2].dynBal.nPorts +(if not genericAHU.dynamicHX.vol2[1].dynBal.use_mWat_flow then 1 else 0)+( if not genericAHU.dynamicHX.vol2[1].use_C_flow then 1 else 0)+3* genericAHU.dynamicHX.vol2[1].dynBal.nPorts+4*genericAHU.dynamicHX.vol2[1].dynBal.nPorts +(if not genericAHU.dynamicHX.vol2[2].dynBal.use_mWat_flow then 1 else 0)+( if not genericAHU.dynamicHX.vol2[2].use_C_flow then 1 else 0)+3* genericAHU.dynamicHX.vol2[2].dynBal.nPorts+4*genericAHU.dynamicHX.vol2[2].dynBal.nPorts +(if not genericAHU.fanSup.vol.dynBal.use_mWat_flow then 1 else 0)+(if not genericAHU.fanSup.vol.use_C_flow then 1 else 0)+3*genericAHU.fanSup.vol.dynBal.nPorts +4*genericAHU.fanSup.vol.dynBal.nPorts+(if not genericAHU.fanRet.vol.dynBal.use_mWat_flow then 1 else 0)+(if not genericAHU.fanRet.vol.use_C_flow then 1 else 0)+3* genericAHU.fanRet.vol.dynBal.nPorts+4*genericAHU.fanRet.vol.dynBal.nPorts+(if not genericAHU.humidifier.vol.use_C_flow then 1 else 0)+3*genericAHU.humidifier.vol.dynBal.nPorts +4*genericAHU.humidifier.vol.dynBal.nPorts+14*thermalZone.zoneParam.nOrientations +(if not thermalZone.eqAirTempWall.TGroundFromInput then 1 else 0)+ thermalZone.zoneParam.nOrientations+2*thermalZone.zoneParam.nOrientations+ thermalZone.ventCont.optimalTemp.nout+thermalZone.ventCont.dEMA.ExpAVG.n-1+ thermalZone.ventCont.dEMA.ExpAVG1.n-1+(if not thermalZone.x_pTphi.use_p_in then 1 else 0)+(if not genericAHU.preheater.hydraulicModule.valve.vol.dynBal.use_mWat_flow then 1 else 0)+genericAHU.preheater.hydraulicModule.valve.vol.dynBal.nPorts+2 *genericAHU.preheater.hydraulicModule.valve.vol.dynBal.nPorts+(if not genericAHU.cooler.hydraulicModule.valve.vol.dynBal.use_mWat_flow then 1 else 0) +genericAHU.cooler.hydraulicModule.valve.vol.dynBal.nPorts+2*genericAHU.cooler.hydraulicModule.valve.vol.dynBal.nPorts +(if not genericAHU.heater.hydraulicModule.valve.vol.dynBal.use_mWat_flow then 1 else 0)+genericAHU.heater.hydraulicModule.valve.vol.dynBal.nPorts+2* genericAHU.heater.hydraulicModule.valve.vol.dynBal.nPorts+(if not thermalZone.use_C_flow then 1 else 0)+3*thermalZone.ROM.volMoiAir.dynBal.nPorts +4*thermalZone.ROM.volMoiAir.dynBal.nPorts+size(genericAHU.cooler.hydraulicModule.PumpInterface.physics.maxMinTable.columns, 1)+size(genericAHU.heater.hydraulicModule.PumpInterface.physics.maxMinTable.columns, 1)+size(genericAHU.preheater.hydraulicModule.PumpInterface.physics.maxMinTable.columns, 1)+thermalZone.zoneParam.nOrientations+thermalZone.zoneParam.nOrientations +scalar equations. +However, exploiting the given numerical settings of parameters gives the same number of unknowns and equations: + 11521 +Check of AixLib.Systems.ModularAHU.Examples.DemandControlledAHU successful. +Declaring variable: Boolean rCheck ; + +Modelica.Utilities.Streams.print(" { \"file\" : \"AixLib/Resources/Scripts/Dymola/Systems/ModularAHU/Examples/DemandControlledAHU.mos\",", "AixLib.Systems.ModularAHU.Examples.DemandControlledAHU.statistics.log"); +Modelica.Utilities.Streams.print(" \"model\" : \"AixLib.Systems.ModularAHU.Examples.DemandControlledAHU\",", "AixLib.Systems.ModularAHU.Examples.DemandControlledAHU.statistics.log"); +Modelica.Utilities.Streams.print(" \"check\" : {", "AixLib.Systems.ModularAHU.Examples.DemandControlledAHU.statistics.log"); +Modelica.Utilities.Streams.print(" \"command\" : \"checkModel(\\\"AixLib.Systems.ModularAHU.Examples.DemandControlledAHU\\\");\",", "AixLib.Systems.ModularAHU.Examples.DemandControlledAHU.statistics.log"); +Modelica.Utilities.Streams.print(" \"result\" : " + String(rCheck), "AixLib.Systems.ModularAHU.Examples.DemandControlledAHU.statistics.log"); +Modelica.Utilities.Streams.print(" },", "AixLib.Systems.ModularAHU.Examples.DemandControlledAHU.statistics.log"); + + +rScript=RunScript("modelica://AixLib/Resources/Scripts/Dymola/Systems/ModularAHU/Examples/DemandControlledAHU.mos"); +simulateModel("AixLib.Systems.ModularAHU.Examples.DemandControlledAHU", tolerance=1e-5, startTime=5961600, stopTime=6566400, outputInterval=120, resultFile="AixLib.Systems.ModularAHU.Examples.DemandControlledAHU"); +Translation of AixLib.Systems.ModularAHU.Examples.DemandControlledAHU +The DAE has 11521 scalar unknowns and 11521 scalar equations. +Redundant consistent initial conditions. +Removed the following equations which are redundant and consistent: + genericAHU.preheater.dynamicHX.vol1[2].p_start = genericAHU.preheater.dynamicHX.p1_start; + genericAHU.preheater.dynamicHX.vol1[3].p_start = genericAHU.preheater.dynamicHX.p1_start; + genericAHU.preheater.dynamicHX.vol1[4].p_start = genericAHU.preheater.dynamicHX.p1_start; + genericAHU.preheater.dynamicHX.vol1[5].p_start = genericAHU.preheater.dynamicHX.p1_start; + genericAHU.cooler.dynamicHX.vol1[2].p_start = genericAHU.cooler.dynamicHX.p1_start; + genericAHU.cooler.dynamicHX.vol1[3].p_start = genericAHU.cooler.dynamicHX.p1_start; + genericAHU.cooler.dynamicHX.vol1[4].p_start = genericAHU.cooler.dynamicHX.p1_start; + genericAHU.heater.dynamicHX.vol1[2].p_start = genericAHU.heater.dynamicHX.p1_start; + genericAHU.heater.dynamicHX.vol1[3].p_start = genericAHU.heater.dynamicHX.p1_start; + genericAHU.heater.dynamicHX.vol1[4].p_start = genericAHU.heater.dynamicHX.p1_start; + genericAHU.dynamicHX.vol1[1].p_start = genericAHU.dynamicHX.p1_start; + genericAHU.dynamicHX.vol2[1].p_start = genericAHU.dynamicHX.p2_start; + genericAHU.fanSup.filter.y_start = genericAHU.fanSup.dp_start; + genericAHU.humidifier.vol.p_start = genericAHU.humidifier.p_start; + if (genericAHU.dynamicHX.vol1[2].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (genericAHU.dynamicHX.vol1[2].dynBal.initialize_p) then + genericAHU.dynamicHX.vol1[2].dynBal.medium.p = genericAHU.dynamicHX.vol1[2].dynBal.p_start; + end if; + else + if (genericAHU.dynamicHX.vol1[2].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. SteadyStateInitial) then + if (genericAHU.dynamicHX.vol1[2].dynBal.initialize_p) then + der(genericAHU.dynamicHX.vol1[2].dynBal.medium.p) = 0; + end if; + end if; + end if; + +This required evaluation of +the interactive parameters + boundaryExhaustAir.p(start = 101325) + genericAHU.dynamicHX.p1_start(start = 101325) + genericAHU.fanSup.dp_start(start = 0) + genericAHU.fanSup.p_start(start = 101325) + genericAHU.humidifier.p_start(start = 101325) + thermalZone.p_start(start = 101325) + +The redundancies involve +initial equations: + genericAHU.fanSup.filter.y = genericAHU.fanSup.filter.y_start; + genericAHU.preheater.dynamicHX.vol1[1].dynBal.medium.p = genericAHU.preheater.dynamicHX.vol1[1].dynBal.p_start; + genericAHU.preheater.dynamicHX.vol1[2].dynBal.medium.p = genericAHU.preheater.dynamicHX.vol1[2].dynBal.p_start; + genericAHU.preheater.dynamicHX.vol1[3].dynBal.medium.p = genericAHU.preheater.dynamicHX.vol1[3].dynBal.p_start; + genericAHU.preheater.dynamicHX.vol1[4].dynBal.medium.p = genericAHU.preheater.dynamicHX.vol1[4].dynBal.p_start; + genericAHU.preheater.dynamicHX.vol1[5].dynBal.medium.p = genericAHU.preheater.dynamicHX.vol1[5].dynBal.p_start; + genericAHU.cooler.dynamicHX.vol1[1].dynBal.medium.p = genericAHU.cooler.dynamicHX.vol1[1].dynBal.p_start; + genericAHU.cooler.dynamicHX.vol1[2].dynBal.medium.p = genericAHU.cooler.dynamicHX.vol1[2].dynBal.p_start; + genericAHU.cooler.dynamicHX.vol1[3].dynBal.medium.p = genericAHU.cooler.dynamicHX.vol1[3].dynBal.p_start; + genericAHU.cooler.dynamicHX.vol1[4].dynBal.medium.p = genericAHU.cooler.dynamicHX.vol1[4].dynBal.p_start; + genericAHU.heater.dynamicHX.vol1[1].dynBal.medium.p = genericAHU.heater.dynamicHX.vol1[1].dynBal.p_start; + genericAHU.heater.dynamicHX.vol1[2].dynBal.medium.p = genericAHU.heater.dynamicHX.vol1[2].dynBal.p_start; + genericAHU.heater.dynamicHX.vol1[3].dynBal.medium.p = genericAHU.heater.dynamicHX.vol1[3].dynBal.p_start; + genericAHU.heater.dynamicHX.vol1[4].dynBal.medium.p = genericAHU.heater.dynamicHX.vol1[4].dynBal.p_start; + genericAHU.dynamicHX.vol1[1].dynBal.medium.p = genericAHU.dynamicHX.vol1[1].dynBal.p_start; + genericAHU.dynamicHX.vol1[2].dynBal.medium.p = genericAHU.dynamicHX.vol1[2].dynBal.p_start; + genericAHU.dynamicHX.vol2[1].dynBal.medium.p = genericAHU.dynamicHX.vol2[1].dynBal.p_start; + genericAHU.dynamicHX.vol2[2].dynBal.medium.p = genericAHU.dynamicHX.vol2[2].dynBal.p_start; + genericAHU.fanSup.vol.dynBal.medium.p = genericAHU.fanSup.vol.dynBal.p_start; + genericAHU.humidifier.vol.dynBal.medium.p = genericAHU.humidifier.vol.dynBal.p_start; + thermalZone.ROM.volMoiAir.dynBal.medium.p = thermalZone.ROM.volMoiAir.dynBal.p_start; + + +Statistics + +Original Model + Number of components: 2017 + Variables: 24959 + Constants: 542 (542 scalars) + Parameters: 10793 (14586 scalars) + Unknowns: 13624 (12024 scalars) + Differentiated variables: 348 scalars + Equations: 10333 + Nontrivial: 8299 +Translated Model + Constants: 8117 scalars + Free parameters: 3606 scalars + Parameter depending: 4645 scalars + Outputs: 23 scalars + Continuous time states: 272 scalars + Time-varying variables: 3262 scalars + Alias variables: 7522 scalars + Number of mixed real/discrete systems of equations: 0 + Sizes of linear systems of equations: {5, 3, 5, 5, 6, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 22, 4} + Sizes after manipulation of the linear systems: {0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 4, 0} + Sizes of nonlinear systems of equations: {1, 1, 1, 3, 1, 1, 1, 4, 18, 6, 6, 6, 6, 6, 6, 17, 6, 6, 6, 6, 6, 6, 17, 6, 6, 6, 6, 6, 6, 1, 1, 1, 1, 1, 1} + Sizes after manipulation of the nonlinear systems: {0, 0, 0, 1, 0, 0, 0, 1, 2, 1, 1, 1, 1, 1, 1, 2, 1, 1, 1, 1, 1, 1, 2, 1, 1, 1, 1, 1, 1, 0, 1, 0, 1, 0, 1} + Number of numerical Jacobians: 0 + Initialization problem + Sizes of linear systems of equations: {24, 5} + Sizes after manipulation of the linear systems: {4, 0} + Sizes of nonlinear systems of equations: {18, 1, 17, 1, 17, 1, 1, 3, 1, 1, 1, 1, 4, 1} + Sizes after manipulation of the nonlinear systems: {4, 0, 3, 0, 3, 0, 0, 1, 0, 0, 0, 0, 1, 0} + Sizes of simplified homotopy nonlinear systems of equations: {18, 1, 17, 1, 17, 1, 3, 1, 4, 1} + Sizes after manipulation of the simplified homotopy nonlinear systems: {3, 0, 3, 0, 3, 0, 1, 0, 1, 0} + Number of numerical Jacobians: 0 + +Sparse solvers enabled: false +Enabled for integrator Jacobian: false +Model sparse and large enough: true. +Sparse solvers are available for dassl, lsodar, cvode, ida, radau, esdirk*, sdirk*. +Enable sparse solvers by setting Advanced.Translation.SparseActivate. +Selected continuous time states +Statically selected continuous time states +ctrAHUCO2.ctrCo.PID.D.x +ctrAHUCO2.ctrCo.PID.I.y +ctrAHUCO2.ctrPh.PID.D.x +ctrAHUCO2.ctrPh.PID.I.y +ctrAHUCO2.ctrRh.PID.D.x +ctrAHUCO2.ctrRh.PID.I.y +ctrAHUCO2.PID_CO2.I.y +ctrAHUCO2.PID_SteamHum.I.y +ctrAHUCO2.PID_VflowSup.I.y +genericAHU.cooler.dynamicHX.heatCapacitor[1].T +genericAHU.cooler.dynamicHX.heatCapacitor[2].T +genericAHU.cooler.dynamicHX.heatCapacitor[3].T +genericAHU.cooler.dynamicHX.heatCapacitor[4].T +genericAHU.cooler.dynamicHX.vol1[1].dynBal.mC[1] +genericAHU.cooler.dynamicHX.vol1[1].dynBal.medium.Xi[1] +genericAHU.cooler.dynamicHX.vol1[1].dynBal.U +genericAHU.cooler.dynamicHX.vol1[2].dynBal.mC[1] +genericAHU.cooler.dynamicHX.vol1[2].dynBal.medium.Xi[1] +genericAHU.cooler.dynamicHX.vol1[2].dynBal.U +genericAHU.cooler.dynamicHX.vol1[3].dynBal.mC[1] +genericAHU.cooler.dynamicHX.vol1[3].dynBal.medium.Xi[1] +genericAHU.cooler.dynamicHX.vol1[3].dynBal.U +genericAHU.cooler.dynamicHX.vol1[4].dynBal.mC[1] +genericAHU.cooler.dynamicHX.vol1[4].dynBal.medium.Xi[1] +genericAHU.cooler.dynamicHX.vol1[4].dynBal.U +genericAHU.cooler.dynamicHX.vol2[1].dynBal.U +genericAHU.cooler.dynamicHX.vol2[2].dynBal.U +genericAHU.cooler.dynamicHX.vol2[3].dynBal.U +genericAHU.cooler.dynamicHX.vol2[4].dynBal.U +genericAHU.cooler.hydraulicModule.junc456.dynBal.U +genericAHU.cooler.hydraulicModule.pipe1.Insulation.CylindricLoad1.heatCapacitor.T +genericAHU.cooler.hydraulicModule.pipe1.plugFlowPipe.del.x +genericAHU.cooler.hydraulicModule.pipe1.plugFlowPipe.timDel.x +genericAHU.cooler.hydraulicModule.pipe1.plugFlowPipe.vol_a.dynBal.U +genericAHU.cooler.hydraulicModule.pipe1.plugFlowPipe.vol_b.dynBal.U +genericAHU.cooler.hydraulicModule.pipe2.Insulation.CylindricLoad1.heatCapacitor.T +genericAHU.cooler.hydraulicModule.pipe2.plugFlowPipe.del.x +genericAHU.cooler.hydraulicModule.pipe2.plugFlowPipe.timDel.x +genericAHU.cooler.hydraulicModule.pipe2.plugFlowPipe.vol_a.dynBal.U +genericAHU.cooler.hydraulicModule.pipe2.plugFlowPipe.vol_b.dynBal.U +genericAHU.cooler.hydraulicModule.pipe3.Insulation.CylindricLoad1.heatCapacitor.T +genericAHU.cooler.hydraulicModule.pipe3.plugFlowPipe.del.x +genericAHU.cooler.hydraulicModule.pipe3.plugFlowPipe.timDel.x +genericAHU.cooler.hydraulicModule.pipe3.plugFlowPipe.vol_a.dynBal.U +genericAHU.cooler.hydraulicModule.pipe3.plugFlowPipe.vol_b.dynBal.U +genericAHU.cooler.hydraulicModule.pipe4.Insulation.CylindricLoad1.heatCapacitor.T +genericAHU.cooler.hydraulicModule.pipe4.plugFlowPipe.del.x +genericAHU.cooler.hydraulicModule.pipe4.plugFlowPipe.timDel.x +genericAHU.cooler.hydraulicModule.pipe4.plugFlowPipe.vol_a.dynBal.U +genericAHU.cooler.hydraulicModule.pipe4.plugFlowPipe.vol_b.dynBal.U +genericAHU.cooler.hydraulicModule.pipe5.Insulation.CylindricLoad1.heatCapacitor.T +genericAHU.cooler.hydraulicModule.pipe5.plugFlowPipe.del.x +genericAHU.cooler.hydraulicModule.pipe5.plugFlowPipe.timDel.x +genericAHU.cooler.hydraulicModule.pipe5.plugFlowPipe.vol_a.dynBal.U +genericAHU.cooler.hydraulicModule.pipe5.plugFlowPipe.vol_b.dynBal.U +genericAHU.cooler.hydraulicModule.pipe6.Insulation.CylindricLoad1.heatCapacitor.T +genericAHU.cooler.hydraulicModule.pipe6.plugFlowPipe.del.x +genericAHU.cooler.hydraulicModule.pipe6.plugFlowPipe.timDel.x +genericAHU.cooler.hydraulicModule.pipe6.plugFlowPipe.vol_a.dynBal.U +genericAHU.cooler.hydraulicModule.pipe6.plugFlowPipe.vol_b.dynBal.U +genericAHU.cooler.hydraulicModule.PT1_a1.y +genericAHU.cooler.hydraulicModule.PT1_a2.y +genericAHU.cooler.hydraulicModule.PT1_b1.y +genericAHU.cooler.hydraulicModule.PT1_b2.y +genericAHU.cooler.hydraulicModule.PumpInterface.physics.criticalDamping.x[1] +genericAHU.cooler.hydraulicModule.PumpInterface.physics.criticalDamping.x[2] +genericAHU.cooler.hydraulicModule.senT_a1.T +genericAHU.cooler.hydraulicModule.senT_a2.T +genericAHU.cooler.hydraulicModule.senT_b1.T +genericAHU.cooler.hydraulicModule.senT_b2.T +genericAHU.cooler.hydraulicModule.valve.filter.s[1] +genericAHU.cooler.hydraulicModule.valve.vol.dynBal.U +genericAHU.cooler.port_a1.p +genericAHU.cooler.port_b1.p +genericAHU.cooler.PT1_airIn.y +genericAHU.cooler.PT1_airOut.y +genericAHU.cooler.senT_airIn.T +genericAHU.cooler.senT_airOut.T +genericAHU.dampBypass.filter.s[1] +genericAHU.dampBypass.filter.s[2] +genericAHU.dampHX.filter.s[1] +genericAHU.dampHX.filter.s[2] +genericAHU.dampHX.port_a.p +genericAHU.dynamicHX.heatCapacitor[1].T +genericAHU.dynamicHX.heatCapacitor[2].T +genericAHU.dynamicHX.vol1[1].dynBal.mC[1] +genericAHU.dynamicHX.vol1[1].dynBal.medium.Xi[1] +genericAHU.dynamicHX.vol1[1].dynBal.U +genericAHU.dynamicHX.vol1[2].dynBal.mC[1] +genericAHU.dynamicHX.vol1[2].dynBal.medium.Xi[1] +genericAHU.dynamicHX.vol1[2].dynBal.U +genericAHU.dynamicHX.vol2[1].dynBal.mC[1] +genericAHU.dynamicHX.vol2[1].dynBal.medium.Xi[1] +genericAHU.dynamicHX.vol2[1].dynBal.U +genericAHU.dynamicHX.vol2[2].dynBal.mC[1] +genericAHU.dynamicHX.vol2[2].dynBal.medium.Xi[1] +genericAHU.dynamicHX.vol2[2].dynBal.U +genericAHU.fanRet.filter.s[1] +genericAHU.fanRet.filter.s[2] +genericAHU.fanRet.vol.dynBal.m +genericAHU.fanRet.vol.dynBal.mC[1] +genericAHU.fanRet.vol.dynBal.medium.Xi[1] +genericAHU.fanRet.vol.dynBal.U +genericAHU.fanSup.filter.s[1] +genericAHU.fanSup.filter.s[2] +genericAHU.fanSup.vol.dynBal.mC[1] +genericAHU.fanSup.vol.dynBal.medium.Xi[1] +genericAHU.fanSup.vol.dynBal.U +genericAHU.flapRet.filter.s[1] +genericAHU.flapRet.filter.s[2] +genericAHU.flapSup.filter.s[1] +genericAHU.flapSup.filter.s[2] +genericAHU.heater.dynamicHX.heatCapacitor[1].T +genericAHU.heater.dynamicHX.heatCapacitor[2].T +genericAHU.heater.dynamicHX.heatCapacitor[3].T +genericAHU.heater.dynamicHX.heatCapacitor[4].T +genericAHU.heater.dynamicHX.vol1[1].dynBal.mC[1] +genericAHU.heater.dynamicHX.vol1[1].dynBal.medium.Xi[1] +genericAHU.heater.dynamicHX.vol1[1].dynBal.U +genericAHU.heater.dynamicHX.vol1[2].dynBal.mC[1] +genericAHU.heater.dynamicHX.vol1[2].dynBal.medium.Xi[1] +genericAHU.heater.dynamicHX.vol1[2].dynBal.U +genericAHU.heater.dynamicHX.vol1[3].dynBal.mC[1] +genericAHU.heater.dynamicHX.vol1[3].dynBal.medium.Xi[1] +genericAHU.heater.dynamicHX.vol1[3].dynBal.U +genericAHU.heater.dynamicHX.vol1[4].dynBal.mC[1] +genericAHU.heater.dynamicHX.vol1[4].dynBal.medium.Xi[1] +genericAHU.heater.dynamicHX.vol1[4].dynBal.U +genericAHU.heater.dynamicHX.vol2[1].dynBal.U +genericAHU.heater.dynamicHX.vol2[2].dynBal.U +genericAHU.heater.dynamicHX.vol2[3].dynBal.U +genericAHU.heater.dynamicHX.vol2[4].dynBal.U +genericAHU.heater.hydraulicModule.junc456.dynBal.U +genericAHU.heater.hydraulicModule.pipe1.Insulation.CylindricLoad1.heatCapacitor.T +genericAHU.heater.hydraulicModule.pipe1.plugFlowPipe.del.x +genericAHU.heater.hydraulicModule.pipe1.plugFlowPipe.timDel.x +genericAHU.heater.hydraulicModule.pipe1.plugFlowPipe.vol_a.dynBal.U +genericAHU.heater.hydraulicModule.pipe1.plugFlowPipe.vol_b.dynBal.U +genericAHU.heater.hydraulicModule.pipe2.Insulation.CylindricLoad1.heatCapacitor.T +genericAHU.heater.hydraulicModule.pipe2.plugFlowPipe.del.x +genericAHU.heater.hydraulicModule.pipe2.plugFlowPipe.timDel.x +genericAHU.heater.hydraulicModule.pipe2.plugFlowPipe.vol_a.dynBal.U +genericAHU.heater.hydraulicModule.pipe2.plugFlowPipe.vol_b.dynBal.U +genericAHU.heater.hydraulicModule.pipe3.Insulation.CylindricLoad1.heatCapacitor.T +genericAHU.heater.hydraulicModule.pipe3.plugFlowPipe.del.x +genericAHU.heater.hydraulicModule.pipe3.plugFlowPipe.timDel.x +genericAHU.heater.hydraulicModule.pipe3.plugFlowPipe.vol_a.dynBal.U +genericAHU.heater.hydraulicModule.pipe3.plugFlowPipe.vol_b.dynBal.U +genericAHU.heater.hydraulicModule.pipe4.Insulation.CylindricLoad1.heatCapacitor.T +genericAHU.heater.hydraulicModule.pipe4.plugFlowPipe.del.x +genericAHU.heater.hydraulicModule.pipe4.plugFlowPipe.timDel.x +genericAHU.heater.hydraulicModule.pipe4.plugFlowPipe.vol_a.dynBal.U +genericAHU.heater.hydraulicModule.pipe4.plugFlowPipe.vol_b.dynBal.U +genericAHU.heater.hydraulicModule.pipe5.Insulation.CylindricLoad1.heatCapacitor.T +genericAHU.heater.hydraulicModule.pipe5.plugFlowPipe.del.x +genericAHU.heater.hydraulicModule.pipe5.plugFlowPipe.timDel.x +genericAHU.heater.hydraulicModule.pipe5.plugFlowPipe.vol_a.dynBal.U +genericAHU.heater.hydraulicModule.pipe5.plugFlowPipe.vol_b.dynBal.U +genericAHU.heater.hydraulicModule.pipe6.Insulation.CylindricLoad1.heatCapacitor.T +genericAHU.heater.hydraulicModule.pipe6.plugFlowPipe.del.x +genericAHU.heater.hydraulicModule.pipe6.plugFlowPipe.timDel.x +genericAHU.heater.hydraulicModule.pipe6.plugFlowPipe.vol_a.dynBal.U +genericAHU.heater.hydraulicModule.pipe6.plugFlowPipe.vol_b.dynBal.U +genericAHU.heater.hydraulicModule.PT1_a1.y +genericAHU.heater.hydraulicModule.PT1_a2.y +genericAHU.heater.hydraulicModule.PT1_b1.y +genericAHU.heater.hydraulicModule.PT1_b2.y +genericAHU.heater.hydraulicModule.PumpInterface.physics.criticalDamping.x[1] +genericAHU.heater.hydraulicModule.PumpInterface.physics.criticalDamping.x[2] +genericAHU.heater.hydraulicModule.senT_a1.T +genericAHU.heater.hydraulicModule.senT_a2.T +genericAHU.heater.hydraulicModule.senT_b1.T +genericAHU.heater.hydraulicModule.senT_b2.T +genericAHU.heater.hydraulicModule.valve.vol.dynBal.U +genericAHU.heater.port_b1.p +genericAHU.heater.PT1_airIn.y +genericAHU.heater.PT1_airOut.y +genericAHU.heater.senT_airIn.T +genericAHU.heater.senT_airOut.T +genericAHU.humidifier.vol.dynBal.mC[1] +genericAHU.humidifier.vol.dynBal.medium.Xi[1] +genericAHU.humidifier.vol.dynBal.U +genericAHU.preheater.dynamicHX.heatCapacitor[1].T +genericAHU.preheater.dynamicHX.heatCapacitor[2].T +genericAHU.preheater.dynamicHX.heatCapacitor[3].T +genericAHU.preheater.dynamicHX.heatCapacitor[4].T +genericAHU.preheater.dynamicHX.heatCapacitor[5].T +genericAHU.preheater.dynamicHX.vol1[1].dynBal.mC[1] +genericAHU.preheater.dynamicHX.vol1[1].dynBal.medium.Xi[1] +genericAHU.preheater.dynamicHX.vol1[1].dynBal.U +genericAHU.preheater.dynamicHX.vol1[2].dynBal.mC[1] +genericAHU.preheater.dynamicHX.vol1[2].dynBal.medium.Xi[1] +genericAHU.preheater.dynamicHX.vol1[2].dynBal.U +genericAHU.preheater.dynamicHX.vol1[3].dynBal.mC[1] +genericAHU.preheater.dynamicHX.vol1[3].dynBal.medium.Xi[1] +genericAHU.preheater.dynamicHX.vol1[3].dynBal.U +genericAHU.preheater.dynamicHX.vol1[4].dynBal.mC[1] +genericAHU.preheater.dynamicHX.vol1[4].dynBal.medium.Xi[1] +genericAHU.preheater.dynamicHX.vol1[4].dynBal.U +genericAHU.preheater.dynamicHX.vol1[5].dynBal.mC[1] +genericAHU.preheater.dynamicHX.vol1[5].dynBal.medium.Xi[1] +genericAHU.preheater.dynamicHX.vol1[5].dynBal.U +genericAHU.preheater.dynamicHX.vol2[1].dynBal.U +genericAHU.preheater.dynamicHX.vol2[2].dynBal.U +genericAHU.preheater.dynamicHX.vol2[3].dynBal.U +genericAHU.preheater.dynamicHX.vol2[4].dynBal.U +genericAHU.preheater.dynamicHX.vol2[5].dynBal.U +genericAHU.preheater.hydraulicModule.junc456.dynBal.U +genericAHU.preheater.hydraulicModule.pipe1.Insulation.CylindricLoad1.heatCapacitor.T +genericAHU.preheater.hydraulicModule.pipe1.plugFlowPipe.del.x +genericAHU.preheater.hydraulicModule.pipe1.plugFlowPipe.timDel.x +genericAHU.preheater.hydraulicModule.pipe1.plugFlowPipe.vol_a.dynBal.U +genericAHU.preheater.hydraulicModule.pipe1.plugFlowPipe.vol_b.dynBal.U +genericAHU.preheater.hydraulicModule.pipe2.Insulation.CylindricLoad1.heatCapacitor.T +genericAHU.preheater.hydraulicModule.pipe2.plugFlowPipe.del.x +genericAHU.preheater.hydraulicModule.pipe2.plugFlowPipe.timDel.x +genericAHU.preheater.hydraulicModule.pipe2.plugFlowPipe.vol_a.dynBal.U +genericAHU.preheater.hydraulicModule.pipe2.plugFlowPipe.vol_b.dynBal.U +genericAHU.preheater.hydraulicModule.pipe3.Insulation.CylindricLoad1.heatCapacitor.T +genericAHU.preheater.hydraulicModule.pipe3.plugFlowPipe.del.x +genericAHU.preheater.hydraulicModule.pipe3.plugFlowPipe.timDel.x +genericAHU.preheater.hydraulicModule.pipe3.plugFlowPipe.vol_a.dynBal.U +genericAHU.preheater.hydraulicModule.pipe3.plugFlowPipe.vol_b.dynBal.U +genericAHU.preheater.hydraulicModule.pipe4.Insulation.CylindricLoad1.heatCapacitor.T +genericAHU.preheater.hydraulicModule.pipe4.plugFlowPipe.del.x +genericAHU.preheater.hydraulicModule.pipe4.plugFlowPipe.timDel.x +genericAHU.preheater.hydraulicModule.pipe4.plugFlowPipe.vol_a.dynBal.U +genericAHU.preheater.hydraulicModule.pipe4.plugFlowPipe.vol_b.dynBal.U +genericAHU.preheater.hydraulicModule.pipe5.Insulation.CylindricLoad1.heatCapacitor.T +genericAHU.preheater.hydraulicModule.pipe5.plugFlowPipe.del.x +genericAHU.preheater.hydraulicModule.pipe5.plugFlowPipe.timDel.x +genericAHU.preheater.hydraulicModule.pipe5.plugFlowPipe.vol_a.dynBal.U +genericAHU.preheater.hydraulicModule.pipe5.plugFlowPipe.vol_b.dynBal.U +genericAHU.preheater.hydraulicModule.pipe6.Insulation.CylindricLoad1.heatCapacitor.T +genericAHU.preheater.hydraulicModule.pipe6.plugFlowPipe.del.x +genericAHU.preheater.hydraulicModule.pipe6.plugFlowPipe.timDel.x +genericAHU.preheater.hydraulicModule.pipe6.plugFlowPipe.vol_a.dynBal.U +genericAHU.preheater.hydraulicModule.pipe6.plugFlowPipe.vol_b.dynBal.U +genericAHU.preheater.hydraulicModule.PT1_a1.y +genericAHU.preheater.hydraulicModule.PT1_a2.y +genericAHU.preheater.hydraulicModule.PT1_b1.y +genericAHU.preheater.hydraulicModule.PT1_b2.y +genericAHU.preheater.hydraulicModule.PumpInterface.physics.criticalDamping.x[1] +genericAHU.preheater.hydraulicModule.PumpInterface.physics.criticalDamping.x[2] +genericAHU.preheater.hydraulicModule.senT_a1.T +genericAHU.preheater.hydraulicModule.senT_a2.T +genericAHU.preheater.hydraulicModule.senT_b1.T +genericAHU.preheater.hydraulicModule.senT_b2.T +genericAHU.preheater.hydraulicModule.valve.filter.s[1] +genericAHU.preheater.hydraulicModule.valve.vol.dynBal.U +genericAHU.preheater.PT1_airIn.y +genericAHU.preheater.PT1_airOut.y +genericAHU.preheater.senT_airIn.T +genericAHU.preheater.senT_airOut.T +genericAHU.PT1_airIn.y +genericAHU.PT1_airIn1.y +genericAHU.PT1_airIn2.y +genericAHU.PT1_airIn3.y +genericAHU.senRelHumSup.phi +genericAHU.senRelHumSup1.phi +genericAHU.senTExh.T +genericAHU.senTOda.T +genericAHU.senTRet.T +genericAHU.senTSup.T +thermalZone.ROM.extWallRC.thermCapExt[1].T +thermalZone.ROM.intWallRC.thermCapInt[1].T +thermalZone.ROM.volMoiAir.dynBal.m +thermalZone.ROM.volMoiAir.dynBal.mC[1] +thermalZone.ROM.volMoiAir.dynBal.medium.Xi[1] +thermalZone.ROM.volMoiAir.dynBal.U +thermalZone.ventCont.dEMA.ExpAVG.x[1] +thermalZone.ventCont.dEMA.ExpAVG1.x[1] +Finished +Finished + = true + + +Declaring variable: Boolean rScript ; + +savelog("AixLib.Systems.ModularAHU.Examples.DemandControlledAHU.translation.log"); = true + + +rCheck = checkModel("AixLib.Systems.ModularAHU.Validation.AHU2_Preheater"); +Check of AixLib.Systems.ModularAHU.Validation.AHU2_Preheater +The model has the same number of unknowns and equations: 2556 +The model could not be deduced to be symbolically well-posed. +The model has + 2471+max([size(combiTimeTable.columns, 1); size(combiTimeTable.offset, 1)])+ registerModule.hydraulicModule.valve.vol.dynBal.nPorts+registerModule.hydraulicModule.pipe1.plugFlowPipe.vol_b.dynBal.nPorts +registerModule.hydraulicModule.pipe1.plugFlowPipe.vol_a.dynBal.nPorts+ registerModule.hydraulicModule.pipe2.plugFlowPipe.vol_b.dynBal.nPorts+ registerModule.hydraulicModule.pipe2.plugFlowPipe.vol_a.dynBal.nPorts+ registerModule.hydraulicModule.pipe3.plugFlowPipe.vol_b.dynBal.nPorts+ registerModule.hydraulicModule.pipe3.plugFlowPipe.vol_a.dynBal.nPorts+ registerModule.hydraulicModule.pipe4.plugFlowPipe.vol_b.dynBal.nPorts+ registerModule.hydraulicModule.pipe4.plugFlowPipe.vol_a.dynBal.nPorts+ registerModule.hydraulicModule.pipe5.plugFlowPipe.vol_b.dynBal.nPorts+ registerModule.hydraulicModule.pipe5.plugFlowPipe.vol_a.dynBal.nPorts+ registerModule.hydraulicModule.pipe6.plugFlowPipe.vol_b.dynBal.nPorts+ registerModule.hydraulicModule.pipe6.plugFlowPipe.vol_a.dynBal.nPorts+ registerModule.hydraulicModule.junc456.dynBal.nPorts+2*size(registerModule.hydraulicModule.PumpInterface.physics.maxMinTable.columns, 1)+2*registerModule.hydraulicModule.PumpInterface.physics.deMultiplex2.n1+2* registerModule.hydraulicModule.PumpInterface.physics.deMultiplex2.n2+ registerModule.hydraulicModule.PumpInterface.physics.criticalDamping.n+ registerModule.hydraulicModule.PumpInterface.physics.vol.dynBal.nPorts+2* registerModule.dynamicHX.vol1[1].dynBal.nPorts+2*registerModule.dynamicHX.vol1[2].dynBal.nPorts +2*registerModule.dynamicHX.vol1[3].dynBal.nPorts+2*registerModule.dynamicHX.vol1[4].dynBal.nPorts +2*registerModule.dynamicHX.vol1[5].dynBal.nPorts+registerModule.dynamicHX.vol2[1].dynBal.nPorts +registerModule.dynamicHX.vol2[2].dynBal.nPorts+registerModule.dynamicHX.vol2[3].dynBal.nPorts +registerModule.dynamicHX.vol2[4].dynBal.nPorts+registerModule.dynamicHX.vol2[5].dynBal.nPorts +scalar unknowns and + 2311+(if boundaryWaterSource.use_Xi_in then 1 else (if boundaryWaterSource.use_X_in then 0 else 1))+(if not boundaryWaterSource.use_p_in then 1 else 0)+2* boundaryWaterSource.nPorts+(if not boundaryWaterSource.use_T_in then 1 else 0) +(if boundaryWaterSink.use_Xi_in then 1 else (if boundaryWaterSink.use_X_in then 0 else 1))+(if not boundaryWaterSink.use_p_in then 1 else 0)+2* boundaryWaterSink.nPorts+(if not boundaryWaterSink.use_T_in then 1 else 0)+( if boundaryAirSource.use_Xi_in then 2 else (if boundaryAirSource.use_X_in then 1 else 3))+3*boundaryAirSource.nPorts+(if not boundaryAirSource.use_m_flow_in then 1 else 0)+(if not boundaryAirSource.use_T_in then 1 else 0)+(if boundaryAirSink.use_Xi_in then 2 else (if boundaryAirSink.use_X_in then 1 else 3))+3*boundaryAirSink.nPorts+(if not boundaryAirSink.use_p_in then 1 else 0)+(if not boundaryAirSink.use_T_in then 1 else 0)+max([size( combiTimeTable.columns, 1); size(combiTimeTable.offset, 1)])+2*size( registerModule.hydraulicModule.PumpInterface.physics.maxMinTable.columns, 1)+ registerModule.hydraulicModule.PumpInterface.physics.deMultiplex2.n1+ registerModule.hydraulicModule.PumpInterface.physics.deMultiplex2.n2+ registerModule.hydraulicModule.PumpInterface.physics.criticalDamping.n+(if not registerModule.hydraulicModule.pipe1.plugFlowPipe.vol_b.dynBal.use_mWat_flow then 1 else 0)+3*registerModule.hydraulicModule.pipe1.plugFlowPipe.vol_b.dynBal.nPorts +(if not registerModule.hydraulicModule.pipe1.plugFlowPipe.vol_a.dynBal.use_mWat_flow then 1 else 0)+3*registerModule.hydraulicModule.pipe1.plugFlowPipe.vol_a.dynBal.nPorts +(if not registerModule.hydraulicModule.pipe2.plugFlowPipe.vol_b.dynBal.use_mWat_flow then 1 else 0)+3*registerModule.hydraulicModule.pipe2.plugFlowPipe.vol_b.dynBal.nPorts +(if not registerModule.hydraulicModule.pipe2.plugFlowPipe.vol_a.dynBal.use_mWat_flow then 1 else 0)+3*registerModule.hydraulicModule.pipe2.plugFlowPipe.vol_a.dynBal.nPorts +(if not registerModule.hydraulicModule.pipe3.plugFlowPipe.vol_b.dynBal.use_mWat_flow then 1 else 0)+3*registerModule.hydraulicModule.pipe3.plugFlowPipe.vol_b.dynBal.nPorts +(if not registerModule.hydraulicModule.pipe3.plugFlowPipe.vol_a.dynBal.use_mWat_flow then 1 else 0)+3*registerModule.hydraulicModule.pipe3.plugFlowPipe.vol_a.dynBal.nPorts +(if not registerModule.hydraulicModule.pipe4.plugFlowPipe.vol_b.dynBal.use_mWat_flow then 1 else 0)+3*registerModule.hydraulicModule.pipe4.plugFlowPipe.vol_b.dynBal.nPorts +(if not registerModule.hydraulicModule.pipe4.plugFlowPipe.vol_a.dynBal.use_mWat_flow then 1 else 0)+3*registerModule.hydraulicModule.pipe4.plugFlowPipe.vol_a.dynBal.nPorts +(if not registerModule.hydraulicModule.pipe5.plugFlowPipe.vol_b.dynBal.use_mWat_flow then 1 else 0)+3*registerModule.hydraulicModule.pipe5.plugFlowPipe.vol_b.dynBal.nPorts +(if not registerModule.hydraulicModule.pipe5.plugFlowPipe.vol_a.dynBal.use_mWat_flow then 1 else 0)+3*registerModule.hydraulicModule.pipe5.plugFlowPipe.vol_a.dynBal.nPorts +(if not registerModule.hydraulicModule.pipe6.plugFlowPipe.vol_b.dynBal.use_mWat_flow then 1 else 0)+3*registerModule.hydraulicModule.pipe6.plugFlowPipe.vol_b.dynBal.nPorts +(if not registerModule.hydraulicModule.pipe6.plugFlowPipe.vol_a.dynBal.use_mWat_flow then 1 else 0)+3*registerModule.hydraulicModule.pipe6.plugFlowPipe.vol_a.dynBal.nPorts +(if not registerModule.hydraulicModule.junc456.dynBal.use_mWat_flow then 1 else 0)+3*registerModule.hydraulicModule.junc456.dynBal.nPorts+(if not registerModule.hydraulicModule.PumpInterface.physics.vol.dynBal.use_mWat_flow then 1 else 0)+3*registerModule.hydraulicModule.PumpInterface.physics.vol.dynBal.nPorts +(if not registerModule.dynamicHX.vol1[1].dynBal.use_mWat_flow then 1 else 0) +5*registerModule.dynamicHX.vol1[1].dynBal.nPorts+(if not registerModule.dynamicHX.vol1[2].dynBal.use_mWat_flow then 1 else 0)+5*registerModule.dynamicHX.vol1[2].dynBal.nPorts+(if not registerModule.dynamicHX.vol1[3].dynBal.use_mWat_flow then 1 else 0)+5* registerModule.dynamicHX.vol1[3].dynBal.nPorts+(if not registerModule.dynamicHX.vol1[4].dynBal.use_mWat_flow then 1 else 0)+5*registerModule.dynamicHX.vol1[4].dynBal.nPorts+(if not registerModule.dynamicHX.vol1[5].dynBal.use_mWat_flow then 1 else 0)+5* registerModule.dynamicHX.vol1[5].dynBal.nPorts+(if not registerModule.dynamicHX.vol2[1].dynBal.use_mWat_flow then 1 else 0)+3*registerModule.dynamicHX.vol2[1].dynBal.nPorts+(if not registerModule.dynamicHX.vol2[2].dynBal.use_mWat_flow then 1 else 0)+3* registerModule.dynamicHX.vol2[2].dynBal.nPorts+(if not registerModule.dynamicHX.vol2[3].dynBal.use_mWat_flow then 1 else 0)+3*registerModule.dynamicHX.vol2[3].dynBal.nPorts+(if not registerModule.dynamicHX.vol2[4].dynBal.use_mWat_flow then 1 else 0)+3* registerModule.dynamicHX.vol2[4].dynBal.nPorts+(if not registerModule.dynamicHX.vol2[5].dynBal.use_mWat_flow then 1 else 0)+3*registerModule.dynamicHX.vol2[5].dynBal.nPorts+(if not registerModule.hydraulicModule.valve.vol.dynBal.use_mWat_flow then 1 else 0)+3 *registerModule.hydraulicModule.valve.vol.dynBal.nPorts +scalar equations. +However, exploiting the given numerical settings of parameters gives the same number of unknowns and equations: + 2556 +Check of AixLib.Systems.ModularAHU.Validation.AHU2_Preheater successful. +Declaring variable: Boolean rCheck ; + +Modelica.Utilities.Streams.print(" { \"file\" : \"AixLib/Resources/Scripts/Dymola/Systems/ModularAHU/Validation/AHU2_Preheater.mos\",", "AixLib.Systems.ModularAHU.Validation.AHU2_Preheater.statistics.log"); +Modelica.Utilities.Streams.print(" \"model\" : \"AixLib.Systems.ModularAHU.Validation.AHU2_Preheater\",", "AixLib.Systems.ModularAHU.Validation.AHU2_Preheater.statistics.log"); +Modelica.Utilities.Streams.print(" \"check\" : {", "AixLib.Systems.ModularAHU.Validation.AHU2_Preheater.statistics.log"); +Modelica.Utilities.Streams.print(" \"command\" : \"checkModel(\\\"AixLib.Systems.ModularAHU.Validation.AHU2_Preheater\\\");\",", "AixLib.Systems.ModularAHU.Validation.AHU2_Preheater.statistics.log"); +Modelica.Utilities.Streams.print(" \"result\" : " + String(rCheck), "AixLib.Systems.ModularAHU.Validation.AHU2_Preheater.statistics.log"); +Modelica.Utilities.Streams.print(" },", "AixLib.Systems.ModularAHU.Validation.AHU2_Preheater.statistics.log"); + + +rScript=RunScript("modelica://AixLib/Resources/Scripts/Dymola/Systems/ModularAHU/Validation/AHU2_Preheater.mos"); +simulateModel("AixLib.Systems.ModularAHU.Validation.AHU2_Preheater", tolerance=1e-6, outputInterval=1, stopTime=7200, resultFile="AixLib.Systems.ModularAHU.Validation.AHU2_Preheater"); +Translation of AixLib.Systems.ModularAHU.Validation.AHU2_Preheater +The DAE has 2556 scalar unknowns and 2556 scalar equations. + +Statistics + +Original Model + Number of components: 487 + Variables: 6441 + Constants: 133 (133 scalars) + Parameters: 2896 (27364 scalars) + Unknowns: 3412 (2665 scalars) + Differentiated variables: 92 scalars + Equations: 2638 + Nontrivial: 2035 +Translated Model + Constants: 2197 scalars + Free parameters: 17980 scalars + Parameter depending: 7652 scalars + Outputs: 17 scalars + Continuous time states: 66 scalars + Time-varying variables: 665 scalars + Alias variables: 1668 scalars + Number of mixed real/discrete systems of equations: 0 + Sizes of linear systems of equations: {2, 2, 2, 2, 2, 2} + Sizes after manipulation of the linear systems: {0, 0, 0, 0, 0, 0} + Sizes of nonlinear systems of equations: {18, 6, 6, 6, 6, 6, 6} + Sizes after manipulation of the nonlinear systems: {2, 1, 1, 1, 1, 1, 1} + Number of numerical Jacobians: 0 + Initialization problem + Sizes of nonlinear systems of equations: {18, 1} + Sizes after manipulation of the nonlinear systems: {4, 0} + Sizes of simplified homotopy nonlinear systems of equations: {18, 1} + Sizes after manipulation of the simplified homotopy nonlinear systems: {3, 0} + Number of numerical Jacobians: 0 + +Selected continuous time states +Statically selected continuous time states +registerModule.dynamicHX.heatCapacitor[1].T +registerModule.dynamicHX.heatCapacitor[2].T +registerModule.dynamicHX.heatCapacitor[3].T +registerModule.dynamicHX.heatCapacitor[4].T +registerModule.dynamicHX.heatCapacitor[5].T +registerModule.dynamicHX.vol1[1].dynBal.medium.Xi[1] +registerModule.dynamicHX.vol1[1].dynBal.U +registerModule.dynamicHX.vol1[2].dynBal.medium.Xi[1] +registerModule.dynamicHX.vol1[2].dynBal.U +registerModule.dynamicHX.vol1[3].dynBal.medium.Xi[1] +registerModule.dynamicHX.vol1[3].dynBal.U +registerModule.dynamicHX.vol1[4].dynBal.medium.Xi[1] +registerModule.dynamicHX.vol1[4].dynBal.U +registerModule.dynamicHX.vol1[5].dynBal.medium.Xi[1] +registerModule.dynamicHX.vol1[5].dynBal.U +registerModule.dynamicHX.vol2[1].dynBal.U +registerModule.dynamicHX.vol2[2].dynBal.U +registerModule.dynamicHX.vol2[3].dynBal.U +registerModule.dynamicHX.vol2[4].dynBal.U +registerModule.dynamicHX.vol2[5].dynBal.U +registerModule.hydraulicModule.junc456.dynBal.U +registerModule.hydraulicModule.pipe1.Insulation.CylindricLoad1.heatCapacitor.T +registerModule.hydraulicModule.pipe1.plugFlowPipe.del.x +registerModule.hydraulicModule.pipe1.plugFlowPipe.timDel.x +registerModule.hydraulicModule.pipe1.plugFlowPipe.vol_a.dynBal.U +registerModule.hydraulicModule.pipe1.plugFlowPipe.vol_b.dynBal.U +registerModule.hydraulicModule.pipe2.Insulation.CylindricLoad1.heatCapacitor.T +registerModule.hydraulicModule.pipe2.plugFlowPipe.del.x +registerModule.hydraulicModule.pipe2.plugFlowPipe.timDel.x +registerModule.hydraulicModule.pipe2.plugFlowPipe.vol_a.dynBal.U +registerModule.hydraulicModule.pipe2.plugFlowPipe.vol_b.dynBal.U +registerModule.hydraulicModule.pipe3.Insulation.CylindricLoad1.heatCapacitor.T +registerModule.hydraulicModule.pipe3.plugFlowPipe.del.x +registerModule.hydraulicModule.pipe3.plugFlowPipe.timDel.x +registerModule.hydraulicModule.pipe3.plugFlowPipe.vol_a.dynBal.U +registerModule.hydraulicModule.pipe3.plugFlowPipe.vol_b.dynBal.U +registerModule.hydraulicModule.pipe4.Insulation.CylindricLoad1.heatCapacitor.T +registerModule.hydraulicModule.pipe4.plugFlowPipe.del.x +registerModule.hydraulicModule.pipe4.plugFlowPipe.timDel.x +registerModule.hydraulicModule.pipe4.plugFlowPipe.vol_a.dynBal.U +registerModule.hydraulicModule.pipe4.plugFlowPipe.vol_b.dynBal.U +registerModule.hydraulicModule.pipe5.Insulation.CylindricLoad1.heatCapacitor.T +registerModule.hydraulicModule.pipe5.plugFlowPipe.del.x +registerModule.hydraulicModule.pipe5.plugFlowPipe.timDel.x +registerModule.hydraulicModule.pipe5.plugFlowPipe.vol_a.dynBal.U +registerModule.hydraulicModule.pipe5.plugFlowPipe.vol_b.dynBal.U +registerModule.hydraulicModule.pipe6.Insulation.CylindricLoad1.heatCapacitor.T +registerModule.hydraulicModule.pipe6.plugFlowPipe.del.x +registerModule.hydraulicModule.pipe6.plugFlowPipe.timDel.x +registerModule.hydraulicModule.pipe6.plugFlowPipe.vol_a.dynBal.U +registerModule.hydraulicModule.pipe6.plugFlowPipe.vol_b.dynBal.U +registerModule.hydraulicModule.PT1_a1.y +registerModule.hydraulicModule.PT1_a2.y +registerModule.hydraulicModule.PT1_b1.y +registerModule.hydraulicModule.PT1_b2.y +registerModule.hydraulicModule.PumpInterface.physics.criticalDamping.x[1] +registerModule.hydraulicModule.PumpInterface.physics.criticalDamping.x[2] +registerModule.hydraulicModule.senT_a1.T +registerModule.hydraulicModule.senT_a2.T +registerModule.hydraulicModule.senT_b1.T +registerModule.hydraulicModule.senT_b2.T +registerModule.hydraulicModule.valve.vol.dynBal.U +registerModule.PT1_airIn.y +registerModule.PT1_airOut.y +registerModule.senT_airIn.T +registerModule.senT_airOut.T +Finished +Finished + = true + +Declaring variable: Boolean rScript ; + +savelog("AixLib.Systems.ModularAHU.Validation.AHU2_Preheater.translation.log"); = true + + +rCheck = checkModel("AixLib.Systems.HydraulicModules.Example.Admix"); +Check of AixLib.Systems.HydraulicModules.Example.Admix +The model has the same number of unknowns and equations: 2088 +The model could not be deduced to be symbolically well-posed. +The model has + 2044+Admix.valve.vol.dynBal.nPorts+Admix.pipe1.simplePipe.vol[1].dynBal.nPorts+ Admix.pipe1.simplePipe.vol[2].dynBal.nPorts+Admix.pipe1.simplePipe.vol[3].dynBal.nPorts +Admix.pipe2.simplePipe.vol[1].dynBal.nPorts+Admix.pipe2.simplePipe.vol[2].dynBal.nPorts +Admix.pipe2.simplePipe.vol[3].dynBal.nPorts+Admix.pipe3.simplePipe.vol[1].dynBal.nPorts +Admix.pipe3.simplePipe.vol[2].dynBal.nPorts+Admix.pipe3.simplePipe.vol[3].dynBal.nPorts +Admix.pipe4.simplePipe.vol[1].dynBal.nPorts+Admix.pipe4.simplePipe.vol[2].dynBal.nPorts +Admix.pipe4.simplePipe.vol[3].dynBal.nPorts+Admix.pipe5.simplePipe.vol[1].dynBal.nPorts +Admix.pipe5.simplePipe.vol[2].dynBal.nPorts+Admix.pipe5.simplePipe.vol[3].dynBal.nPorts +Admix.pipe6.simplePipe.vol[1].dynBal.nPorts+Admix.pipe6.simplePipe.vol[2].dynBal.nPorts +Admix.pipe6.simplePipe.vol[3].dynBal.nPorts+Admix.junc456.dynBal.nPorts+ Admix.PumpInterface.pump.vol.dynBal.nPorts +scalar unknowns and + 1925+(if boundary.use_Xi_in then 1 else (if boundary.use_X_in then 0 else 1))+( if not boundary.use_p_in then 1 else 0)+2*boundary.nPorts+(if not boundary.use_T_in then 1 else 0)+(if boundary1.use_Xi_in then 1 else (if boundary1.use_X_in then 0 else 1))+(if not boundary1.use_p_in then 1 else 0)+2 *boundary1.nPorts+(if not boundary1.use_T_in then 1 else 0)+(if not Admix.pipe1.simplePipe.vol[1].dynBal.use_mWat_flow then 1 else 0)+3* Admix.pipe1.simplePipe.vol[1].dynBal.nPorts+(if not Admix.pipe1.simplePipe.vol[2].dynBal.use_mWat_flow then 1 else 0)+3*Admix.pipe1.simplePipe.vol[2].dynBal.nPorts+(if not Admix.pipe1.simplePipe.vol[3].dynBal.use_mWat_flow then 1 else 0)+3* Admix.pipe1.simplePipe.vol[3].dynBal.nPorts+(if not Admix.pipe2.simplePipe.vol[1].dynBal.use_mWat_flow then 1 else 0)+3*Admix.pipe2.simplePipe.vol[1].dynBal.nPorts+(if not Admix.pipe2.simplePipe.vol[2].dynBal.use_mWat_flow then 1 else 0)+3* Admix.pipe2.simplePipe.vol[2].dynBal.nPorts+(if not Admix.pipe2.simplePipe.vol[3].dynBal.use_mWat_flow then 1 else 0)+3*Admix.pipe2.simplePipe.vol[3].dynBal.nPorts+(if not Admix.pipe3.simplePipe.vol[1].dynBal.use_mWat_flow then 1 else 0)+3* Admix.pipe3.simplePipe.vol[1].dynBal.nPorts+(if not Admix.pipe3.simplePipe.vol[2].dynBal.use_mWat_flow then 1 else 0)+3*Admix.pipe3.simplePipe.vol[2].dynBal.nPorts+(if not Admix.pipe3.simplePipe.vol[3].dynBal.use_mWat_flow then 1 else 0)+3* Admix.pipe3.simplePipe.vol[3].dynBal.nPorts+(if not Admix.pipe4.simplePipe.vol[1].dynBal.use_mWat_flow then 1 else 0)+3*Admix.pipe4.simplePipe.vol[1].dynBal.nPorts+(if not Admix.pipe4.simplePipe.vol[2].dynBal.use_mWat_flow then 1 else 0)+3* Admix.pipe4.simplePipe.vol[2].dynBal.nPorts+(if not Admix.pipe4.simplePipe.vol[3].dynBal.use_mWat_flow then 1 else 0)+3*Admix.pipe4.simplePipe.vol[3].dynBal.nPorts+(if not Admix.pipe5.simplePipe.vol[1].dynBal.use_mWat_flow then 1 else 0)+3* Admix.pipe5.simplePipe.vol[1].dynBal.nPorts+(if not Admix.pipe5.simplePipe.vol[2].dynBal.use_mWat_flow then 1 else 0)+3*Admix.pipe5.simplePipe.vol[2].dynBal.nPorts+(if not Admix.pipe5.simplePipe.vol[3].dynBal.use_mWat_flow then 1 else 0)+3* Admix.pipe5.simplePipe.vol[3].dynBal.nPorts+(if not Admix.pipe6.simplePipe.vol[1].dynBal.use_mWat_flow then 1 else 0)+3*Admix.pipe6.simplePipe.vol[1].dynBal.nPorts+(if not Admix.pipe6.simplePipe.vol[2].dynBal.use_mWat_flow then 1 else 0)+3* Admix.pipe6.simplePipe.vol[2].dynBal.nPorts+(if not Admix.pipe6.simplePipe.vol[3].dynBal.use_mWat_flow then 1 else 0)+3*Admix.pipe6.simplePipe.vol[3].dynBal.nPorts+(if not Admix.junc456.dynBal.use_mWat_flow then 1 else 0)+3*Admix.junc456.dynBal.nPorts +(if not Admix.PumpInterface.pump.vol.dynBal.use_mWat_flow then 1 else 0)+3* Admix.PumpInterface.pump.vol.dynBal.nPorts+(if not Admix.valve.vol.dynBal.use_mWat_flow then 1 else 0)+3*Admix.valve.vol.dynBal.nPorts +scalar equations. +However, exploiting the given numerical settings of parameters gives the same number of unknowns and equations: + 2088 +Check of AixLib.Systems.HydraulicModules.Example.Admix successful. +Declaring variable: Boolean rCheck ; + +Modelica.Utilities.Streams.print(" { \"file\" : \"AixLib/Resources/Scripts/Dymola/Systems/HydraulicModules/Examples/Admix.mos\",", "AixLib.Systems.HydraulicModules.Example.Admix.statistics.log"); +Modelica.Utilities.Streams.print(" \"model\" : \"AixLib.Systems.HydraulicModules.Example.Admix\",", "AixLib.Systems.HydraulicModules.Example.Admix.statistics.log"); +Modelica.Utilities.Streams.print(" \"check\" : {", "AixLib.Systems.HydraulicModules.Example.Admix.statistics.log"); +Modelica.Utilities.Streams.print(" \"command\" : \"checkModel(\\\"AixLib.Systems.HydraulicModules.Example.Admix\\\");\",", "AixLib.Systems.HydraulicModules.Example.Admix.statistics.log"); +Modelica.Utilities.Streams.print(" \"result\" : " + String(rCheck), "AixLib.Systems.HydraulicModules.Example.Admix.statistics.log"); +Modelica.Utilities.Streams.print(" },", "AixLib.Systems.HydraulicModules.Example.Admix.statistics.log"); + + +rScript=RunScript("modelica://AixLib/Resources/Scripts/Dymola/Systems/HydraulicModules/Examples/Admix.mos"); +simulateModel("AixLib.Systems.HydraulicModules.Example.Admix", tolerance=1e-6, stopTime=800, resultFile="AixLib.Systems.HydraulicModules.Example.Admix"); +Translation of AixLib.Systems.HydraulicModules.Example.Admix +The DAE has 2088 scalar unknowns and 2088 scalar equations. + +Statistics + +Original Model + Number of components: 467 + Variables: 5670 + Constants: 111 (111 scalars) + Parameters: 2755 (2949 scalars) + Unknowns: 2804 (2171 scalars) + Differentiated variables: 77 scalars + Equations: 2056 + Nontrivial: 1589 +Translated Model + Constants: 2081 scalars + Free parameters: 168 scalars + Parameter depending: 1054 scalars + Outputs: 12 scalars + Continuous time states: 56 scalars + Time-varying variables: 471 scalars + Alias variables: 1457 scalars + Number of mixed real/discrete systems of equations: 0 + Sizes of linear systems of equations: {5, 2, 5, 2, 5, 2, 5, 2, 5, 2, 5, 2} + Sizes after manipulation of the linear systems: {0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0} + Sizes of nonlinear systems of equations: {21} + Sizes after manipulation of the nonlinear systems: {2} + Number of numerical Jacobians: 0 + Initialization problem + Sizes of nonlinear systems of equations: {21, 1} + Sizes after manipulation of the nonlinear systems: {4, 0} + Sizes of simplified homotopy nonlinear systems of equations: {21, 1} + Sizes after manipulation of the simplified homotopy nonlinear systems: {3, 0} + Number of numerical Jacobians: 0 + +Selected continuous time states +Statically selected continuous time states +Admix.junc456.dynBal.U +Admix.pipe1.Insulation.CylindricLoad1.heatCapacitor.T +Admix.pipe1.simplePipe.PipeWall[1].CylindricLoad1.heatCapacitor.T +Admix.pipe1.simplePipe.PipeWall[2].CylindricLoad1.heatCapacitor.T +Admix.pipe1.simplePipe.PipeWall[3].CylindricLoad1.heatCapacitor.T +Admix.pipe1.simplePipe.vol[1].dynBal.U +Admix.pipe1.simplePipe.vol[2].dynBal.U +Admix.pipe1.simplePipe.vol[3].dynBal.U +Admix.pipe2.Insulation.CylindricLoad1.heatCapacitor.T +Admix.pipe2.simplePipe.PipeWall[1].CylindricLoad1.heatCapacitor.T +Admix.pipe2.simplePipe.PipeWall[2].CylindricLoad1.heatCapacitor.T +Admix.pipe2.simplePipe.PipeWall[3].CylindricLoad1.heatCapacitor.T +Admix.pipe2.simplePipe.vol[1].dynBal.U +Admix.pipe2.simplePipe.vol[2].dynBal.U +Admix.pipe2.simplePipe.vol[3].dynBal.U +Admix.pipe3.Insulation.CylindricLoad1.heatCapacitor.T +Admix.pipe3.simplePipe.PipeWall[1].CylindricLoad1.heatCapacitor.T +Admix.pipe3.simplePipe.PipeWall[2].CylindricLoad1.heatCapacitor.T +Admix.pipe3.simplePipe.PipeWall[3].CylindricLoad1.heatCapacitor.T +Admix.pipe3.simplePipe.vol[1].dynBal.U +Admix.pipe3.simplePipe.vol[2].dynBal.U +Admix.pipe3.simplePipe.vol[3].dynBal.U +Admix.pipe4.Insulation.CylindricLoad1.heatCapacitor.T +Admix.pipe4.simplePipe.PipeWall[1].CylindricLoad1.heatCapacitor.T +Admix.pipe4.simplePipe.PipeWall[2].CylindricLoad1.heatCapacitor.T +Admix.pipe4.simplePipe.PipeWall[3].CylindricLoad1.heatCapacitor.T +Admix.pipe4.simplePipe.vol[1].dynBal.U +Admix.pipe4.simplePipe.vol[2].dynBal.U +Admix.pipe4.simplePipe.vol[3].dynBal.U +Admix.pipe5.Insulation.CylindricLoad1.heatCapacitor.T +Admix.pipe5.simplePipe.PipeWall[1].CylindricLoad1.heatCapacitor.T +Admix.pipe5.simplePipe.PipeWall[2].CylindricLoad1.heatCapacitor.T +Admix.pipe5.simplePipe.PipeWall[3].CylindricLoad1.heatCapacitor.T +Admix.pipe5.simplePipe.vol[1].dynBal.U +Admix.pipe5.simplePipe.vol[2].dynBal.U +Admix.pipe5.simplePipe.vol[3].dynBal.U +Admix.pipe6.Insulation.CylindricLoad1.heatCapacitor.T +Admix.pipe6.simplePipe.PipeWall[1].CylindricLoad1.heatCapacitor.T +Admix.pipe6.simplePipe.PipeWall[2].CylindricLoad1.heatCapacitor.T +Admix.pipe6.simplePipe.PipeWall[3].CylindricLoad1.heatCapacitor.T +Admix.pipe6.simplePipe.vol[1].dynBal.U +Admix.pipe6.simplePipe.vol[2].dynBal.U +Admix.pipe6.simplePipe.vol[3].dynBal.U +Admix.PT1_a1.y +Admix.PT1_a2.y +Admix.PT1_b1.y +Admix.PT1_b2.y +Admix.PumpInterface.pump.filter.s[1] +Admix.PumpInterface.pump.filter.s[2] +Admix.PumpInterface.pump.vol.dynBal.U +Admix.senT_a1.T +Admix.senT_a2.T +Admix.senT_b1.T +Admix.senT_b2.T +Admix.valve.filter.s[1] +Admix.valve.vol.dynBal.U +Finished +Finished + = true + + +Declaring variable: Boolean rScript ; + +savelog("AixLib.Systems.HydraulicModules.Example.Admix.translation.log"); = true + + +rCheck = checkModel("AixLib.Systems.ModularEnergySystems.ModularBoiler.Examples.ModularBoilerFeedback"); +Check of AixLib.Systems.ModularEnergySystems.ModularBoiler.Examples.ModularBoilerFeedback +The model has the same number of unknowns and equations: 745 +The model could not be deduced to be symbolically well-posed. +The model has + 712+modularBoiler.boilerGeneric.vol.dynBal.nPorts+2*modularBoiler.boilerGeneric.offDesignOperation.multiplex4.n1 +2*modularBoiler.boilerGeneric.offDesignOperation.multiplex4.n2+2* modularBoiler.boilerGeneric.offDesignOperation.multiplex4.n3+2* modularBoiler.boilerGeneric.offDesignOperation.multiplex4.n4+modularBoiler.boilerGeneric.offDesignOperation.boilerEffciency.nin +2*modularBoiler.boilerGeneric.designOperation.multiplex4.n1+2* modularBoiler.boilerGeneric.designOperation.multiplex4.n2+2*modularBoiler.boilerGeneric.designOperation.multiplex4.n3 +2*modularBoiler.boilerGeneric.designOperation.multiplex4.n4+modularBoiler.boilerGeneric.designOperation.boilerEffciency.nin +modularBoiler.pump.vol.dynBal.nPorts+modularBoiler.val.vol.dynBal.nPorts+ vol.dynBal.nPorts +scalar unknowns and + 693+2*(modularBoiler.boilerGeneric.offDesignOperation.multiplex4.n1+ modularBoiler.boilerGeneric.offDesignOperation.multiplex4.n2+modularBoiler.boilerGeneric.offDesignOperation.multiplex4.n3 +modularBoiler.boilerGeneric.offDesignOperation.multiplex4.n4+modularBoiler.boilerGeneric.designOperation.multiplex4.n1 +modularBoiler.boilerGeneric.designOperation.multiplex4.n2+modularBoiler.boilerGeneric.designOperation.multiplex4.n3 +modularBoiler.boilerGeneric.designOperation.multiplex4.n4)+(if bou.use_Xi_in then 1 else (if bou.use_X_in then 0 else 1))+(if not bou.use_p_in then 1 else 0)+2*bou.nPorts+(if not bou.use_T_in then 1 else 0)+(if not modularBoiler.boilerGeneric.vol.dynBal.use_mWat_flow then 1 else 0)+3* modularBoiler.boilerGeneric.vol.dynBal.nPorts+(if not modularBoiler.pump.vol.dynBal.use_mWat_flow then 1 else 0)+3*modularBoiler.pump.vol.dynBal.nPorts+(if not vol.dynBal.use_mWat_flow then 1 else 0)+3*vol.dynBal.nPorts+(if not modularBoiler.val.vol.dynBal.use_mWat_flow then 1 else 0)+3*modularBoiler.val.vol.dynBal.nPorts +scalar equations. +However, exploiting the given numerical settings of parameters gives the same number of unknowns and equations: + 745 +Check of AixLib.Systems.ModularEnergySystems.ModularBoiler.Examples.ModularBoilerFeedback successful. +Declaring variable: Boolean rCheck ; + +Modelica.Utilities.Streams.print(" { \"file\" : \"AixLib/Resources/Scripts/Dymola/Systems/ModularEnergySystems/Examples/ModularBoilerFeedback.mos\",", "AixLib.Systems.ModularEnergySystems.ModularBoiler.Examples.ModularBoilerFeedback.statistics.log"); +Modelica.Utilities.Streams.print(" \"model\" : \"AixLib.Systems.ModularEnergySystems.ModularBoiler.Examples.ModularBoilerFeedback\",", "AixLib.Systems.ModularEnergySystems.ModularBoiler.Examples.ModularBoilerFeedback.statistics.log"); +Modelica.Utilities.Streams.print(" \"check\" : {", "AixLib.Systems.ModularEnergySystems.ModularBoiler.Examples.ModularBoilerFeedback.statistics.log"); +Modelica.Utilities.Streams.print(" \"command\" : \"checkModel(\\\"AixLib.Systems.ModularEnergySystems.ModularBoiler.Examples.ModularBoilerFeedback\\\");\",", "AixLib.Systems.ModularEnergySystems.ModularBoiler.Examples.ModularBoilerFeedback.statistics.log"); +Modelica.Utilities.Streams.print(" \"result\" : " + String(rCheck), "AixLib.Systems.ModularEnergySystems.ModularBoiler.Examples.ModularBoilerFeedback.statistics.log"); +Modelica.Utilities.Streams.print(" },", "AixLib.Systems.ModularEnergySystems.ModularBoiler.Examples.ModularBoilerFeedback.statistics.log"); + + +rScript=RunScript("modelica://AixLib/Resources/Scripts/Dymola/Systems/ModularEnergySystems/Examples/ModularBoilerFeedback.mos"); +simulateModel("AixLib.Systems.ModularEnergySystems.ModularBoiler.Examples.ModularBoilerFeedback", tolerance=1e-06, stopTime=20000, method="dassl", resultFile="AixLib.Systems.ModularEnergySystems.ModularBoiler.Examples.ModularBoilerFeedback"); +Translation of AixLib.Systems.ModularEnergySystems.ModularBoiler.Examples.ModularBoilerFeedback +The DAE has 745 scalar unknowns and 745 scalar equations. + +Statistics + +Original Model + Number of components: 192 + Variables: 1742 + Constants: 29 (29 scalars) + Parameters: 856 (976 scalars) + Unknowns: 857 (771 scalars) + Differentiated variables: 18 scalars + Equations: 759 + Nontrivial: 630 +Translated Model + Constants: 559 scalars + Free parameters: 171 scalars + Parameter depending: 360 scalars + Outputs: 11 scalars + Continuous time states: 13 scalars + Time-varying variables: 195 scalars + Alias variables: 491 scalars + Number of mixed real/discrete systems of equations: 0 + Sizes of linear systems of equations: {4} + Sizes after manipulation of the linear systems: {0} + Sizes of nonlinear systems of equations: {10} + Sizes after manipulation of the nonlinear systems: {2} + Number of numerical Jacobians: 0 + Initialization problem + Sizes of nonlinear systems of equations: {10} + Sizes after manipulation of the nonlinear systems: {1} + Number of numerical Jacobians: 0 + +Selected continuous time states +Statically selected continuous time states +modularBoiler.boilerControl.feedbackControl.PIValve.I.y +modularBoiler.boilerControl.internalFirRatControl.PID.I.y +modularBoiler.boilerGeneric.senTRet.T +modularBoiler.boilerGeneric.senTSup.T +modularBoiler.boilerGeneric.vol.dynBal.U +modularBoiler.pump.filter.s[1] +modularBoiler.pump.filter.s[2] +modularBoiler.pump.vol.dynBal.U +modularBoiler.senTRet.T +modularBoiler.senTSup.T +modularBoiler.val.vol.dynBal.U +senTRet.T +vol.dynBal.U +Finished +Finished + = true + +Declaring variable: Boolean rScript ; + +savelog("AixLib.Systems.ModularEnergySystems.ModularBoiler.Examples.ModularBoilerFeedback.translation.log"); = true + + +rCheck = checkModel("AixLib.Systems.HydraulicModules.Example.Pump"); +Check of AixLib.Systems.HydraulicModules.Example.Pump +The model has the same number of unknowns and equations: 916 +The model could not be deduced to be symbolically well-posed. +The model has + 902+Unmixed.PumpInterface.pump.vol.dynBal.nPorts+Unmixed.pipe1.plugFlowPipe.vol_b.dynBal.nPorts +Unmixed.pipe1.plugFlowPipe.vol_a.dynBal.nPorts+Unmixed.pipe2.plugFlowPipe.vol_b.dynBal.nPorts +Unmixed.pipe2.plugFlowPipe.vol_a.dynBal.nPorts+Unmixed.pipe3.plugFlowPipe.vol_b.dynBal.nPorts +Unmixed.pipe3.plugFlowPipe.vol_a.dynBal.nPorts +scalar unknowns and + 857+(if boundary.use_Xi_in then 1 else (if boundary.use_X_in then 0 else 1))+( if not boundary.use_p_in then 1 else 0)+2*boundary.nPorts+(if not boundary.use_T_in then 1 else 0)+(if boundary1.use_Xi_in then 1 else (if boundary1.use_X_in then 0 else 1))+(if not boundary1.use_p_in then 1 else 0)+2 *boundary1.nPorts+(if not boundary1.use_T_in then 1 else 0)+(if not Unmixed.PumpInterface.pump.vol.dynBal.use_mWat_flow then 1 else 0)+3* Unmixed.PumpInterface.pump.vol.dynBal.nPorts+(if not Unmixed.pipe1.plugFlowPipe.vol_b.dynBal.use_mWat_flow then 1 else 0)+3*Unmixed.pipe1.plugFlowPipe.vol_b.dynBal.nPorts+(if not Unmixed.pipe1.plugFlowPipe.vol_a.dynBal.use_mWat_flow then 1 else 0)+3* Unmixed.pipe1.plugFlowPipe.vol_a.dynBal.nPorts+(if not Unmixed.pipe2.plugFlowPipe.vol_b.dynBal.use_mWat_flow then 1 else 0)+3*Unmixed.pipe2.plugFlowPipe.vol_b.dynBal.nPorts+(if not Unmixed.pipe2.plugFlowPipe.vol_a.dynBal.use_mWat_flow then 1 else 0)+3* Unmixed.pipe2.plugFlowPipe.vol_a.dynBal.nPorts+(if not Unmixed.pipe3.plugFlowPipe.vol_b.dynBal.use_mWat_flow then 1 else 0)+3*Unmixed.pipe3.plugFlowPipe.vol_b.dynBal.nPorts+(if not Unmixed.pipe3.plugFlowPipe.vol_a.dynBal.use_mWat_flow then 1 else 0)+3* Unmixed.pipe3.plugFlowPipe.vol_a.dynBal.nPorts +scalar equations. +However, exploiting the given numerical settings of parameters gives the same number of unknowns and equations: + 916 +Check of AixLib.Systems.HydraulicModules.Example.Pump successful. +Declaring variable: Boolean rCheck ; + +Modelica.Utilities.Streams.print(" { \"file\" : \"AixLib/Resources/Scripts/Dymola/Systems/HydraulicModules/Examples/Pump.mos\",", "AixLib.Systems.HydraulicModules.Example.Pump.statistics.log"); +Modelica.Utilities.Streams.print(" \"model\" : \"AixLib.Systems.HydraulicModules.Example.Pump\",", "AixLib.Systems.HydraulicModules.Example.Pump.statistics.log"); +Modelica.Utilities.Streams.print(" \"check\" : {", "AixLib.Systems.HydraulicModules.Example.Pump.statistics.log"); +Modelica.Utilities.Streams.print(" \"command\" : \"checkModel(\\\"AixLib.Systems.HydraulicModules.Example.Pump\\\");\",", "AixLib.Systems.HydraulicModules.Example.Pump.statistics.log"); +Modelica.Utilities.Streams.print(" \"result\" : " + String(rCheck), "AixLib.Systems.HydraulicModules.Example.Pump.statistics.log"); +Modelica.Utilities.Streams.print(" },", "AixLib.Systems.HydraulicModules.Example.Pump.statistics.log"); + + +rScript=RunScript("modelica://AixLib/Resources/Scripts/Dymola/Systems/HydraulicModules/Examples/Pump.mos"); +simulateModel("AixLib.Systems.HydraulicModules.Example.Pump", tolerance=1e-6, outputInterval=5, stopTime=800, resultFile="AixLib.Systems.HydraulicModules.Example.Pump"); +Translation of AixLib.Systems.HydraulicModules.Example.Pump +The DAE has 916 scalar unknowns and 916 scalar equations. + +Statistics + +Original Model + Number of components: 195 + Variables: 2528 + Constants: 42 (42 scalars) + Parameters: 1214 (1411 scalars) + Unknowns: 1272 (954 scalars) + Differentiated variables: 33 scalars + Equations: 1018 + Nontrivial: 814 +Translated Model + Constants: 936 scalars + Free parameters: 127 scalars + Parameter depending: 522 scalars + Outputs: 10 scalars + Continuous time states: 26 scalars + Time-varying variables: 227 scalars + Alias variables: 595 scalars + Number of mixed real/discrete systems of equations: 0 + Sizes of linear systems of equations: {2, 2, 2} + Sizes after manipulation of the linear systems: {0, 0, 0} + Sizes of nonlinear systems of equations: {10, 6, 6, 6} + Sizes after manipulation of the nonlinear systems: {1, 1, 1, 1} + Number of numerical Jacobians: 0 + Initialization problem + Sizes of nonlinear systems of equations: {10, 1} + Sizes after manipulation of the nonlinear systems: {1, 0} + Sizes of simplified homotopy nonlinear systems of equations: {10, 1} + Sizes after manipulation of the simplified homotopy nonlinear systems: {1, 0} + Number of numerical Jacobians: 0 + +Selected continuous time states +Statically selected continuous time states +Unmixed.pipe1.Insulation.CylindricLoad1.heatCapacitor.T +Unmixed.pipe1.plugFlowPipe.del.x +Unmixed.pipe1.plugFlowPipe.timDel.x +Unmixed.pipe1.plugFlowPipe.vol_a.dynBal.U +Unmixed.pipe1.plugFlowPipe.vol_b.dynBal.U +Unmixed.pipe2.Insulation.CylindricLoad1.heatCapacitor.T +Unmixed.pipe2.plugFlowPipe.del.x +Unmixed.pipe2.plugFlowPipe.timDel.x +Unmixed.pipe2.plugFlowPipe.vol_a.dynBal.U +Unmixed.pipe2.plugFlowPipe.vol_b.dynBal.U +Unmixed.pipe3.Insulation.CylindricLoad1.heatCapacitor.T +Unmixed.pipe3.plugFlowPipe.del.x +Unmixed.pipe3.plugFlowPipe.timDel.x +Unmixed.pipe3.plugFlowPipe.vol_a.dynBal.U +Unmixed.pipe3.plugFlowPipe.vol_b.dynBal.U +Unmixed.PT1_a1.y +Unmixed.PT1_a2.y +Unmixed.PT1_b1.y +Unmixed.PT1_b2.y +Unmixed.PumpInterface.pump.filter.s[1] +Unmixed.PumpInterface.pump.filter.s[2] +Unmixed.PumpInterface.pump.vol.dynBal.U +Unmixed.senT_a1.T +Unmixed.senT_a2.T +Unmixed.senT_b1.T +Unmixed.senT_b2.T +Finished +Finished + = true + + +Declaring variable: Boolean rScript ; + +savelog("AixLib.Systems.HydraulicModules.Example.Pump.translation.log"); = true + + +rCheck = checkModel("AixLib.Systems.HydraulicModules.Example.Injection2WayValve"); +Check of AixLib.Systems.HydraulicModules.Example.Injection2WayValve +The model has the same number of unknowns and equations: 2316 +The model could not be deduced to be symbolically well-posed. +The model has + 2266+Injection.PumpInterface.pump.vol.dynBal.nPorts+Injection.pipe1.simplePipe.vol[1].dynBal.nPorts +Injection.pipe1.simplePipe.vol[2].dynBal.nPorts+Injection.pipe1.simplePipe.vol[3].dynBal.nPorts +Injection.pipe2.simplePipe.vol[1].dynBal.nPorts+Injection.pipe2.simplePipe.vol[2].dynBal.nPorts +Injection.pipe2.simplePipe.vol[3].dynBal.nPorts+Injection.pipe3.simplePipe.vol[1].dynBal.nPorts +Injection.pipe3.simplePipe.vol[2].dynBal.nPorts+Injection.pipe3.simplePipe.vol[3].dynBal.nPorts +Injection.pipe4.simplePipe.vol[1].dynBal.nPorts+Injection.pipe4.simplePipe.vol[2].dynBal.nPorts +Injection.pipe4.simplePipe.vol[3].dynBal.nPorts+Injection.pipe5.simplePipe.vol[1].dynBal.nPorts +Injection.pipe5.simplePipe.vol[2].dynBal.nPorts+Injection.pipe5.simplePipe.vol[3].dynBal.nPorts +Injection.pipe6.simplePipe.vol[1].dynBal.nPorts+Injection.pipe6.simplePipe.vol[2].dynBal.nPorts +Injection.pipe6.simplePipe.vol[3].dynBal.nPorts+Injection.pipe7.simplePipe.vol[1].dynBal.nPorts +Injection.pipe7.simplePipe.vol[2].dynBal.nPorts+Injection.pipe7.simplePipe.vol[3].dynBal.nPorts +Injection.junc3v6.dynBal.nPorts+Injection.juncjp6.dynBal.nPorts +scalar unknowns and + 2132+(if boundary.use_Xi_in then 1 else (if boundary.use_X_in then 0 else 1))+( if not boundary.use_p_in then 1 else 0)+2*boundary.nPorts+(if not boundary.use_T_in then 1 else 0)+(if boundary1.use_Xi_in then 1 else (if boundary1.use_X_in then 0 else 1))+(if not boundary1.use_p_in then 1 else 0)+2 *boundary1.nPorts+(if not boundary1.use_T_in then 1 else 0)+(if not Injection.PumpInterface.pump.vol.dynBal.use_mWat_flow then 1 else 0)+3* Injection.PumpInterface.pump.vol.dynBal.nPorts+(if not Injection.pipe1.simplePipe.vol[1].dynBal.use_mWat_flow then 1 else 0)+3*Injection.pipe1.simplePipe.vol[1].dynBal.nPorts+(if not Injection.pipe1.simplePipe.vol[2].dynBal.use_mWat_flow then 1 else 0)+3* Injection.pipe1.simplePipe.vol[2].dynBal.nPorts+(if not Injection.pipe1.simplePipe.vol[3].dynBal.use_mWat_flow then 1 else 0)+3*Injection.pipe1.simplePipe.vol[3].dynBal.nPorts+(if not Injection.pipe2.simplePipe.vol[1].dynBal.use_mWat_flow then 1 else 0)+3* Injection.pipe2.simplePipe.vol[1].dynBal.nPorts+(if not Injection.pipe2.simplePipe.vol[2].dynBal.use_mWat_flow then 1 else 0)+3*Injection.pipe2.simplePipe.vol[2].dynBal.nPorts+(if not Injection.pipe2.simplePipe.vol[3].dynBal.use_mWat_flow then 1 else 0)+3* Injection.pipe2.simplePipe.vol[3].dynBal.nPorts+(if not Injection.pipe3.simplePipe.vol[1].dynBal.use_mWat_flow then 1 else 0)+3*Injection.pipe3.simplePipe.vol[1].dynBal.nPorts+(if not Injection.pipe3.simplePipe.vol[2].dynBal.use_mWat_flow then 1 else 0)+3* Injection.pipe3.simplePipe.vol[2].dynBal.nPorts+(if not Injection.pipe3.simplePipe.vol[3].dynBal.use_mWat_flow then 1 else 0)+3*Injection.pipe3.simplePipe.vol[3].dynBal.nPorts+(if not Injection.pipe4.simplePipe.vol[1].dynBal.use_mWat_flow then 1 else 0)+3* Injection.pipe4.simplePipe.vol[1].dynBal.nPorts+(if not Injection.pipe4.simplePipe.vol[2].dynBal.use_mWat_flow then 1 else 0)+3*Injection.pipe4.simplePipe.vol[2].dynBal.nPorts+(if not Injection.pipe4.simplePipe.vol[3].dynBal.use_mWat_flow then 1 else 0)+3* Injection.pipe4.simplePipe.vol[3].dynBal.nPorts+(if not Injection.pipe5.simplePipe.vol[1].dynBal.use_mWat_flow then 1 else 0)+3*Injection.pipe5.simplePipe.vol[1].dynBal.nPorts+(if not Injection.pipe5.simplePipe.vol[2].dynBal.use_mWat_flow then 1 else 0)+3* Injection.pipe5.simplePipe.vol[2].dynBal.nPorts+(if not Injection.pipe5.simplePipe.vol[3].dynBal.use_mWat_flow then 1 else 0)+3*Injection.pipe5.simplePipe.vol[3].dynBal.nPorts+(if not Injection.pipe6.simplePipe.vol[1].dynBal.use_mWat_flow then 1 else 0)+3* Injection.pipe6.simplePipe.vol[1].dynBal.nPorts+(if not Injection.pipe6.simplePipe.vol[2].dynBal.use_mWat_flow then 1 else 0)+3*Injection.pipe6.simplePipe.vol[2].dynBal.nPorts+(if not Injection.pipe6.simplePipe.vol[3].dynBal.use_mWat_flow then 1 else 0)+3* Injection.pipe6.simplePipe.vol[3].dynBal.nPorts+(if not Injection.pipe7.simplePipe.vol[1].dynBal.use_mWat_flow then 1 else 0)+3*Injection.pipe7.simplePipe.vol[1].dynBal.nPorts+(if not Injection.pipe7.simplePipe.vol[2].dynBal.use_mWat_flow then 1 else 0)+3* Injection.pipe7.simplePipe.vol[2].dynBal.nPorts+(if not Injection.pipe7.simplePipe.vol[3].dynBal.use_mWat_flow then 1 else 0)+3*Injection.pipe7.simplePipe.vol[3].dynBal.nPorts+(if not Injection.junc3v6.dynBal.use_mWat_flow then 1 else 0)+3*Injection.junc3v6.dynBal.nPorts +(if not Injection.juncjp6.dynBal.use_mWat_flow then 1 else 0)+3* Injection.juncjp6.dynBal.nPorts +scalar equations. +However, exploiting the given numerical settings of parameters gives the same number of unknowns and equations: + 2316 +Check of AixLib.Systems.HydraulicModules.Example.Injection2WayValve successful. +Declaring variable: Boolean rCheck ; + +Modelica.Utilities.Streams.print(" { \"file\" : \"AixLib/Resources/Scripts/Dymola/Systems/HydraulicModules/Examples/Injection2WayValve.mos\",", "AixLib.Systems.HydraulicModules.Example.Injection2WayValve.statistics.log"); +Modelica.Utilities.Streams.print(" \"model\" : \"AixLib.Systems.HydraulicModules.Example.Injection2WayValve\",", "AixLib.Systems.HydraulicModules.Example.Injection2WayValve.statistics.log"); +Modelica.Utilities.Streams.print(" \"check\" : {", "AixLib.Systems.HydraulicModules.Example.Injection2WayValve.statistics.log"); +Modelica.Utilities.Streams.print(" \"command\" : \"checkModel(\\\"AixLib.Systems.HydraulicModules.Example.Injection2WayValve\\\");\",", "AixLib.Systems.HydraulicModules.Example.Injection2WayValve.statistics.log"); +Modelica.Utilities.Streams.print(" \"result\" : " + String(rCheck), "AixLib.Systems.HydraulicModules.Example.Injection2WayValve.statistics.log"); +Modelica.Utilities.Streams.print(" },", "AixLib.Systems.HydraulicModules.Example.Injection2WayValve.statistics.log"); + + +rScript=RunScript("modelica://AixLib/Resources/Scripts/Dymola/Systems/HydraulicModules/Examples/Injection2WayValve.mos"); +simulateModel("AixLib.Systems.HydraulicModules.Example.Injection2WayValve", tolerance=1e-6, stopTime=800, resultFile="AixLib.Systems.HydraulicModules.Example.Injection2WayValve"); +Translation of AixLib.Systems.HydraulicModules.Example.Injection2WayValve +The DAE has 2316 scalar unknowns and 2316 scalar equations. + +Statistics + +Original Model + Number of components: 512 + Variables: 6229 + Constants: 121 (121 scalars) + Parameters: 3000 (3117 scalars) + Unknowns: 3108 (2406 scalars) + Differentiated variables: 87 scalars + Equations: 2272 + Nontrivial: 1746 +Translated Model + Constants: 2281 scalars + Free parameters: 149 scalars + Parameter depending: 1075 scalars + Outputs: 12 scalars + Continuous time states: 63 scalars + Time-varying variables: 515 scalars + Alias variables: 1624 scalars + Number of mixed real/discrete systems of equations: 0 + Sizes of linear systems of equations: {5, 2, 5, 2, 5, 2, 5, 2, 5, 2, 5, 2, 5, 2} + Sizes after manipulation of the linear systems: {0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0} + Sizes of nonlinear systems of equations: {21} + Sizes after manipulation of the nonlinear systems: {2} + Number of numerical Jacobians: 0 + Initialization problem + Sizes of nonlinear systems of equations: {21, 1, 1} + Sizes after manipulation of the nonlinear systems: {3, 0, 0} + Sizes of simplified homotopy nonlinear systems of equations: {21, 1, 1} + Sizes after manipulation of the simplified homotopy nonlinear systems: {3, 0, 0} + Number of numerical Jacobians: 0 + +Selected continuous time states +Statically selected continuous time states +Injection.junc3v6.dynBal.U +Injection.juncjp6.dynBal.U +Injection.pipe1.Insulation.CylindricLoad1.heatCapacitor.T +Injection.pipe1.simplePipe.PipeWall[1].CylindricLoad1.heatCapacitor.T +Injection.pipe1.simplePipe.PipeWall[2].CylindricLoad1.heatCapacitor.T +Injection.pipe1.simplePipe.PipeWall[3].CylindricLoad1.heatCapacitor.T +Injection.pipe1.simplePipe.vol[1].dynBal.U +Injection.pipe1.simplePipe.vol[2].dynBal.U +Injection.pipe1.simplePipe.vol[3].dynBal.U +Injection.pipe2.Insulation.CylindricLoad1.heatCapacitor.T +Injection.pipe2.simplePipe.PipeWall[1].CylindricLoad1.heatCapacitor.T +Injection.pipe2.simplePipe.PipeWall[2].CylindricLoad1.heatCapacitor.T +Injection.pipe2.simplePipe.PipeWall[3].CylindricLoad1.heatCapacitor.T +Injection.pipe2.simplePipe.vol[1].dynBal.U +Injection.pipe2.simplePipe.vol[2].dynBal.U +Injection.pipe2.simplePipe.vol[3].dynBal.U +Injection.pipe3.Insulation.CylindricLoad1.heatCapacitor.T +Injection.pipe3.simplePipe.PipeWall[1].CylindricLoad1.heatCapacitor.T +Injection.pipe3.simplePipe.PipeWall[2].CylindricLoad1.heatCapacitor.T +Injection.pipe3.simplePipe.PipeWall[3].CylindricLoad1.heatCapacitor.T +Injection.pipe3.simplePipe.vol[1].dynBal.U +Injection.pipe3.simplePipe.vol[2].dynBal.U +Injection.pipe3.simplePipe.vol[3].dynBal.U +Injection.pipe4.Insulation.CylindricLoad1.heatCapacitor.T +Injection.pipe4.simplePipe.PipeWall[1].CylindricLoad1.heatCapacitor.T +Injection.pipe4.simplePipe.PipeWall[2].CylindricLoad1.heatCapacitor.T +Injection.pipe4.simplePipe.PipeWall[3].CylindricLoad1.heatCapacitor.T +Injection.pipe4.simplePipe.vol[1].dynBal.U +Injection.pipe4.simplePipe.vol[2].dynBal.U +Injection.pipe4.simplePipe.vol[3].dynBal.U +Injection.pipe5.Insulation.CylindricLoad1.heatCapacitor.T +Injection.pipe5.simplePipe.PipeWall[1].CylindricLoad1.heatCapacitor.T +Injection.pipe5.simplePipe.PipeWall[2].CylindricLoad1.heatCapacitor.T +Injection.pipe5.simplePipe.PipeWall[3].CylindricLoad1.heatCapacitor.T +Injection.pipe5.simplePipe.vol[1].dynBal.U +Injection.pipe5.simplePipe.vol[2].dynBal.U +Injection.pipe5.simplePipe.vol[3].dynBal.U +Injection.pipe6.Insulation.CylindricLoad1.heatCapacitor.T +Injection.pipe6.simplePipe.PipeWall[1].CylindricLoad1.heatCapacitor.T +Injection.pipe6.simplePipe.PipeWall[2].CylindricLoad1.heatCapacitor.T +Injection.pipe6.simplePipe.PipeWall[3].CylindricLoad1.heatCapacitor.T +Injection.pipe6.simplePipe.vol[1].dynBal.U +Injection.pipe6.simplePipe.vol[2].dynBal.U +Injection.pipe6.simplePipe.vol[3].dynBal.U +Injection.pipe7.Insulation.CylindricLoad1.heatCapacitor.T +Injection.pipe7.simplePipe.PipeWall[1].CylindricLoad1.heatCapacitor.T +Injection.pipe7.simplePipe.PipeWall[2].CylindricLoad1.heatCapacitor.T +Injection.pipe7.simplePipe.PipeWall[3].CylindricLoad1.heatCapacitor.T +Injection.pipe7.simplePipe.vol[1].dynBal.U +Injection.pipe7.simplePipe.vol[2].dynBal.U +Injection.pipe7.simplePipe.vol[3].dynBal.U +Injection.PT1_a1.y +Injection.PT1_a2.y +Injection.PT1_b1.y +Injection.PT1_b2.y +Injection.PumpInterface.pump.filter.s[1] +Injection.PumpInterface.pump.filter.s[2] +Injection.PumpInterface.pump.vol.dynBal.U +Injection.senT_a1.T +Injection.senT_a2.T +Injection.senT_b1.T +Injection.senT_b2.T +Injection.valve.filter.s[1] +Finished +Finished + = true + + +Declaring variable: Boolean rScript ; + +savelog("AixLib.Systems.HydraulicModules.Example.Injection2WayValve.translation.log"); = true + + +rCheck = checkModel("AixLib.Systems.ModularAHU.Examples.Heater"); +Check of AixLib.Systems.ModularAHU.Examples.Heater +The model has the same number of unknowns and equations: 2546 +The model could not be deduced to be symbolically well-posed. +The model has + 2490+registerModule.hydraulicModule.valve.vol.dynBal.nPorts+registerModule.hydraulicModule.pipe1.simplePipe.vol[1].dynBal.nPorts +registerModule.hydraulicModule.pipe1.simplePipe.vol[2].dynBal.nPorts+ registerModule.hydraulicModule.pipe1.simplePipe.vol[3].dynBal.nPorts+ registerModule.hydraulicModule.pipe2.simplePipe.vol[1].dynBal.nPorts+ registerModule.hydraulicModule.pipe2.simplePipe.vol[2].dynBal.nPorts+ registerModule.hydraulicModule.pipe2.simplePipe.vol[3].dynBal.nPorts+ registerModule.hydraulicModule.pipe3.simplePipe.vol[1].dynBal.nPorts+ registerModule.hydraulicModule.pipe3.simplePipe.vol[2].dynBal.nPorts+ registerModule.hydraulicModule.pipe3.simplePipe.vol[3].dynBal.nPorts+ registerModule.hydraulicModule.pipe4.simplePipe.vol[1].dynBal.nPorts+ registerModule.hydraulicModule.pipe4.simplePipe.vol[2].dynBal.nPorts+ registerModule.hydraulicModule.pipe4.simplePipe.vol[3].dynBal.nPorts+ registerModule.hydraulicModule.pipe5.simplePipe.vol[1].dynBal.nPorts+ registerModule.hydraulicModule.pipe5.simplePipe.vol[2].dynBal.nPorts+ registerModule.hydraulicModule.pipe5.simplePipe.vol[3].dynBal.nPorts+ registerModule.hydraulicModule.pipe6.simplePipe.vol[1].dynBal.nPorts+ registerModule.hydraulicModule.pipe6.simplePipe.vol[2].dynBal.nPorts+ registerModule.hydraulicModule.pipe6.simplePipe.vol[3].dynBal.nPorts+ registerModule.hydraulicModule.junc456.dynBal.nPorts+registerModule.hydraulicModule.PumpInterface.pump.vol.dynBal.nPorts +2*registerModule.dynamicHX.vol1[1].dynBal.nPorts+2*registerModule.dynamicHX.vol1[2].dynBal.nPorts +registerModule.dynamicHX.vol2[1].dynBal.nPorts+registerModule.dynamicHX.vol2[2].dynBal.nPorts +scalar unknowns and + 2331+(if boundaryWaterSource.use_Xi_in then 1 else (if boundaryWaterSource.use_X_in then 0 else 1))+(if not boundaryWaterSource.use_p_in then 1 else 0)+2* boundaryWaterSource.nPorts+(if not boundaryWaterSource.use_T_in then 1 else 0) +(if boundaryWaterSink.use_Xi_in then 1 else (if boundaryWaterSink.use_X_in then 0 else 1))+(if not boundaryWaterSink.use_p_in then 1 else 0)+2* boundaryWaterSink.nPorts+(if not boundaryWaterSink.use_T_in then 1 else 0)+( if boundaryAirSource.use_Xi_in then 2 else (if boundaryAirSource.use_X_in then 1 else 3))+3*boundaryAirSource.nPorts+(if not boundaryAirSource.use_p_in then 1 else 0)+(if not boundaryAirSource.use_T_in then 1 else 0)+(if boundaryAirSink.use_Xi_in then 2 else (if boundaryAirSink.use_X_in then 1 else 3))+3*boundaryAirSink.nPorts+(if not boundaryAirSink.use_p_in then 1 else 0)+(if not boundaryAirSink.use_T_in then 1 else 0)+(if not registerModule.hydraulicModule.pipe1.simplePipe.vol[1].dynBal.use_mWat_flow then 1 else 0)+3*registerModule.hydraulicModule.pipe1.simplePipe.vol[1].dynBal.nPorts +(if not registerModule.hydraulicModule.pipe1.simplePipe.vol[2].dynBal.use_mWat_flow then 1 else 0)+3*registerModule.hydraulicModule.pipe1.simplePipe.vol[2].dynBal.nPorts +(if not registerModule.hydraulicModule.pipe1.simplePipe.vol[3].dynBal.use_mWat_flow then 1 else 0)+3*registerModule.hydraulicModule.pipe1.simplePipe.vol[3].dynBal.nPorts +(if not registerModule.hydraulicModule.pipe2.simplePipe.vol[1].dynBal.use_mWat_flow then 1 else 0)+3*registerModule.hydraulicModule.pipe2.simplePipe.vol[1].dynBal.nPorts +(if not registerModule.hydraulicModule.pipe2.simplePipe.vol[2].dynBal.use_mWat_flow then 1 else 0)+3*registerModule.hydraulicModule.pipe2.simplePipe.vol[2].dynBal.nPorts +(if not registerModule.hydraulicModule.pipe2.simplePipe.vol[3].dynBal.use_mWat_flow then 1 else 0)+3*registerModule.hydraulicModule.pipe2.simplePipe.vol[3].dynBal.nPorts +(if not registerModule.hydraulicModule.pipe3.simplePipe.vol[1].dynBal.use_mWat_flow then 1 else 0)+3*registerModule.hydraulicModule.pipe3.simplePipe.vol[1].dynBal.nPorts +(if not registerModule.hydraulicModule.pipe3.simplePipe.vol[2].dynBal.use_mWat_flow then 1 else 0)+3*registerModule.hydraulicModule.pipe3.simplePipe.vol[2].dynBal.nPorts +(if not registerModule.hydraulicModule.pipe3.simplePipe.vol[3].dynBal.use_mWat_flow then 1 else 0)+3*registerModule.hydraulicModule.pipe3.simplePipe.vol[3].dynBal.nPorts +(if not registerModule.hydraulicModule.pipe4.simplePipe.vol[1].dynBal.use_mWat_flow then 1 else 0)+3*registerModule.hydraulicModule.pipe4.simplePipe.vol[1].dynBal.nPorts +(if not registerModule.hydraulicModule.pipe4.simplePipe.vol[2].dynBal.use_mWat_flow then 1 else 0)+3*registerModule.hydraulicModule.pipe4.simplePipe.vol[2].dynBal.nPorts +(if not registerModule.hydraulicModule.pipe4.simplePipe.vol[3].dynBal.use_mWat_flow then 1 else 0)+3*registerModule.hydraulicModule.pipe4.simplePipe.vol[3].dynBal.nPorts +(if not registerModule.hydraulicModule.pipe5.simplePipe.vol[1].dynBal.use_mWat_flow then 1 else 0)+3*registerModule.hydraulicModule.pipe5.simplePipe.vol[1].dynBal.nPorts +(if not registerModule.hydraulicModule.pipe5.simplePipe.vol[2].dynBal.use_mWat_flow then 1 else 0)+3*registerModule.hydraulicModule.pipe5.simplePipe.vol[2].dynBal.nPorts +(if not registerModule.hydraulicModule.pipe5.simplePipe.vol[3].dynBal.use_mWat_flow then 1 else 0)+3*registerModule.hydraulicModule.pipe5.simplePipe.vol[3].dynBal.nPorts +(if not registerModule.hydraulicModule.pipe6.simplePipe.vol[1].dynBal.use_mWat_flow then 1 else 0)+3*registerModule.hydraulicModule.pipe6.simplePipe.vol[1].dynBal.nPorts +(if not registerModule.hydraulicModule.pipe6.simplePipe.vol[2].dynBal.use_mWat_flow then 1 else 0)+3*registerModule.hydraulicModule.pipe6.simplePipe.vol[2].dynBal.nPorts +(if not registerModule.hydraulicModule.pipe6.simplePipe.vol[3].dynBal.use_mWat_flow then 1 else 0)+3*registerModule.hydraulicModule.pipe6.simplePipe.vol[3].dynBal.nPorts +(if not registerModule.hydraulicModule.junc456.dynBal.use_mWat_flow then 1 else 0)+3*registerModule.hydraulicModule.junc456.dynBal.nPorts+(if not registerModule.hydraulicModule.PumpInterface.pump.vol.dynBal.use_mWat_flow then 1 else 0)+3*registerModule.hydraulicModule.PumpInterface.pump.vol.dynBal.nPorts +(if not registerModule.dynamicHX.vol1[1].dynBal.use_mWat_flow then 1 else 0) +5*registerModule.dynamicHX.vol1[1].dynBal.nPorts+(if not registerModule.dynamicHX.vol1[2].dynBal.use_mWat_flow then 1 else 0)+5*registerModule.dynamicHX.vol1[2].dynBal.nPorts+(if not registerModule.dynamicHX.vol2[1].dynBal.use_mWat_flow then 1 else 0)+3* registerModule.dynamicHX.vol2[1].dynBal.nPorts+(if not registerModule.dynamicHX.vol2[2].dynBal.use_mWat_flow then 1 else 0)+3*registerModule.dynamicHX.vol2[2].dynBal.nPorts+(if not registerModule.hydraulicModule.valve.vol.dynBal.use_mWat_flow then 1 else 0)+3 *registerModule.hydraulicModule.valve.vol.dynBal.nPorts +scalar equations. +However, exploiting the given numerical settings of parameters gives the same number of unknowns and equations: + 2546 +Check of AixLib.Systems.ModularAHU.Examples.Heater successful. +Declaring variable: Boolean rCheck ; + +Modelica.Utilities.Streams.print(" { \"file\" : \"AixLib/Resources/Scripts/Dymola/Systems/ModularAHU/Examples/Heater.mos\",", "AixLib.Systems.ModularAHU.Examples.Heater.statistics.log"); +Modelica.Utilities.Streams.print(" \"model\" : \"AixLib.Systems.ModularAHU.Examples.Heater\",", "AixLib.Systems.ModularAHU.Examples.Heater.statistics.log"); +Modelica.Utilities.Streams.print(" \"check\" : {", "AixLib.Systems.ModularAHU.Examples.Heater.statistics.log"); +Modelica.Utilities.Streams.print(" \"command\" : \"checkModel(\\\"AixLib.Systems.ModularAHU.Examples.Heater\\\");\",", "AixLib.Systems.ModularAHU.Examples.Heater.statistics.log"); +Modelica.Utilities.Streams.print(" \"result\" : " + String(rCheck), "AixLib.Systems.ModularAHU.Examples.Heater.statistics.log"); +Modelica.Utilities.Streams.print(" },", "AixLib.Systems.ModularAHU.Examples.Heater.statistics.log"); + + +rScript=RunScript("modelica://AixLib/Resources/Scripts/Dymola/Systems/ModularAHU/Examples/Heater.mos"); +simulateModel("AixLib.Systems.ModularAHU.Examples.Heater", tolerance=1e-6, stopTime=3600, resultFile="AixLib.Systems.ModularAHU.Examples.Heater"); +Translation of AixLib.Systems.ModularAHU.Examples.Heater +The DAE has 2546 scalar unknowns and 2546 scalar equations. +Redundant consistent initial conditions. +Removed the following equations which are redundant and consistent: + if (registerModule.dynamicHX.vol1[1].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (registerModule.dynamicHX.vol1[1].dynBal.initialize_p) then + registerModule.dynamicHX.vol1[1].dynBal.medium.p = registerModule.dynamicHX.vol1[1].dynBal.p_start; + end if; + else + if (registerModule.dynamicHX.vol1[1].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. SteadyStateInitial) then + if (registerModule.dynamicHX.vol1[1].dynBal.initialize_p) then + der(registerModule.dynamicHX.vol1[1].dynBal.medium.p) = 0; + end if; + end if; + end if; + if (registerModule.dynamicHX.vol1[2].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (registerModule.dynamicHX.vol1[2].dynBal.initialize_p) then + registerModule.dynamicHX.vol1[2].dynBal.medium.p = registerModule.dynamicHX.vol1[2].dynBal.p_start; + end if; + else + if (registerModule.dynamicHX.vol1[2].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. SteadyStateInitial) then + if (registerModule.dynamicHX.vol1[2].dynBal.initialize_p) then + der(registerModule.dynamicHX.vol1[2].dynBal.medium.p) = 0; + end if; + end if; + end if; + +The redundancies involve +initial equations: + 0.0 = 0; + 0.0 = 0; + + +Statistics + +Original Model + Number of components: 549 + Variables: 6673 + Constants: 134 (134 scalars) + Parameters: 3181 (3386 scalars) + Unknowns: 3358 (2653 scalars) + Differentiated variables: 122 scalars + Equations: 2479 + Nontrivial: 1925 +Translated Model + Constants: 2408 scalars + Free parameters: 212 scalars + Parameter depending: 1209 scalars + Continuous time states: 70 scalars + Time-varying variables: 592 scalars + Alias variables: 1752 scalars + Number of mixed real/discrete systems of equations: 0 + Sizes of linear systems of equations: {5, 2, 5, 2, 5, 2, 5, 2, 5, 2, 5, 2} + Sizes after manipulation of the linear systems: {0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0} + Sizes of nonlinear systems of equations: {21} + Sizes after manipulation of the nonlinear systems: {2} + Number of numerical Jacobians: 0 + Initialization problem + Sizes of linear systems of equations: {4, 179, 12} + Sizes after manipulation of the linear systems: {2, 59, 2} + Sizes of nonlinear systems of equations: {1, 21, 1} + Sizes after manipulation of the nonlinear systems: {0, 4, 0} + Sizes of simplified homotopy nonlinear systems of equations: {21, 1} + Sizes after manipulation of the simplified homotopy nonlinear systems: {3, 0} + Number of numerical Jacobians: 0 + +Selected continuous time states +Statically selected continuous time states +ctrBasic.PID.D.x +ctrBasic.PID.I.y +registerModule.dynamicHX.heatCapacitor[1].T +registerModule.dynamicHX.heatCapacitor[2].T +registerModule.dynamicHX.vol1[1].dynBal.medium.T +registerModule.dynamicHX.vol1[1].dynBal.medium.Xi[1] +registerModule.dynamicHX.vol1[2].dynBal.medium.T +registerModule.dynamicHX.vol1[2].dynBal.medium.Xi[1] +registerModule.dynamicHX.vol2[1].dynBal.medium.T +registerModule.dynamicHX.vol2[2].dynBal.medium.T +registerModule.hydraulicModule.junc456.dynBal.medium.T +registerModule.hydraulicModule.pipe1.Insulation.CylindricLoad1.heatCapacitor.T +registerModule.hydraulicModule.pipe1.simplePipe.PipeWall[1].CylindricLoad1.heatCapacitor.T +registerModule.hydraulicModule.pipe1.simplePipe.PipeWall[2].CylindricLoad1.heatCapacitor.T +registerModule.hydraulicModule.pipe1.simplePipe.PipeWall[3].CylindricLoad1.heatCapacitor.T +registerModule.hydraulicModule.pipe1.simplePipe.vol[1].dynBal.medium.T +registerModule.hydraulicModule.pipe1.simplePipe.vol[2].dynBal.medium.T +registerModule.hydraulicModule.pipe1.simplePipe.vol[3].dynBal.medium.T +registerModule.hydraulicModule.pipe2.Insulation.CylindricLoad1.heatCapacitor.T +registerModule.hydraulicModule.pipe2.simplePipe.PipeWall[1].CylindricLoad1.heatCapacitor.T +registerModule.hydraulicModule.pipe2.simplePipe.PipeWall[2].CylindricLoad1.heatCapacitor.T +registerModule.hydraulicModule.pipe2.simplePipe.PipeWall[3].CylindricLoad1.heatCapacitor.T +registerModule.hydraulicModule.pipe2.simplePipe.vol[1].dynBal.medium.T +registerModule.hydraulicModule.pipe2.simplePipe.vol[2].dynBal.medium.T +registerModule.hydraulicModule.pipe2.simplePipe.vol[3].dynBal.medium.T +registerModule.hydraulicModule.pipe3.Insulation.CylindricLoad1.heatCapacitor.T +registerModule.hydraulicModule.pipe3.simplePipe.PipeWall[1].CylindricLoad1.heatCapacitor.T +registerModule.hydraulicModule.pipe3.simplePipe.PipeWall[2].CylindricLoad1.heatCapacitor.T +registerModule.hydraulicModule.pipe3.simplePipe.PipeWall[3].CylindricLoad1.heatCapacitor.T +registerModule.hydraulicModule.pipe3.simplePipe.vol[1].dynBal.medium.T +registerModule.hydraulicModule.pipe3.simplePipe.vol[2].dynBal.medium.T +registerModule.hydraulicModule.pipe3.simplePipe.vol[3].dynBal.medium.T +registerModule.hydraulicModule.pipe4.Insulation.CylindricLoad1.heatCapacitor.T +registerModule.hydraulicModule.pipe4.simplePipe.PipeWall[1].CylindricLoad1.heatCapacitor.T +registerModule.hydraulicModule.pipe4.simplePipe.PipeWall[2].CylindricLoad1.heatCapacitor.T +registerModule.hydraulicModule.pipe4.simplePipe.PipeWall[3].CylindricLoad1.heatCapacitor.T +registerModule.hydraulicModule.pipe4.simplePipe.vol[1].dynBal.medium.T +registerModule.hydraulicModule.pipe4.simplePipe.vol[2].dynBal.medium.T +registerModule.hydraulicModule.pipe4.simplePipe.vol[3].dynBal.medium.T +registerModule.hydraulicModule.pipe5.Insulation.CylindricLoad1.heatCapacitor.T +registerModule.hydraulicModule.pipe5.simplePipe.PipeWall[1].CylindricLoad1.heatCapacitor.T +registerModule.hydraulicModule.pipe5.simplePipe.PipeWall[2].CylindricLoad1.heatCapacitor.T +registerModule.hydraulicModule.pipe5.simplePipe.PipeWall[3].CylindricLoad1.heatCapacitor.T +registerModule.hydraulicModule.pipe5.simplePipe.vol[1].dynBal.medium.T +registerModule.hydraulicModule.pipe5.simplePipe.vol[2].dynBal.medium.T +registerModule.hydraulicModule.pipe5.simplePipe.vol[3].dynBal.medium.T +registerModule.hydraulicModule.pipe6.Insulation.CylindricLoad1.heatCapacitor.T +registerModule.hydraulicModule.pipe6.simplePipe.PipeWall[1].CylindricLoad1.heatCapacitor.T +registerModule.hydraulicModule.pipe6.simplePipe.PipeWall[2].CylindricLoad1.heatCapacitor.T +registerModule.hydraulicModule.pipe6.simplePipe.PipeWall[3].CylindricLoad1.heatCapacitor.T +registerModule.hydraulicModule.pipe6.simplePipe.vol[1].dynBal.medium.T +registerModule.hydraulicModule.pipe6.simplePipe.vol[2].dynBal.medium.T +registerModule.hydraulicModule.pipe6.simplePipe.vol[3].dynBal.medium.T +registerModule.hydraulicModule.PT1_a1.y +registerModule.hydraulicModule.PT1_a2.y +registerModule.hydraulicModule.PT1_b1.y +registerModule.hydraulicModule.PT1_b2.y +registerModule.hydraulicModule.PumpInterface.pump.filter.s[1] +registerModule.hydraulicModule.PumpInterface.pump.filter.s[2] +registerModule.hydraulicModule.PumpInterface.pump.vol.dynBal.medium.T +registerModule.hydraulicModule.senT_a1.T +registerModule.hydraulicModule.senT_a2.T +registerModule.hydraulicModule.senT_b1.T +registerModule.hydraulicModule.senT_b2.T +registerModule.hydraulicModule.valve.filter.s[1] +registerModule.hydraulicModule.valve.vol.dynBal.medium.T +registerModule.PT1_airIn.y +registerModule.PT1_airOut.y +registerModule.senT_airIn.T +registerModule.senT_airOut.T +Finished +Finished + = true + +Declaring variable: Boolean rScript ; + +savelog("AixLib.Systems.ModularAHU.Examples.Heater.translation.log"); = true + + +rCheck = checkModel("AixLib.Systems.HydraulicModules.Example.ThrottlePump"); +Check of AixLib.Systems.HydraulicModules.Example.ThrottlePump +The model has the same number of unknowns and equations: 1396 +The model could not be deduced to be symbolically well-posed. +The model has + 1370+ThrottlePump.PumpInterface.pump.vol.dynBal.nPorts+ThrottlePump.pipe1.simplePipe.vol[1].dynBal.nPorts +ThrottlePump.pipe1.simplePipe.vol[2].dynBal.nPorts+ThrottlePump.pipe1.simplePipe.vol[3].dynBal.nPorts +ThrottlePump.pipe2.simplePipe.vol[1].dynBal.nPorts+ThrottlePump.pipe2.simplePipe.vol[2].dynBal.nPorts +ThrottlePump.pipe2.simplePipe.vol[3].dynBal.nPorts+ThrottlePump.pipe3.simplePipe.vol[1].dynBal.nPorts +ThrottlePump.pipe3.simplePipe.vol[2].dynBal.nPorts+ThrottlePump.pipe3.simplePipe.vol[3].dynBal.nPorts +ThrottlePump.pipe4.simplePipe.vol[1].dynBal.nPorts+ThrottlePump.pipe4.simplePipe.vol[2].dynBal.nPorts +ThrottlePump.pipe4.simplePipe.vol[3].dynBal.nPorts +scalar unknowns and + 1295+(if boundary.use_Xi_in then 1 else (if boundary.use_X_in then 0 else 1))+( if not boundary.use_p_in then 1 else 0)+2*boundary.nPorts+(if not boundary.use_T_in then 1 else 0)+(if boundary1.use_Xi_in then 1 else (if boundary1.use_X_in then 0 else 1))+(if not boundary1.use_p_in then 1 else 0)+2 *boundary1.nPorts+(if not boundary1.use_T_in then 1 else 0)+(if not ThrottlePump.PumpInterface.pump.vol.dynBal.use_mWat_flow then 1 else 0)+3* ThrottlePump.PumpInterface.pump.vol.dynBal.nPorts+(if not ThrottlePump.pipe1.simplePipe.vol[1].dynBal.use_mWat_flow then 1 else 0)+3*ThrottlePump.pipe1.simplePipe.vol[1].dynBal.nPorts+(if not ThrottlePump.pipe1.simplePipe.vol[2].dynBal.use_mWat_flow then 1 else 0)+3* ThrottlePump.pipe1.simplePipe.vol[2].dynBal.nPorts+(if not ThrottlePump.pipe1.simplePipe.vol[3].dynBal.use_mWat_flow then 1 else 0)+3*ThrottlePump.pipe1.simplePipe.vol[3].dynBal.nPorts+(if not ThrottlePump.pipe2.simplePipe.vol[1].dynBal.use_mWat_flow then 1 else 0)+3* ThrottlePump.pipe2.simplePipe.vol[1].dynBal.nPorts+(if not ThrottlePump.pipe2.simplePipe.vol[2].dynBal.use_mWat_flow then 1 else 0)+3*ThrottlePump.pipe2.simplePipe.vol[2].dynBal.nPorts+(if not ThrottlePump.pipe2.simplePipe.vol[3].dynBal.use_mWat_flow then 1 else 0)+3* ThrottlePump.pipe2.simplePipe.vol[3].dynBal.nPorts+(if not ThrottlePump.pipe3.simplePipe.vol[1].dynBal.use_mWat_flow then 1 else 0)+3*ThrottlePump.pipe3.simplePipe.vol[1].dynBal.nPorts+(if not ThrottlePump.pipe3.simplePipe.vol[2].dynBal.use_mWat_flow then 1 else 0)+3* ThrottlePump.pipe3.simplePipe.vol[2].dynBal.nPorts+(if not ThrottlePump.pipe3.simplePipe.vol[3].dynBal.use_mWat_flow then 1 else 0)+3*ThrottlePump.pipe3.simplePipe.vol[3].dynBal.nPorts+(if not ThrottlePump.pipe4.simplePipe.vol[1].dynBal.use_mWat_flow then 1 else 0)+3* ThrottlePump.pipe4.simplePipe.vol[1].dynBal.nPorts+(if not ThrottlePump.pipe4.simplePipe.vol[2].dynBal.use_mWat_flow then 1 else 0)+3*ThrottlePump.pipe4.simplePipe.vol[2].dynBal.nPorts+(if not ThrottlePump.pipe4.simplePipe.vol[3].dynBal.use_mWat_flow then 1 else 0)+3* ThrottlePump.pipe4.simplePipe.vol[3].dynBal.nPorts +scalar equations. +However, exploiting the given numerical settings of parameters gives the same number of unknowns and equations: + 1396 +Check of AixLib.Systems.HydraulicModules.Example.ThrottlePump successful. +Declaring variable: Boolean rCheck ; + +Modelica.Utilities.Streams.print(" { \"file\" : \"AixLib/Resources/Scripts/Dymola/Systems/HydraulicModules/Examples/ThrottlePump.mos\",", "AixLib.Systems.HydraulicModules.Example.ThrottlePump.statistics.log"); +Modelica.Utilities.Streams.print(" \"model\" : \"AixLib.Systems.HydraulicModules.Example.ThrottlePump\",", "AixLib.Systems.HydraulicModules.Example.ThrottlePump.statistics.log"); +Modelica.Utilities.Streams.print(" \"check\" : {", "AixLib.Systems.HydraulicModules.Example.ThrottlePump.statistics.log"); +Modelica.Utilities.Streams.print(" \"command\" : \"checkModel(\\\"AixLib.Systems.HydraulicModules.Example.ThrottlePump\\\");\",", "AixLib.Systems.HydraulicModules.Example.ThrottlePump.statistics.log"); +Modelica.Utilities.Streams.print(" \"result\" : " + String(rCheck), "AixLib.Systems.HydraulicModules.Example.ThrottlePump.statistics.log"); +Modelica.Utilities.Streams.print(" },", "AixLib.Systems.HydraulicModules.Example.ThrottlePump.statistics.log"); + + +rScript=RunScript("modelica://AixLib/Resources/Scripts/Dymola/Systems/HydraulicModules/Examples/ThrottlePump.mos"); +simulateModel("AixLib.Systems.HydraulicModules.Example.ThrottlePump", tolerance=1e-6, stopTime=600, resultFile="AixLib.Systems.HydraulicModules.Example.ThrottlePump"); +Translation of AixLib.Systems.HydraulicModules.Example.ThrottlePump +The DAE has 1396 scalar unknowns and 1396 scalar equations. + +Statistics + +Original Model + Number of components: 315 + Variables: 3779 + Constants: 71 (71 scalars) + Parameters: 1848 (2020 scalars) + Unknowns: 1860 (1450 scalars) + Differentiated variables: 53 scalars + Equations: 1378 + Nontrivial: 1079 +Translated Model + Constants: 1400 scalars + Free parameters: 120 scalars + Parameter depending: 731 scalars + Outputs: 12 scalars + Continuous time states: 40 scalars + Time-varying variables: 312 scalars + Alias variables: 978 scalars + Number of mixed real/discrete systems of equations: 0 + Sizes of linear systems of equations: {5, 2, 5, 2, 5, 2, 5, 2} + Sizes after manipulation of the linear systems: {0, 0, 0, 0, 0, 0, 0, 0} + Sizes of nonlinear systems of equations: {14} + Sizes after manipulation of the nonlinear systems: {1} + Number of numerical Jacobians: 0 + Initialization problem + Sizes of nonlinear systems of equations: {14, 1} + Sizes after manipulation of the nonlinear systems: {1, 0} + Sizes of simplified homotopy nonlinear systems of equations: {14, 1} + Sizes after manipulation of the simplified homotopy nonlinear systems: {1, 0} + Number of numerical Jacobians: 0 + +Selected continuous time states +Statically selected continuous time states +ThrottlePump.pipe1.Insulation.CylindricLoad1.heatCapacitor.T +ThrottlePump.pipe1.simplePipe.PipeWall[1].CylindricLoad1.heatCapacitor.T +ThrottlePump.pipe1.simplePipe.PipeWall[2].CylindricLoad1.heatCapacitor.T +ThrottlePump.pipe1.simplePipe.PipeWall[3].CylindricLoad1.heatCapacitor.T +ThrottlePump.pipe1.simplePipe.vol[1].dynBal.U +ThrottlePump.pipe1.simplePipe.vol[2].dynBal.U +ThrottlePump.pipe1.simplePipe.vol[3].dynBal.U +ThrottlePump.pipe2.Insulation.CylindricLoad1.heatCapacitor.T +ThrottlePump.pipe2.simplePipe.PipeWall[1].CylindricLoad1.heatCapacitor.T +ThrottlePump.pipe2.simplePipe.PipeWall[2].CylindricLoad1.heatCapacitor.T +ThrottlePump.pipe2.simplePipe.PipeWall[3].CylindricLoad1.heatCapacitor.T +ThrottlePump.pipe2.simplePipe.vol[1].dynBal.U +ThrottlePump.pipe2.simplePipe.vol[2].dynBal.U +ThrottlePump.pipe2.simplePipe.vol[3].dynBal.U +ThrottlePump.pipe3.Insulation.CylindricLoad1.heatCapacitor.T +ThrottlePump.pipe3.simplePipe.PipeWall[1].CylindricLoad1.heatCapacitor.T +ThrottlePump.pipe3.simplePipe.PipeWall[2].CylindricLoad1.heatCapacitor.T +ThrottlePump.pipe3.simplePipe.PipeWall[3].CylindricLoad1.heatCapacitor.T +ThrottlePump.pipe3.simplePipe.vol[1].dynBal.U +ThrottlePump.pipe3.simplePipe.vol[2].dynBal.U +ThrottlePump.pipe3.simplePipe.vol[3].dynBal.U +ThrottlePump.pipe4.Insulation.CylindricLoad1.heatCapacitor.T +ThrottlePump.pipe4.simplePipe.PipeWall[1].CylindricLoad1.heatCapacitor.T +ThrottlePump.pipe4.simplePipe.PipeWall[2].CylindricLoad1.heatCapacitor.T +ThrottlePump.pipe4.simplePipe.PipeWall[3].CylindricLoad1.heatCapacitor.T +ThrottlePump.pipe4.simplePipe.vol[1].dynBal.U +ThrottlePump.pipe4.simplePipe.vol[2].dynBal.U +ThrottlePump.pipe4.simplePipe.vol[3].dynBal.U +ThrottlePump.PT1_a1.y +ThrottlePump.PT1_a2.y +ThrottlePump.PT1_b1.y +ThrottlePump.PT1_b2.y +ThrottlePump.PumpInterface.pump.filter.s[1] +ThrottlePump.PumpInterface.pump.filter.s[2] +ThrottlePump.PumpInterface.pump.vol.dynBal.U +ThrottlePump.senT_a1.T +ThrottlePump.senT_a2.T +ThrottlePump.senT_b1.T +ThrottlePump.senT_b2.T +ThrottlePump.valve.filter.s[1] +Finished +Finished + = true + + +Declaring variable: Boolean rScript ; + +savelog("AixLib.Systems.HydraulicModules.Example.ThrottlePump.translation.log"); = true + + +rCheck = checkModel("AixLib.Systems.ModularAHU.Validation.AHU2_Cooler"); +Check of AixLib.Systems.ModularAHU.Validation.AHU2_Cooler +The model has the same number of unknowns and equations: 2420 +The model could not be deduced to be symbolically well-posed. +The model has + 2341+max([size(combiTimeTable.columns, 1); size(combiTimeTable.offset, 1)])+ registerModule.hydraulicModule.valve.vol.dynBal.nPorts+registerModule.hydraulicModule.pipe1.plugFlowPipe.vol_b.dynBal.nPorts +registerModule.hydraulicModule.pipe1.plugFlowPipe.vol_a.dynBal.nPorts+ registerModule.hydraulicModule.pipe2.plugFlowPipe.vol_b.dynBal.nPorts+ registerModule.hydraulicModule.pipe2.plugFlowPipe.vol_a.dynBal.nPorts+ registerModule.hydraulicModule.pipe3.plugFlowPipe.vol_b.dynBal.nPorts+ registerModule.hydraulicModule.pipe3.plugFlowPipe.vol_a.dynBal.nPorts+ registerModule.hydraulicModule.pipe4.plugFlowPipe.vol_b.dynBal.nPorts+ registerModule.hydraulicModule.pipe4.plugFlowPipe.vol_a.dynBal.nPorts+ registerModule.hydraulicModule.pipe5.plugFlowPipe.vol_b.dynBal.nPorts+ registerModule.hydraulicModule.pipe5.plugFlowPipe.vol_a.dynBal.nPorts+ registerModule.hydraulicModule.pipe6.plugFlowPipe.vol_b.dynBal.nPorts+ registerModule.hydraulicModule.pipe6.plugFlowPipe.vol_a.dynBal.nPorts+ registerModule.hydraulicModule.junc456.dynBal.nPorts+2*size(registerModule.hydraulicModule.PumpInterface.physics.maxMinTable.columns, 1)+2*registerModule.hydraulicModule.PumpInterface.physics.deMultiplex2.n1+2* registerModule.hydraulicModule.PumpInterface.physics.deMultiplex2.n2+ registerModule.hydraulicModule.PumpInterface.physics.criticalDamping.n+ registerModule.hydraulicModule.PumpInterface.physics.vol.dynBal.nPorts+2* registerModule.dynamicHX.vol1[1].dynBal.nPorts+2*registerModule.dynamicHX.vol1[2].dynBal.nPorts +2*registerModule.dynamicHX.vol1[3].dynBal.nPorts+2*registerModule.dynamicHX.vol1[4].dynBal.nPorts +registerModule.dynamicHX.vol2[1].dynBal.nPorts+registerModule.dynamicHX.vol2[2].dynBal.nPorts +registerModule.dynamicHX.vol2[3].dynBal.nPorts+registerModule.dynamicHX.vol2[4].dynBal.nPorts +scalar unknowns and + 2193+(if boundaryWaterSource.use_Xi_in then 1 else (if boundaryWaterSource.use_X_in then 0 else 1))+(if not boundaryWaterSource.use_p_in then 1 else 0)+2* boundaryWaterSource.nPorts+(if not boundaryWaterSource.use_T_in then 1 else 0) +(if boundaryWaterSink.use_Xi_in then 1 else (if boundaryWaterSink.use_X_in then 0 else 1))+(if not boundaryWaterSink.use_p_in then 1 else 0)+2* boundaryWaterSink.nPorts+(if not boundaryWaterSink.use_T_in then 1 else 0)+( if boundaryAirSource.use_Xi_in then 2 else (if boundaryAirSource.use_X_in then 1 else 3))+3*boundaryAirSource.nPorts+(if not boundaryAirSource.use_m_flow_in then 1 else 0)+(if not boundaryAirSource.use_T_in then 1 else 0)+(if boundaryAirSink.use_Xi_in then 2 else (if boundaryAirSink.use_X_in then 1 else 3))+3*boundaryAirSink.nPorts+(if not boundaryAirSink.use_p_in then 1 else 0)+(if not boundaryAirSink.use_T_in then 1 else 0)+max([size( combiTimeTable.columns, 1); size(combiTimeTable.offset, 1)])+2*size( registerModule.hydraulicModule.PumpInterface.physics.maxMinTable.columns, 1)+ registerModule.hydraulicModule.PumpInterface.physics.deMultiplex2.n1+ registerModule.hydraulicModule.PumpInterface.physics.deMultiplex2.n2+ registerModule.hydraulicModule.PumpInterface.physics.criticalDamping.n+(if not registerModule.hydraulicModule.pipe1.plugFlowPipe.vol_b.dynBal.use_mWat_flow then 1 else 0)+3*registerModule.hydraulicModule.pipe1.plugFlowPipe.vol_b.dynBal.nPorts +(if not registerModule.hydraulicModule.pipe1.plugFlowPipe.vol_a.dynBal.use_mWat_flow then 1 else 0)+3*registerModule.hydraulicModule.pipe1.plugFlowPipe.vol_a.dynBal.nPorts +(if not registerModule.hydraulicModule.pipe2.plugFlowPipe.vol_b.dynBal.use_mWat_flow then 1 else 0)+3*registerModule.hydraulicModule.pipe2.plugFlowPipe.vol_b.dynBal.nPorts +(if not registerModule.hydraulicModule.pipe2.plugFlowPipe.vol_a.dynBal.use_mWat_flow then 1 else 0)+3*registerModule.hydraulicModule.pipe2.plugFlowPipe.vol_a.dynBal.nPorts +(if not registerModule.hydraulicModule.pipe3.plugFlowPipe.vol_b.dynBal.use_mWat_flow then 1 else 0)+3*registerModule.hydraulicModule.pipe3.plugFlowPipe.vol_b.dynBal.nPorts +(if not registerModule.hydraulicModule.pipe3.plugFlowPipe.vol_a.dynBal.use_mWat_flow then 1 else 0)+3*registerModule.hydraulicModule.pipe3.plugFlowPipe.vol_a.dynBal.nPorts +(if not registerModule.hydraulicModule.pipe4.plugFlowPipe.vol_b.dynBal.use_mWat_flow then 1 else 0)+3*registerModule.hydraulicModule.pipe4.plugFlowPipe.vol_b.dynBal.nPorts +(if not registerModule.hydraulicModule.pipe4.plugFlowPipe.vol_a.dynBal.use_mWat_flow then 1 else 0)+3*registerModule.hydraulicModule.pipe4.plugFlowPipe.vol_a.dynBal.nPorts +(if not registerModule.hydraulicModule.pipe5.plugFlowPipe.vol_b.dynBal.use_mWat_flow then 1 else 0)+3*registerModule.hydraulicModule.pipe5.plugFlowPipe.vol_b.dynBal.nPorts +(if not registerModule.hydraulicModule.pipe5.plugFlowPipe.vol_a.dynBal.use_mWat_flow then 1 else 0)+3*registerModule.hydraulicModule.pipe5.plugFlowPipe.vol_a.dynBal.nPorts +(if not registerModule.hydraulicModule.pipe6.plugFlowPipe.vol_b.dynBal.use_mWat_flow then 1 else 0)+3*registerModule.hydraulicModule.pipe6.plugFlowPipe.vol_b.dynBal.nPorts +(if not registerModule.hydraulicModule.pipe6.plugFlowPipe.vol_a.dynBal.use_mWat_flow then 1 else 0)+3*registerModule.hydraulicModule.pipe6.plugFlowPipe.vol_a.dynBal.nPorts +(if not registerModule.hydraulicModule.junc456.dynBal.use_mWat_flow then 1 else 0)+3*registerModule.hydraulicModule.junc456.dynBal.nPorts+(if not registerModule.hydraulicModule.PumpInterface.physics.vol.dynBal.use_mWat_flow then 1 else 0)+3*registerModule.hydraulicModule.PumpInterface.physics.vol.dynBal.nPorts +(if not registerModule.dynamicHX.vol1[1].dynBal.use_mWat_flow then 1 else 0) +5*registerModule.dynamicHX.vol1[1].dynBal.nPorts+(if not registerModule.dynamicHX.vol1[2].dynBal.use_mWat_flow then 1 else 0)+5*registerModule.dynamicHX.vol1[2].dynBal.nPorts+(if not registerModule.dynamicHX.vol1[3].dynBal.use_mWat_flow then 1 else 0)+5* registerModule.dynamicHX.vol1[3].dynBal.nPorts+(if not registerModule.dynamicHX.vol1[4].dynBal.use_mWat_flow then 1 else 0)+5*registerModule.dynamicHX.vol1[4].dynBal.nPorts+(if not registerModule.dynamicHX.vol2[1].dynBal.use_mWat_flow then 1 else 0)+3* registerModule.dynamicHX.vol2[1].dynBal.nPorts+(if not registerModule.dynamicHX.vol2[2].dynBal.use_mWat_flow then 1 else 0)+3*registerModule.dynamicHX.vol2[2].dynBal.nPorts+(if not registerModule.dynamicHX.vol2[3].dynBal.use_mWat_flow then 1 else 0)+3* registerModule.dynamicHX.vol2[3].dynBal.nPorts+(if not registerModule.dynamicHX.vol2[4].dynBal.use_mWat_flow then 1 else 0)+3*registerModule.dynamicHX.vol2[4].dynBal.nPorts+(if not registerModule.hydraulicModule.valve.vol.dynBal.use_mWat_flow then 1 else 0)+3 *registerModule.hydraulicModule.valve.vol.dynBal.nPorts +scalar equations. +However, exploiting the given numerical settings of parameters gives the same number of unknowns and equations: + 2420 +Check of AixLib.Systems.ModularAHU.Validation.AHU2_Cooler successful. +Declaring variable: Boolean rCheck ; + +Modelica.Utilities.Streams.print(" { \"file\" : \"AixLib/Resources/Scripts/Dymola/Systems/ModularAHU/Validation/AHU2_Cooler.mos\",", "AixLib.Systems.ModularAHU.Validation.AHU2_Cooler.statistics.log"); +Modelica.Utilities.Streams.print(" \"model\" : \"AixLib.Systems.ModularAHU.Validation.AHU2_Cooler\",", "AixLib.Systems.ModularAHU.Validation.AHU2_Cooler.statistics.log"); +Modelica.Utilities.Streams.print(" \"check\" : {", "AixLib.Systems.ModularAHU.Validation.AHU2_Cooler.statistics.log"); +Modelica.Utilities.Streams.print(" \"command\" : \"checkModel(\\\"AixLib.Systems.ModularAHU.Validation.AHU2_Cooler\\\");\",", "AixLib.Systems.ModularAHU.Validation.AHU2_Cooler.statistics.log"); +Modelica.Utilities.Streams.print(" \"result\" : " + String(rCheck), "AixLib.Systems.ModularAHU.Validation.AHU2_Cooler.statistics.log"); +Modelica.Utilities.Streams.print(" },", "AixLib.Systems.ModularAHU.Validation.AHU2_Cooler.statistics.log"); + + +rScript=RunScript("modelica://AixLib/Resources/Scripts/Dymola/Systems/ModularAHU/Validation/AHU2_Cooler.mos"); +simulateModel("AixLib.Systems.ModularAHU.Validation.AHU2_Cooler", tolerance=1e-6, outputInterval=1, stopTime=2700, resultFile="AixLib.Systems.ModularAHU.Validation.AHU2_Cooler"); +Translation of AixLib.Systems.ModularAHU.Validation.AHU2_Cooler +The DAE has 2420 scalar unknowns and 2420 scalar equations. + +Statistics + +Original Model + Number of components: 464 + Variables: 6155 + Constants: 125 (125 scalars) + Parameters: 2790 (41180 scalars) + Unknowns: 3240 (2523 scalars) + Differentiated variables: 86 scalars + Equations: 2514 + Nontrivial: 1950 +Translated Model + Constants: 2102 scalars + Free parameters: 19390 scalars + Parameter depending: 20131 scalars + Outputs: 17 scalars + Continuous time states: 62 scalars + Time-varying variables: 629 scalars + Alias variables: 1576 scalars + Number of mixed real/discrete systems of equations: 0 + Sizes of linear systems of equations: {2, 2, 2, 2, 2, 2} + Sizes after manipulation of the linear systems: {0, 0, 0, 0, 0, 0} + Sizes of nonlinear systems of equations: {18, 6, 6, 6, 6, 6, 6} + Sizes after manipulation of the nonlinear systems: {2, 1, 1, 1, 1, 1, 1} + Number of numerical Jacobians: 0 + Initialization problem + Sizes of nonlinear systems of equations: {18, 1} + Sizes after manipulation of the nonlinear systems: {4, 0} + Sizes of simplified homotopy nonlinear systems of equations: {18, 1} + Sizes after manipulation of the simplified homotopy nonlinear systems: {3, 0} + Number of numerical Jacobians: 0 + +Selected continuous time states +Statically selected continuous time states +registerModule.dynamicHX.heatCapacitor[1].T +registerModule.dynamicHX.heatCapacitor[2].T +registerModule.dynamicHX.heatCapacitor[3].T +registerModule.dynamicHX.heatCapacitor[4].T +registerModule.dynamicHX.vol1[1].dynBal.medium.Xi[1] +registerModule.dynamicHX.vol1[1].dynBal.U +registerModule.dynamicHX.vol1[2].dynBal.medium.Xi[1] +registerModule.dynamicHX.vol1[2].dynBal.U +registerModule.dynamicHX.vol1[3].dynBal.medium.Xi[1] +registerModule.dynamicHX.vol1[3].dynBal.U +registerModule.dynamicHX.vol1[4].dynBal.medium.Xi[1] +registerModule.dynamicHX.vol1[4].dynBal.U +registerModule.dynamicHX.vol2[1].dynBal.U +registerModule.dynamicHX.vol2[2].dynBal.U +registerModule.dynamicHX.vol2[3].dynBal.U +registerModule.dynamicHX.vol2[4].dynBal.U +registerModule.hydraulicModule.junc456.dynBal.U +registerModule.hydraulicModule.pipe1.Insulation.CylindricLoad1.heatCapacitor.T +registerModule.hydraulicModule.pipe1.plugFlowPipe.del.x +registerModule.hydraulicModule.pipe1.plugFlowPipe.timDel.x +registerModule.hydraulicModule.pipe1.plugFlowPipe.vol_a.dynBal.U +registerModule.hydraulicModule.pipe1.plugFlowPipe.vol_b.dynBal.U +registerModule.hydraulicModule.pipe2.Insulation.CylindricLoad1.heatCapacitor.T +registerModule.hydraulicModule.pipe2.plugFlowPipe.del.x +registerModule.hydraulicModule.pipe2.plugFlowPipe.timDel.x +registerModule.hydraulicModule.pipe2.plugFlowPipe.vol_a.dynBal.U +registerModule.hydraulicModule.pipe2.plugFlowPipe.vol_b.dynBal.U +registerModule.hydraulicModule.pipe3.Insulation.CylindricLoad1.heatCapacitor.T +registerModule.hydraulicModule.pipe3.plugFlowPipe.del.x +registerModule.hydraulicModule.pipe3.plugFlowPipe.timDel.x +registerModule.hydraulicModule.pipe3.plugFlowPipe.vol_a.dynBal.U +registerModule.hydraulicModule.pipe3.plugFlowPipe.vol_b.dynBal.U +registerModule.hydraulicModule.pipe4.Insulation.CylindricLoad1.heatCapacitor.T +registerModule.hydraulicModule.pipe4.plugFlowPipe.del.x +registerModule.hydraulicModule.pipe4.plugFlowPipe.timDel.x +registerModule.hydraulicModule.pipe4.plugFlowPipe.vol_a.dynBal.U +registerModule.hydraulicModule.pipe4.plugFlowPipe.vol_b.dynBal.U +registerModule.hydraulicModule.pipe5.Insulation.CylindricLoad1.heatCapacitor.T +registerModule.hydraulicModule.pipe5.plugFlowPipe.del.x +registerModule.hydraulicModule.pipe5.plugFlowPipe.timDel.x +registerModule.hydraulicModule.pipe5.plugFlowPipe.vol_a.dynBal.U +registerModule.hydraulicModule.pipe5.plugFlowPipe.vol_b.dynBal.U +registerModule.hydraulicModule.pipe6.Insulation.CylindricLoad1.heatCapacitor.T +registerModule.hydraulicModule.pipe6.plugFlowPipe.del.x +registerModule.hydraulicModule.pipe6.plugFlowPipe.timDel.x +registerModule.hydraulicModule.pipe6.plugFlowPipe.vol_a.dynBal.U +registerModule.hydraulicModule.pipe6.plugFlowPipe.vol_b.dynBal.U +registerModule.hydraulicModule.PT1_a1.y +registerModule.hydraulicModule.PT1_a2.y +registerModule.hydraulicModule.PT1_b1.y +registerModule.hydraulicModule.PT1_b2.y +registerModule.hydraulicModule.PumpInterface.physics.criticalDamping.x[1] +registerModule.hydraulicModule.PumpInterface.physics.criticalDamping.x[2] +registerModule.hydraulicModule.senT_a1.T +registerModule.hydraulicModule.senT_a2.T +registerModule.hydraulicModule.senT_b1.T +registerModule.hydraulicModule.senT_b2.T +registerModule.hydraulicModule.valve.vol.dynBal.U +registerModule.PT1_airIn.y +registerModule.PT1_airOut.y +registerModule.senT_airIn.T +registerModule.senT_airOut.T +Finished +Finished + = true + +Declaring variable: Boolean rScript ; + +savelog("AixLib.Systems.ModularAHU.Validation.AHU2_Cooler.translation.log"); = true + + +rCheck = checkModel("AixLib.Systems.ModularEnergySystems.ModularBoiler.Examples.ModularBoilerSimple"); +Check of AixLib.Systems.ModularEnergySystems.ModularBoiler.Examples.ModularBoilerSimple +The model has the same number of unknowns and equations: 575 +The model could not be deduced to be symbolically well-posed. +The model has + 545+modularBoiler.boilerGeneric.vol.dynBal.nPorts+2*modularBoiler.boilerGeneric.offDesignOperation.multiplex4.n1 +2*modularBoiler.boilerGeneric.offDesignOperation.multiplex4.n2+2* modularBoiler.boilerGeneric.offDesignOperation.multiplex4.n3+2* modularBoiler.boilerGeneric.offDesignOperation.multiplex4.n4+modularBoiler.boilerGeneric.offDesignOperation.boilerEffciency.nin +2*modularBoiler.boilerGeneric.designOperation.multiplex4.n1+2* modularBoiler.boilerGeneric.designOperation.multiplex4.n2+2*modularBoiler.boilerGeneric.designOperation.multiplex4.n3 +2*modularBoiler.boilerGeneric.designOperation.multiplex4.n4+modularBoiler.boilerGeneric.designOperation.boilerEffciency.nin +modularBoiler.pump.vol.dynBal.nPorts+vol.dynBal.nPorts +scalar unknowns and + 533+2*(modularBoiler.boilerGeneric.offDesignOperation.multiplex4.n1+ modularBoiler.boilerGeneric.offDesignOperation.multiplex4.n2+modularBoiler.boilerGeneric.offDesignOperation.multiplex4.n3 +modularBoiler.boilerGeneric.offDesignOperation.multiplex4.n4+modularBoiler.boilerGeneric.designOperation.multiplex4.n1 +modularBoiler.boilerGeneric.designOperation.multiplex4.n2+modularBoiler.boilerGeneric.designOperation.multiplex4.n3 +modularBoiler.boilerGeneric.designOperation.multiplex4.n4)+(if bou.use_Xi_in then 1 else (if bou.use_X_in then 0 else 1))+(if not bou.use_p_in then 1 else 0)+2*bou.nPorts+(if not bou.use_T_in then 1 else 0)+(if not modularBoiler.boilerGeneric.vol.dynBal.use_mWat_flow then 1 else 0)+3* modularBoiler.boilerGeneric.vol.dynBal.nPorts+(if not modularBoiler.pump.vol.dynBal.use_mWat_flow then 1 else 0)+3*modularBoiler.pump.vol.dynBal.nPorts+(if not vol.dynBal.use_mWat_flow then 1 else 0)+3*vol.dynBal.nPorts +scalar equations. +However, exploiting the given numerical settings of parameters gives the same number of unknowns and equations: + 575 +Check of AixLib.Systems.ModularEnergySystems.ModularBoiler.Examples.ModularBoilerSimple successful. +Declaring variable: Boolean rCheck ; + +Modelica.Utilities.Streams.print(" { \"file\" : \"AixLib/Resources/Scripts/Dymola/Systems/ModularEnergySystems/Examples/ModularBoilerSimple.mos\",", "AixLib.Systems.ModularEnergySystems.ModularBoiler.Examples.ModularBoilerSimple.statistics.log"); +Modelica.Utilities.Streams.print(" \"model\" : \"AixLib.Systems.ModularEnergySystems.ModularBoiler.Examples.ModularBoilerSimple\",", "AixLib.Systems.ModularEnergySystems.ModularBoiler.Examples.ModularBoilerSimple.statistics.log"); +Modelica.Utilities.Streams.print(" \"check\" : {", "AixLib.Systems.ModularEnergySystems.ModularBoiler.Examples.ModularBoilerSimple.statistics.log"); +Modelica.Utilities.Streams.print(" \"command\" : \"checkModel(\\\"AixLib.Systems.ModularEnergySystems.ModularBoiler.Examples.ModularBoilerSimple\\\");\",", "AixLib.Systems.ModularEnergySystems.ModularBoiler.Examples.ModularBoilerSimple.statistics.log"); +Modelica.Utilities.Streams.print(" \"result\" : " + String(rCheck), "AixLib.Systems.ModularEnergySystems.ModularBoiler.Examples.ModularBoilerSimple.statistics.log"); +Modelica.Utilities.Streams.print(" },", "AixLib.Systems.ModularEnergySystems.ModularBoiler.Examples.ModularBoilerSimple.statistics.log"); + + +rScript=RunScript("modelica://AixLib/Resources/Scripts/Dymola/Systems/ModularEnergySystems/Examples/ModularBoilerSimple.mos"); +simulateModel("AixLib.Systems.ModularEnergySystems.ModularBoiler.Examples.ModularBoilerSimple", tolerance=1e-06, stopTime=84000, method="dassl", resultFile="AixLib.Systems.ModularEnergySystems.ModularBoiler.Examples.ModularBoilerSimple"); +Translation of AixLib.Systems.ModularEnergySystems.ModularBoiler.Examples.ModularBoilerSimple +The DAE has 575 scalar unknowns and 575 scalar equations. + +Statistics + +Original Model + Number of components: 156 + Variables: 1280 + Constants: 18 (18 scalars) + Parameters: 621 (745 scalars) + Unknowns: 641 (594 scalars) + Differentiated variables: 14 scalars + Equations: 586 + Nontrivial: 485 +Translated Model + Constants: 412 scalars + Free parameters: 126 scalars + Parameter depending: 294 scalars + Outputs: 10 scalars + Continuous time states: 10 scalars + Time-varying variables: 143 scalars + Alias variables: 382 scalars + Number of mixed real/discrete systems of equations: 0 + Sizes of linear systems of equations: {4} + Sizes after manipulation of the linear systems: {0} + Sizes of nonlinear systems of equations: {5} + Sizes after manipulation of the nonlinear systems: {1} + Number of numerical Jacobians: 0 + Initialization problem + Sizes of nonlinear systems of equations: {5} + Sizes after manipulation of the nonlinear systems: {1} + Number of numerical Jacobians: 0 + +Selected continuous time states +Statically selected continuous time states +modularBoiler.boilerControl.internalFirRatControl.PID.I.y +modularBoiler.boilerGeneric.senTRet.T +modularBoiler.boilerGeneric.senTSup.T +modularBoiler.boilerGeneric.vol.dynBal.U +modularBoiler.pump.filter.s[1] +modularBoiler.pump.filter.s[2] +modularBoiler.pump.vol.dynBal.U +modularBoiler.senTRet.T +modularBoiler.senTSup.T +vol.dynBal.U +Finished +Finished + = true + +Declaring variable: Boolean rScript ; + +savelog("AixLib.Systems.ModularEnergySystems.ModularBoiler.Examples.ModularBoilerSimple.translation.log"); \ No newline at end of file diff --git a/docs/correct_HTML_issue1147_GenericBoiler/regression/Systems/unitTests-dymola.log b/docs/correct_HTML_issue1147_GenericBoiler/regression/Systems/unitTests-dymola.log new file mode 100644 index 0000000000..1e81a233a7 --- /dev/null +++ b/docs/correct_HTML_issue1147_GenericBoiler/regression/Systems/unitTests-dymola.log @@ -0,0 +1,11 @@ +Regression tests are only run for the following package: + AixLib.Systems +*** Warning: AixLib.Systems.ModularEnergySystems.ModularBoiler.Examples.ModularBoilerFeedback: Translation statistics for simulation changed for nonlinear, but results are unchanged. + Old = 1 + New = 2 +Comparison files output by funnel are stored in the directory 'funnel_comp' of size 1.1 MB. +Run 'python -c "import buildingspy.development.regressiontest as t; t.Tester(tool=\"dymola\").report()"' +to access a summary of the comparison results. + +Script that runs unit tests had 1 warnings and 0 errors. + diff --git a/docs/correct_HTML_issue1147_GenericBoiler/regression/ThermalZones/comparison-dymola.log b/docs/correct_HTML_issue1147_GenericBoiler/regression/ThermalZones/comparison-dymola.log new file mode 100644 index 0000000000..f91a07ea4a --- /dev/null +++ b/docs/correct_HTML_issue1147_GenericBoiler/regression/ThermalZones/comparison-dymola.log @@ -0,0 +1,3494 @@ +[ + { + "comparison": { + "file_name": "AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case430.mat", + "funnel_dirs": [ + "funnel_comp/AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case430.mat_checkResultsAccordingToASHRAEHeatingOrTempMax.lowerLimit", + "funnel_comp/AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case430.mat_AnnualHeatingLoad", + "funnel_comp/AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case430.mat_checkResultsAccordingToASHRAEHeatingOrTempMax.upperLimit", + "funnel_comp/AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case430.mat_checkResultsAccordingToASHRAECoolingOrTempMin.lowerLimit", + "funnel_comp/AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case430.mat_AnnualCoolingLoad", + "funnel_comp/AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case430.mat_checkResultsAccordingToASHRAECoolingOrTempMin.upperLimit", + "funnel_comp/AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case430.mat_checkResultsAccordingToASHRAEHeatingOrTempMax.satisfied", + 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a/docs/correct_HTML_issue1147_GenericBoiler/regression/ThermalZones/funnel_comp/AixLib.ThermalZones.HighOrder.Examples.ASHREA140.CompareDynamicAndStaticSolarFrac_Case270.mat_Room.solarRadInRoom.solar_frac_wall[1]/test.csv b/docs/correct_HTML_issue1147_GenericBoiler/regression/ThermalZones/funnel_comp/AixLib.ThermalZones.HighOrder.Examples.ASHREA140.CompareDynamicAndStaticSolarFrac_Case270.mat_Room.solarRadInRoom.solar_frac_wall[1]/test.csv new file mode 100644 index 0000000000..708f871592 --- /dev/null +++ b/docs/correct_HTML_issue1147_GenericBoiler/regression/ThermalZones/funnel_comp/AixLib.ThermalZones.HighOrder.Examples.ASHREA140.CompareDynamicAndStaticSolarFrac_Case270.mat_Room.solarRadInRoom.solar_frac_wall[1]/test.csv @@ -0,0 +1,3 @@ +x,y +0,0.0130000002682209 +86400,0.0130000002682209 diff --git 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a/docs/correct_HTML_issue1147_GenericBoiler/regression/ThermalZones/funnel_comp/AixLib.ThermalZones.HighOrder.Examples.ASHREA140.CompareDynamicAndStaticSolarFrac_Case270.mat_Room.solarRadInRoom.solar_frac_wall[3]/errors.csv b/docs/correct_HTML_issue1147_GenericBoiler/regression/ThermalZones/funnel_comp/AixLib.ThermalZones.HighOrder.Examples.ASHREA140.CompareDynamicAndStaticSolarFrac_Case270.mat_Room.solarRadInRoom.solar_frac_wall[3]/errors.csv new file mode 100644 index 0000000000..9d3b74303d --- /dev/null +++ b/docs/correct_HTML_issue1147_GenericBoiler/regression/ThermalZones/funnel_comp/AixLib.ThermalZones.HighOrder.Examples.ASHREA140.CompareDynamicAndStaticSolarFrac_Case270.mat_Room.solarRadInRoom.solar_frac_wall[3]/errors.csv @@ -0,0 +1,3 @@ +x,y +0,0 +86400,0 diff --git a/docs/correct_HTML_issue1147_GenericBoiler/regression/ThermalZones/funnel_comp/AixLib.ThermalZones.HighOrder.Examples.ASHREA140.CompareDynamicAndStaticSolarFrac_Case270.mat_Room.solarRadInRoom.solar_frac_wall[3]/lowerBound.csv b/docs/correct_HTML_issue1147_GenericBoiler/regression/ThermalZones/funnel_comp/AixLib.ThermalZones.HighOrder.Examples.ASHREA140.CompareDynamicAndStaticSolarFrac_Case270.mat_Room.solarRadInRoom.solar_frac_wall[3]/lowerBound.csv new file mode 100644 index 0000000000..994ea24b47 --- /dev/null +++ b/docs/correct_HTML_issue1147_GenericBoiler/regression/ThermalZones/funnel_comp/AixLib.ThermalZones.HighOrder.Examples.ASHREA140.CompareDynamicAndStaticSolarFrac_Case270.mat_Room.solarRadInRoom.solar_frac_wall[3]/lowerBound.csv @@ -0,0 +1,3 @@ +x,y +-0.001,0.0120000002682209 +86400.001,0.0120000002682209 diff --git a/docs/correct_HTML_issue1147_GenericBoiler/regression/ThermalZones/funnel_comp/AixLib.ThermalZones.HighOrder.Examples.ASHREA140.CompareDynamicAndStaticSolarFrac_Case270.mat_Room.solarRadInRoom.solar_frac_wall[3]/reference.csv b/docs/correct_HTML_issue1147_GenericBoiler/regression/ThermalZones/funnel_comp/AixLib.ThermalZones.HighOrder.Examples.ASHREA140.CompareDynamicAndStaticSolarFrac_Case270.mat_Room.solarRadInRoom.solar_frac_wall[3]/reference.csv new file mode 100644 index 0000000000..708f871592 --- /dev/null +++ b/docs/correct_HTML_issue1147_GenericBoiler/regression/ThermalZones/funnel_comp/AixLib.ThermalZones.HighOrder.Examples.ASHREA140.CompareDynamicAndStaticSolarFrac_Case270.mat_Room.solarRadInRoom.solar_frac_wall[3]/reference.csv @@ -0,0 +1,3 @@ +x,y +0,0.0130000002682209 +86400,0.0130000002682209 diff --git a/docs/correct_HTML_issue1147_GenericBoiler/regression/ThermalZones/funnel_comp/AixLib.ThermalZones.HighOrder.Examples.ASHREA140.CompareDynamicAndStaticSolarFrac_Case270.mat_Room.solarRadInRoom.solar_frac_wall[3]/test.csv b/docs/correct_HTML_issue1147_GenericBoiler/regression/ThermalZones/funnel_comp/AixLib.ThermalZones.HighOrder.Examples.ASHREA140.CompareDynamicAndStaticSolarFrac_Case270.mat_Room.solarRadInRoom.solar_frac_wall[3]/test.csv new file mode 100644 index 0000000000..708f871592 --- /dev/null +++ b/docs/correct_HTML_issue1147_GenericBoiler/regression/ThermalZones/funnel_comp/AixLib.ThermalZones.HighOrder.Examples.ASHREA140.CompareDynamicAndStaticSolarFrac_Case270.mat_Room.solarRadInRoom.solar_frac_wall[3]/test.csv @@ -0,0 +1,3 @@ +x,y +0,0.0130000002682209 +86400,0.0130000002682209 diff --git a/docs/correct_HTML_issue1147_GenericBoiler/regression/ThermalZones/funnel_comp/AixLib.ThermalZones.HighOrder.Examples.ASHREA140.CompareDynamicAndStaticSolarFrac_Case270.mat_Room.solarRadInRoom.solar_frac_wall[3]/upperBound.csv b/docs/correct_HTML_issue1147_GenericBoiler/regression/ThermalZones/funnel_comp/AixLib.ThermalZones.HighOrder.Examples.ASHREA140.CompareDynamicAndStaticSolarFrac_Case270.mat_Room.solarRadInRoom.solar_frac_wall[3]/upperBound.csv new file mode 100644 index 0000000000..8a2a5c733a --- /dev/null +++ b/docs/correct_HTML_issue1147_GenericBoiler/regression/ThermalZones/funnel_comp/AixLib.ThermalZones.HighOrder.Examples.ASHREA140.CompareDynamicAndStaticSolarFrac_Case270.mat_Room.solarRadInRoom.solar_frac_wall[3]/upperBound.csv @@ -0,0 +1,3 @@ +x,y +-0.001,0.0140000002682209 +86400.001,0.0140000002682209 diff --git a/docs/correct_HTML_issue1147_GenericBoiler/regression/ThermalZones/funnel_comp/AixLib.ThermalZones.HighOrder.Examples.ASHREA140.CompareDynamicAndStaticSolarFrac_Case270.mat_Room.solarRadInRoom.solar_frac_wall[4]/errors.csv b/docs/correct_HTML_issue1147_GenericBoiler/regression/ThermalZones/funnel_comp/AixLib.ThermalZones.HighOrder.Examples.ASHREA140.CompareDynamicAndStaticSolarFrac_Case270.mat_Room.solarRadInRoom.solar_frac_wall[4]/errors.csv new file mode 100644 index 0000000000..9d3b74303d --- /dev/null +++ b/docs/correct_HTML_issue1147_GenericBoiler/regression/ThermalZones/funnel_comp/AixLib.ThermalZones.HighOrder.Examples.ASHREA140.CompareDynamicAndStaticSolarFrac_Case270.mat_Room.solarRadInRoom.solar_frac_wall[4]/errors.csv @@ -0,0 +1,3 @@ +x,y +0,0 +86400,0 diff --git a/docs/correct_HTML_issue1147_GenericBoiler/regression/ThermalZones/funnel_comp/AixLib.ThermalZones.HighOrder.Examples.ASHREA140.CompareDynamicAndStaticSolarFrac_Case270.mat_Room.solarRadInRoom.solar_frac_wall[4]/lowerBound.csv b/docs/correct_HTML_issue1147_GenericBoiler/regression/ThermalZones/funnel_comp/AixLib.ThermalZones.HighOrder.Examples.ASHREA140.CompareDynamicAndStaticSolarFrac_Case270.mat_Room.solarRadInRoom.solar_frac_wall[4]/lowerBound.csv new file mode 100644 index 0000000000..1980e96446 --- /dev/null +++ b/docs/correct_HTML_issue1147_GenericBoiler/regression/ThermalZones/funnel_comp/AixLib.ThermalZones.HighOrder.Examples.ASHREA140.CompareDynamicAndStaticSolarFrac_Case270.mat_Room.solarRadInRoom.solar_frac_wall[4]/lowerBound.csv @@ -0,0 +1,3 @@ +x,y +-0.001,0.01699999922513962 +86400.001,0.01699999922513962 diff --git 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a/docs/correct_HTML_issue1147_GenericBoiler/regression/ThermalZones/funnel_comp/AixLib.ThermalZones.HighOrder.Examples.ASHREA140.CompareDynamicAndStaticSolarFrac_Case270.mat_Room.solarRadInRoom.solar_frac_wall[4]/test.csv b/docs/correct_HTML_issue1147_GenericBoiler/regression/ThermalZones/funnel_comp/AixLib.ThermalZones.HighOrder.Examples.ASHREA140.CompareDynamicAndStaticSolarFrac_Case270.mat_Room.solarRadInRoom.solar_frac_wall[4]/test.csv new file mode 100644 index 0000000000..dd6f1c827a --- /dev/null +++ b/docs/correct_HTML_issue1147_GenericBoiler/regression/ThermalZones/funnel_comp/AixLib.ThermalZones.HighOrder.Examples.ASHREA140.CompareDynamicAndStaticSolarFrac_Case270.mat_Room.solarRadInRoom.solar_frac_wall[4]/test.csv @@ -0,0 +1,3 @@ +x,y +0,0.01799999922513962 +86400,0.01799999922513962 diff --git a/docs/correct_HTML_issue1147_GenericBoiler/regression/ThermalZones/funnel_comp/AixLib.ThermalZones.HighOrder.Examples.ASHREA140.CompareDynamicAndStaticSolarFrac_Case270.mat_Room.solarRadInRoom.solar_frac_wall[4]/upperBound.csv b/docs/correct_HTML_issue1147_GenericBoiler/regression/ThermalZones/funnel_comp/AixLib.ThermalZones.HighOrder.Examples.ASHREA140.CompareDynamicAndStaticSolarFrac_Case270.mat_Room.solarRadInRoom.solar_frac_wall[4]/upperBound.csv new file mode 100644 index 0000000000..93abcd7fd9 --- /dev/null +++ b/docs/correct_HTML_issue1147_GenericBoiler/regression/ThermalZones/funnel_comp/AixLib.ThermalZones.HighOrder.Examples.ASHREA140.CompareDynamicAndStaticSolarFrac_Case270.mat_Room.solarRadInRoom.solar_frac_wall[4]/upperBound.csv @@ -0,0 +1,3 @@ +x,y +-0.001,0.01899999922513962 +86400.001,0.01899999922513962 diff --git a/docs/correct_HTML_issue1147_GenericBoiler/regression/ThermalZones/funnel_comp/AixLib.ThermalZones.HighOrder.Examples.ASHREA140.CompareDynamicAndStaticSolarFrac_Case270.mat_Room.solarRadInRoom.solar_frac_win_abs[1]/errors.csv b/docs/correct_HTML_issue1147_GenericBoiler/regression/ThermalZones/funnel_comp/AixLib.ThermalZones.HighOrder.Examples.ASHREA140.CompareDynamicAndStaticSolarFrac_Case270.mat_Room.solarRadInRoom.solar_frac_win_abs[1]/errors.csv new file mode 100644 index 0000000000..9d3b74303d --- /dev/null +++ b/docs/correct_HTML_issue1147_GenericBoiler/regression/ThermalZones/funnel_comp/AixLib.ThermalZones.HighOrder.Examples.ASHREA140.CompareDynamicAndStaticSolarFrac_Case270.mat_Room.solarRadInRoom.solar_frac_win_abs[1]/errors.csv @@ -0,0 +1,3 @@ +x,y +0,0 +86400,0 diff --git a/docs/correct_HTML_issue1147_GenericBoiler/regression/ThermalZones/funnel_comp/AixLib.ThermalZones.HighOrder.Examples.ASHREA140.CompareDynamicAndStaticSolarFrac_Case270.mat_Room.solarRadInRoom.solar_frac_win_abs[1]/lowerBound.csv b/docs/correct_HTML_issue1147_GenericBoiler/regression/ThermalZones/funnel_comp/AixLib.ThermalZones.HighOrder.Examples.ASHREA140.CompareDynamicAndStaticSolarFrac_Case270.mat_Room.solarRadInRoom.solar_frac_win_abs[1]/lowerBound.csv new file mode 100644 index 0000000000..432043ac38 --- /dev/null +++ b/docs/correct_HTML_issue1147_GenericBoiler/regression/ThermalZones/funnel_comp/AixLib.ThermalZones.HighOrder.Examples.ASHREA140.CompareDynamicAndStaticSolarFrac_Case270.mat_Room.solarRadInRoom.solar_frac_win_abs[1]/lowerBound.csv @@ -0,0 +1,3 @@ +x,y +-0.001,-0.001 +86400.001,-0.001 diff --git a/docs/correct_HTML_issue1147_GenericBoiler/regression/ThermalZones/funnel_comp/AixLib.ThermalZones.HighOrder.Examples.ASHREA140.CompareDynamicAndStaticSolarFrac_Case270.mat_Room.solarRadInRoom.solar_frac_win_abs[1]/reference.csv b/docs/correct_HTML_issue1147_GenericBoiler/regression/ThermalZones/funnel_comp/AixLib.ThermalZones.HighOrder.Examples.ASHREA140.CompareDynamicAndStaticSolarFrac_Case270.mat_Room.solarRadInRoom.solar_frac_win_abs[1]/reference.csv new file mode 100644 index 0000000000..9d3b74303d --- /dev/null +++ b/docs/correct_HTML_issue1147_GenericBoiler/regression/ThermalZones/funnel_comp/AixLib.ThermalZones.HighOrder.Examples.ASHREA140.CompareDynamicAndStaticSolarFrac_Case270.mat_Room.solarRadInRoom.solar_frac_win_abs[1]/reference.csv @@ -0,0 +1,3 @@ +x,y +0,0 +86400,0 diff --git a/docs/correct_HTML_issue1147_GenericBoiler/regression/ThermalZones/funnel_comp/AixLib.ThermalZones.HighOrder.Examples.ASHREA140.CompareDynamicAndStaticSolarFrac_Case270.mat_Room.solarRadInRoom.solar_frac_win_abs[1]/test.csv b/docs/correct_HTML_issue1147_GenericBoiler/regression/ThermalZones/funnel_comp/AixLib.ThermalZones.HighOrder.Examples.ASHREA140.CompareDynamicAndStaticSolarFrac_Case270.mat_Room.solarRadInRoom.solar_frac_win_abs[1]/test.csv new file mode 100644 index 0000000000..9d3b74303d --- /dev/null +++ b/docs/correct_HTML_issue1147_GenericBoiler/regression/ThermalZones/funnel_comp/AixLib.ThermalZones.HighOrder.Examples.ASHREA140.CompareDynamicAndStaticSolarFrac_Case270.mat_Room.solarRadInRoom.solar_frac_win_abs[1]/test.csv @@ -0,0 +1,3 @@ +x,y +0,0 +86400,0 diff --git a/docs/correct_HTML_issue1147_GenericBoiler/regression/ThermalZones/funnel_comp/AixLib.ThermalZones.HighOrder.Examples.ASHREA140.CompareDynamicAndStaticSolarFrac_Case270.mat_Room.solarRadInRoom.solar_frac_win_abs[1]/upperBound.csv b/docs/correct_HTML_issue1147_GenericBoiler/regression/ThermalZones/funnel_comp/AixLib.ThermalZones.HighOrder.Examples.ASHREA140.CompareDynamicAndStaticSolarFrac_Case270.mat_Room.solarRadInRoom.solar_frac_win_abs[1]/upperBound.csv new file mode 100644 index 0000000000..abbb677bde --- /dev/null +++ b/docs/correct_HTML_issue1147_GenericBoiler/regression/ThermalZones/funnel_comp/AixLib.ThermalZones.HighOrder.Examples.ASHREA140.CompareDynamicAndStaticSolarFrac_Case270.mat_Room.solarRadInRoom.solar_frac_win_abs[1]/upperBound.csv @@ -0,0 +1,3 @@ +x,y +-0.001,0.001 +86400.001,0.001 diff --git a/docs/correct_HTML_issue1147_GenericBoiler/regression/ThermalZones/funnel_comp/AixLib.ThermalZones.HighOrder.Examples.ASHREA140.CompareDynamicAndStaticSolarFrac_Case270.mat_Room.solarRadInRoom.solar_frac_win_lost[1]/errors.csv b/docs/correct_HTML_issue1147_GenericBoiler/regression/ThermalZones/funnel_comp/AixLib.ThermalZones.HighOrder.Examples.ASHREA140.CompareDynamicAndStaticSolarFrac_Case270.mat_Room.solarRadInRoom.solar_frac_win_lost[1]/errors.csv new file mode 100644 index 0000000000..9d3b74303d --- /dev/null +++ b/docs/correct_HTML_issue1147_GenericBoiler/regression/ThermalZones/funnel_comp/AixLib.ThermalZones.HighOrder.Examples.ASHREA140.CompareDynamicAndStaticSolarFrac_Case270.mat_Room.solarRadInRoom.solar_frac_win_lost[1]/errors.csv @@ -0,0 +1,3 @@ +x,y +0,0 +86400,0 diff --git a/docs/correct_HTML_issue1147_GenericBoiler/regression/ThermalZones/funnel_comp/AixLib.ThermalZones.HighOrder.Examples.ASHREA140.CompareDynamicAndStaticSolarFrac_Case270.mat_Room.solarRadInRoom.solar_frac_win_lost[1]/lowerBound.csv b/docs/correct_HTML_issue1147_GenericBoiler/regression/ThermalZones/funnel_comp/AixLib.ThermalZones.HighOrder.Examples.ASHREA140.CompareDynamicAndStaticSolarFrac_Case270.mat_Room.solarRadInRoom.solar_frac_win_lost[1]/lowerBound.csv new file mode 100644 index 0000000000..7995551093 --- /dev/null +++ b/docs/correct_HTML_issue1147_GenericBoiler/regression/ThermalZones/funnel_comp/AixLib.ThermalZones.HighOrder.Examples.ASHREA140.CompareDynamicAndStaticSolarFrac_Case270.mat_Room.solarRadInRoom.solar_frac_win_lost[1]/lowerBound.csv @@ -0,0 +1,3 @@ +x,y +-0.001,0.005000000052154064 +86400.001,0.005000000052154064 diff --git a/docs/correct_HTML_issue1147_GenericBoiler/regression/ThermalZones/funnel_comp/AixLib.ThermalZones.HighOrder.Examples.ASHREA140.CompareDynamicAndStaticSolarFrac_Case270.mat_Room.solarRadInRoom.solar_frac_win_lost[1]/reference.csv b/docs/correct_HTML_issue1147_GenericBoiler/regression/ThermalZones/funnel_comp/AixLib.ThermalZones.HighOrder.Examples.ASHREA140.CompareDynamicAndStaticSolarFrac_Case270.mat_Room.solarRadInRoom.solar_frac_win_lost[1]/reference.csv new file mode 100644 index 0000000000..148a587dce --- /dev/null +++ b/docs/correct_HTML_issue1147_GenericBoiler/regression/ThermalZones/funnel_comp/AixLib.ThermalZones.HighOrder.Examples.ASHREA140.CompareDynamicAndStaticSolarFrac_Case270.mat_Room.solarRadInRoom.solar_frac_win_lost[1]/reference.csv @@ -0,0 +1,3 @@ +x,y +0,0.006000000052154064 +86400,0.006000000052154064 diff --git a/docs/correct_HTML_issue1147_GenericBoiler/regression/ThermalZones/funnel_comp/AixLib.ThermalZones.HighOrder.Examples.ASHREA140.CompareDynamicAndStaticSolarFrac_Case270.mat_Room.solarRadInRoom.solar_frac_win_lost[1]/test.csv b/docs/correct_HTML_issue1147_GenericBoiler/regression/ThermalZones/funnel_comp/AixLib.ThermalZones.HighOrder.Examples.ASHREA140.CompareDynamicAndStaticSolarFrac_Case270.mat_Room.solarRadInRoom.solar_frac_win_lost[1]/test.csv new file mode 100644 index 0000000000..148a587dce --- /dev/null +++ b/docs/correct_HTML_issue1147_GenericBoiler/regression/ThermalZones/funnel_comp/AixLib.ThermalZones.HighOrder.Examples.ASHREA140.CompareDynamicAndStaticSolarFrac_Case270.mat_Room.solarRadInRoom.solar_frac_win_lost[1]/test.csv @@ -0,0 +1,3 @@ +x,y +0,0.006000000052154064 +86400,0.006000000052154064 diff --git a/docs/correct_HTML_issue1147_GenericBoiler/regression/ThermalZones/funnel_comp/AixLib.ThermalZones.HighOrder.Examples.ASHREA140.CompareDynamicAndStaticSolarFrac_Case270.mat_Room.solarRadInRoom.solar_frac_win_lost[1]/upperBound.csv b/docs/correct_HTML_issue1147_GenericBoiler/regression/ThermalZones/funnel_comp/AixLib.ThermalZones.HighOrder.Examples.ASHREA140.CompareDynamicAndStaticSolarFrac_Case270.mat_Room.solarRadInRoom.solar_frac_win_lost[1]/upperBound.csv new file mode 100644 index 0000000000..4eaffeba54 --- /dev/null +++ b/docs/correct_HTML_issue1147_GenericBoiler/regression/ThermalZones/funnel_comp/AixLib.ThermalZones.HighOrder.Examples.ASHREA140.CompareDynamicAndStaticSolarFrac_Case270.mat_Room.solarRadInRoom.solar_frac_win_lost[1]/upperBound.csv @@ -0,0 +1,3 @@ +x,y +-0.001,0.007000000052154064 +86400.001,0.007000000052154064 diff --git a/docs/correct_HTML_issue1147_GenericBoiler/regression/ThermalZones/funnel_comp/AixLib.ThermalZones.HighOrder.Examples.ASHREA140.CompareDynamicAndStaticSolarFrac_Case270.mat_Room_dyn.solarRadInRoom.solar_frac_cei[1]/errors.csv b/docs/correct_HTML_issue1147_GenericBoiler/regression/ThermalZones/funnel_comp/AixLib.ThermalZones.HighOrder.Examples.ASHREA140.CompareDynamicAndStaticSolarFrac_Case270.mat_Room_dyn.solarRadInRoom.solar_frac_cei[1]/errors.csv new file mode 100644 index 0000000000..9d3b74303d --- /dev/null +++ b/docs/correct_HTML_issue1147_GenericBoiler/regression/ThermalZones/funnel_comp/AixLib.ThermalZones.HighOrder.Examples.ASHREA140.CompareDynamicAndStaticSolarFrac_Case270.mat_Room_dyn.solarRadInRoom.solar_frac_cei[1]/errors.csv @@ -0,0 +1,3 @@ +x,y +0,0 +86400,0 diff --git a/docs/correct_HTML_issue1147_GenericBoiler/regression/ThermalZones/funnel_comp/AixLib.ThermalZones.HighOrder.Examples.ASHREA140.CompareDynamicAndStaticSolarFrac_Case270.mat_Room_dyn.solarRadInRoom.solar_frac_cei[1]/lowerBound.csv b/docs/correct_HTML_issue1147_GenericBoiler/regression/ThermalZones/funnel_comp/AixLib.ThermalZones.HighOrder.Examples.ASHREA140.CompareDynamicAndStaticSolarFrac_Case270.mat_Room_dyn.solarRadInRoom.solar_frac_cei[1]/lowerBound.csv new file mode 100644 index 0000000000..ab942665d0 --- /dev/null +++ b/docs/correct_HTML_issue1147_GenericBoiler/regression/ThermalZones/funnel_comp/AixLib.ThermalZones.HighOrder.Examples.ASHREA140.CompareDynamicAndStaticSolarFrac_Case270.mat_Room_dyn.solarRadInRoom.solar_frac_cei[1]/lowerBound.csv @@ -0,0 +1,3 @@ +x,y +-0.001,0.05011178755760193 +86400.001,0.05011178755760193 diff --git a/docs/correct_HTML_issue1147_GenericBoiler/regression/ThermalZones/funnel_comp/AixLib.ThermalZones.HighOrder.Examples.ASHREA140.CompareDynamicAndStaticSolarFrac_Case270.mat_Room_dyn.solarRadInRoom.solar_frac_cei[1]/reference.csv b/docs/correct_HTML_issue1147_GenericBoiler/regression/ThermalZones/funnel_comp/AixLib.ThermalZones.HighOrder.Examples.ASHREA140.CompareDynamicAndStaticSolarFrac_Case270.mat_Room_dyn.solarRadInRoom.solar_frac_cei[1]/reference.csv new file mode 100644 index 0000000000..3dc20c1b96 --- /dev/null +++ b/docs/correct_HTML_issue1147_GenericBoiler/regression/ThermalZones/funnel_comp/AixLib.ThermalZones.HighOrder.Examples.ASHREA140.CompareDynamicAndStaticSolarFrac_Case270.mat_Room_dyn.solarRadInRoom.solar_frac_cei[1]/reference.csv @@ -0,0 +1,3 @@ +x,y +0,0.05111178755760193 +86400,0.05111178755760193 diff --git a/docs/correct_HTML_issue1147_GenericBoiler/regression/ThermalZones/funnel_comp/AixLib.ThermalZones.HighOrder.Examples.ASHREA140.CompareDynamicAndStaticSolarFrac_Case270.mat_Room_dyn.solarRadInRoom.solar_frac_cei[1]/test.csv b/docs/correct_HTML_issue1147_GenericBoiler/regression/ThermalZones/funnel_comp/AixLib.ThermalZones.HighOrder.Examples.ASHREA140.CompareDynamicAndStaticSolarFrac_Case270.mat_Room_dyn.solarRadInRoom.solar_frac_cei[1]/test.csv new file mode 100644 index 0000000000..3dc20c1b96 --- /dev/null +++ b/docs/correct_HTML_issue1147_GenericBoiler/regression/ThermalZones/funnel_comp/AixLib.ThermalZones.HighOrder.Examples.ASHREA140.CompareDynamicAndStaticSolarFrac_Case270.mat_Room_dyn.solarRadInRoom.solar_frac_cei[1]/test.csv @@ -0,0 +1,3 @@ +x,y +0,0.05111178755760193 +86400,0.05111178755760193 diff --git a/docs/correct_HTML_issue1147_GenericBoiler/regression/ThermalZones/funnel_comp/AixLib.ThermalZones.HighOrder.Examples.ASHREA140.CompareDynamicAndStaticSolarFrac_Case270.mat_Room_dyn.solarRadInRoom.solar_frac_cei[1]/upperBound.csv b/docs/correct_HTML_issue1147_GenericBoiler/regression/ThermalZones/funnel_comp/AixLib.ThermalZones.HighOrder.Examples.ASHREA140.CompareDynamicAndStaticSolarFrac_Case270.mat_Room_dyn.solarRadInRoom.solar_frac_cei[1]/upperBound.csv new file mode 100644 index 0000000000..f0bb9c1a3a --- /dev/null +++ b/docs/correct_HTML_issue1147_GenericBoiler/regression/ThermalZones/funnel_comp/AixLib.ThermalZones.HighOrder.Examples.ASHREA140.CompareDynamicAndStaticSolarFrac_Case270.mat_Room_dyn.solarRadInRoom.solar_frac_cei[1]/upperBound.csv @@ -0,0 +1,3 @@ +x,y +-0.001,0.05211178755760193 +86400.001,0.05211178755760193 diff --git a/docs/correct_HTML_issue1147_GenericBoiler/regression/ThermalZones/funnel_comp/AixLib.ThermalZones.HighOrder.Examples.ASHREA140.CompareDynamicAndStaticSolarFrac_Case270.mat_Room_dyn.solarRadInRoom.solar_frac_flo[1]/errors.csv b/docs/correct_HTML_issue1147_GenericBoiler/regression/ThermalZones/funnel_comp/AixLib.ThermalZones.HighOrder.Examples.ASHREA140.CompareDynamicAndStaticSolarFrac_Case270.mat_Room_dyn.solarRadInRoom.solar_frac_flo[1]/errors.csv new file mode 100644 index 0000000000..9d3b74303d --- /dev/null +++ b/docs/correct_HTML_issue1147_GenericBoiler/regression/ThermalZones/funnel_comp/AixLib.ThermalZones.HighOrder.Examples.ASHREA140.CompareDynamicAndStaticSolarFrac_Case270.mat_Room_dyn.solarRadInRoom.solar_frac_flo[1]/errors.csv @@ -0,0 +1,3 @@ +x,y +0,0 +86400,0 diff --git a/docs/correct_HTML_issue1147_GenericBoiler/regression/ThermalZones/funnel_comp/AixLib.ThermalZones.HighOrder.Examples.ASHREA140.CompareDynamicAndStaticSolarFrac_Case270.mat_Room_dyn.solarRadInRoom.solar_frac_flo[1]/lowerBound.csv b/docs/correct_HTML_issue1147_GenericBoiler/regression/ThermalZones/funnel_comp/AixLib.ThermalZones.HighOrder.Examples.ASHREA140.CompareDynamicAndStaticSolarFrac_Case270.mat_Room_dyn.solarRadInRoom.solar_frac_flo[1]/lowerBound.csv new file mode 100644 index 0000000000..27b997977d --- /dev/null +++ b/docs/correct_HTML_issue1147_GenericBoiler/regression/ThermalZones/funnel_comp/AixLib.ThermalZones.HighOrder.Examples.ASHREA140.CompareDynamicAndStaticSolarFrac_Case270.mat_Room_dyn.solarRadInRoom.solar_frac_flo[1]/lowerBound.csv @@ -0,0 +1,3 @@ +x,y +-0.001,0.9014140238761902 +86400.001,0.9014140238761902 diff --git a/docs/correct_HTML_issue1147_GenericBoiler/regression/ThermalZones/funnel_comp/AixLib.ThermalZones.HighOrder.Examples.ASHREA140.CompareDynamicAndStaticSolarFrac_Case270.mat_Room_dyn.solarRadInRoom.solar_frac_flo[1]/reference.csv b/docs/correct_HTML_issue1147_GenericBoiler/regression/ThermalZones/funnel_comp/AixLib.ThermalZones.HighOrder.Examples.ASHREA140.CompareDynamicAndStaticSolarFrac_Case270.mat_Room_dyn.solarRadInRoom.solar_frac_flo[1]/reference.csv new file mode 100644 index 0000000000..3eba136e8d --- /dev/null +++ b/docs/correct_HTML_issue1147_GenericBoiler/regression/ThermalZones/funnel_comp/AixLib.ThermalZones.HighOrder.Examples.ASHREA140.CompareDynamicAndStaticSolarFrac_Case270.mat_Room_dyn.solarRadInRoom.solar_frac_flo[1]/reference.csv @@ -0,0 +1,3 @@ +x,y +0,0.9024140238761902 +86400,0.9024140238761902 diff --git a/docs/correct_HTML_issue1147_GenericBoiler/regression/ThermalZones/funnel_comp/AixLib.ThermalZones.HighOrder.Examples.ASHREA140.CompareDynamicAndStaticSolarFrac_Case270.mat_Room_dyn.solarRadInRoom.solar_frac_flo[1]/test.csv b/docs/correct_HTML_issue1147_GenericBoiler/regression/ThermalZones/funnel_comp/AixLib.ThermalZones.HighOrder.Examples.ASHREA140.CompareDynamicAndStaticSolarFrac_Case270.mat_Room_dyn.solarRadInRoom.solar_frac_flo[1]/test.csv new file mode 100644 index 0000000000..3eba136e8d --- /dev/null +++ b/docs/correct_HTML_issue1147_GenericBoiler/regression/ThermalZones/funnel_comp/AixLib.ThermalZones.HighOrder.Examples.ASHREA140.CompareDynamicAndStaticSolarFrac_Case270.mat_Room_dyn.solarRadInRoom.solar_frac_flo[1]/test.csv @@ -0,0 +1,3 @@ +x,y +0,0.9024140238761902 +86400,0.9024140238761902 diff --git a/docs/correct_HTML_issue1147_GenericBoiler/regression/ThermalZones/funnel_comp/AixLib.ThermalZones.HighOrder.Examples.ASHREA140.CompareDynamicAndStaticSolarFrac_Case270.mat_Room_dyn.solarRadInRoom.solar_frac_flo[1]/upperBound.csv b/docs/correct_HTML_issue1147_GenericBoiler/regression/ThermalZones/funnel_comp/AixLib.ThermalZones.HighOrder.Examples.ASHREA140.CompareDynamicAndStaticSolarFrac_Case270.mat_Room_dyn.solarRadInRoom.solar_frac_flo[1]/upperBound.csv new file mode 100644 index 0000000000..1e74eeb366 --- /dev/null +++ b/docs/correct_HTML_issue1147_GenericBoiler/regression/ThermalZones/funnel_comp/AixLib.ThermalZones.HighOrder.Examples.ASHREA140.CompareDynamicAndStaticSolarFrac_Case270.mat_Room_dyn.solarRadInRoom.solar_frac_flo[1]/upperBound.csv @@ -0,0 +1,3 @@ +x,y +-0.001,0.9034140238761902 +86400.001,0.9034140238761902 diff --git a/docs/correct_HTML_issue1147_GenericBoiler/regression/ThermalZones/funnel_comp/AixLib.ThermalZones.HighOrder.Examples.ASHREA140.CompareDynamicAndStaticSolarFrac_Case270.mat_Room_dyn.solarRadInRoom.solar_frac_wall[1]/errors.csv b/docs/correct_HTML_issue1147_GenericBoiler/regression/ThermalZones/funnel_comp/AixLib.ThermalZones.HighOrder.Examples.ASHREA140.CompareDynamicAndStaticSolarFrac_Case270.mat_Room_dyn.solarRadInRoom.solar_frac_wall[1]/errors.csv new file mode 100644 index 0000000000..9d3b74303d --- /dev/null +++ b/docs/correct_HTML_issue1147_GenericBoiler/regression/ThermalZones/funnel_comp/AixLib.ThermalZones.HighOrder.Examples.ASHREA140.CompareDynamicAndStaticSolarFrac_Case270.mat_Room_dyn.solarRadInRoom.solar_frac_wall[1]/errors.csv @@ -0,0 +1,3 @@ +x,y +0,0 +86400,0 diff --git a/docs/correct_HTML_issue1147_GenericBoiler/regression/ThermalZones/funnel_comp/AixLib.ThermalZones.HighOrder.Examples.ASHREA140.CompareDynamicAndStaticSolarFrac_Case270.mat_Room_dyn.solarRadInRoom.solar_frac_wall[1]/lowerBound.csv b/docs/correct_HTML_issue1147_GenericBoiler/regression/ThermalZones/funnel_comp/AixLib.ThermalZones.HighOrder.Examples.ASHREA140.CompareDynamicAndStaticSolarFrac_Case270.mat_Room_dyn.solarRadInRoom.solar_frac_wall[1]/lowerBound.csv new file mode 100644 index 0000000000..97622c3c31 --- /dev/null +++ b/docs/correct_HTML_issue1147_GenericBoiler/regression/ThermalZones/funnel_comp/AixLib.ThermalZones.HighOrder.Examples.ASHREA140.CompareDynamicAndStaticSolarFrac_Case270.mat_Room_dyn.solarRadInRoom.solar_frac_wall[1]/lowerBound.csv @@ -0,0 +1,3 @@ +x,y +-0.001,0.007452805690467358 +86400.001,0.007452805690467358 diff --git a/docs/correct_HTML_issue1147_GenericBoiler/regression/ThermalZones/funnel_comp/AixLib.ThermalZones.HighOrder.Examples.ASHREA140.CompareDynamicAndStaticSolarFrac_Case270.mat_Room_dyn.solarRadInRoom.solar_frac_wall[1]/reference.csv b/docs/correct_HTML_issue1147_GenericBoiler/regression/ThermalZones/funnel_comp/AixLib.ThermalZones.HighOrder.Examples.ASHREA140.CompareDynamicAndStaticSolarFrac_Case270.mat_Room_dyn.solarRadInRoom.solar_frac_wall[1]/reference.csv new file mode 100644 index 0000000000..f764606a52 --- /dev/null +++ b/docs/correct_HTML_issue1147_GenericBoiler/regression/ThermalZones/funnel_comp/AixLib.ThermalZones.HighOrder.Examples.ASHREA140.CompareDynamicAndStaticSolarFrac_Case270.mat_Room_dyn.solarRadInRoom.solar_frac_wall[1]/reference.csv @@ -0,0 +1,3 @@ +x,y +0,0.008452805690467358 +86400,0.008452805690467358 diff --git a/docs/correct_HTML_issue1147_GenericBoiler/regression/ThermalZones/funnel_comp/AixLib.ThermalZones.HighOrder.Examples.ASHREA140.CompareDynamicAndStaticSolarFrac_Case270.mat_Room_dyn.solarRadInRoom.solar_frac_wall[1]/test.csv b/docs/correct_HTML_issue1147_GenericBoiler/regression/ThermalZones/funnel_comp/AixLib.ThermalZones.HighOrder.Examples.ASHREA140.CompareDynamicAndStaticSolarFrac_Case270.mat_Room_dyn.solarRadInRoom.solar_frac_wall[1]/test.csv new file mode 100644 index 0000000000..f764606a52 --- /dev/null +++ b/docs/correct_HTML_issue1147_GenericBoiler/regression/ThermalZones/funnel_comp/AixLib.ThermalZones.HighOrder.Examples.ASHREA140.CompareDynamicAndStaticSolarFrac_Case270.mat_Room_dyn.solarRadInRoom.solar_frac_wall[1]/test.csv @@ -0,0 +1,3 @@ +x,y +0,0.008452805690467358 +86400,0.008452805690467358 diff --git a/docs/correct_HTML_issue1147_GenericBoiler/regression/ThermalZones/funnel_comp/AixLib.ThermalZones.HighOrder.Examples.ASHREA140.CompareDynamicAndStaticSolarFrac_Case270.mat_Room_dyn.solarRadInRoom.solar_frac_wall[1]/upperBound.csv b/docs/correct_HTML_issue1147_GenericBoiler/regression/ThermalZones/funnel_comp/AixLib.ThermalZones.HighOrder.Examples.ASHREA140.CompareDynamicAndStaticSolarFrac_Case270.mat_Room_dyn.solarRadInRoom.solar_frac_wall[1]/upperBound.csv new file mode 100644 index 0000000000..3a92383a99 --- /dev/null +++ b/docs/correct_HTML_issue1147_GenericBoiler/regression/ThermalZones/funnel_comp/AixLib.ThermalZones.HighOrder.Examples.ASHREA140.CompareDynamicAndStaticSolarFrac_Case270.mat_Room_dyn.solarRadInRoom.solar_frac_wall[1]/upperBound.csv @@ -0,0 +1,3 @@ +x,y +-0.001,0.009452805690467359 +86400.001,0.009452805690467359 diff --git a/docs/correct_HTML_issue1147_GenericBoiler/regression/ThermalZones/funnel_comp/AixLib.ThermalZones.HighOrder.Examples.ASHREA140.CompareDynamicAndStaticSolarFrac_Case270.mat_Room_dyn.solarRadInRoom.solar_frac_wall[2]/errors.csv b/docs/correct_HTML_issue1147_GenericBoiler/regression/ThermalZones/funnel_comp/AixLib.ThermalZones.HighOrder.Examples.ASHREA140.CompareDynamicAndStaticSolarFrac_Case270.mat_Room_dyn.solarRadInRoom.solar_frac_wall[2]/errors.csv new file mode 100644 index 0000000000..9d3b74303d --- /dev/null +++ b/docs/correct_HTML_issue1147_GenericBoiler/regression/ThermalZones/funnel_comp/AixLib.ThermalZones.HighOrder.Examples.ASHREA140.CompareDynamicAndStaticSolarFrac_Case270.mat_Room_dyn.solarRadInRoom.solar_frac_wall[2]/errors.csv @@ -0,0 +1,3 @@ +x,y +0,0 +86400,0 diff --git a/docs/correct_HTML_issue1147_GenericBoiler/regression/ThermalZones/funnel_comp/AixLib.ThermalZones.HighOrder.Examples.ASHREA140.CompareDynamicAndStaticSolarFrac_Case270.mat_Room_dyn.solarRadInRoom.solar_frac_wall[2]/lowerBound.csv b/docs/correct_HTML_issue1147_GenericBoiler/regression/ThermalZones/funnel_comp/AixLib.ThermalZones.HighOrder.Examples.ASHREA140.CompareDynamicAndStaticSolarFrac_Case270.mat_Room_dyn.solarRadInRoom.solar_frac_wall[2]/lowerBound.csv new file mode 100644 index 0000000000..20e6e451d9 --- /dev/null +++ b/docs/correct_HTML_issue1147_GenericBoiler/regression/ThermalZones/funnel_comp/AixLib.ThermalZones.HighOrder.Examples.ASHREA140.CompareDynamicAndStaticSolarFrac_Case270.mat_Room_dyn.solarRadInRoom.solar_frac_wall[2]/lowerBound.csv @@ -0,0 +1,3 @@ +x,y +-0.001,0.01027040758728981 +86400.001,0.01027040758728981 diff --git a/docs/correct_HTML_issue1147_GenericBoiler/regression/ThermalZones/funnel_comp/AixLib.ThermalZones.HighOrder.Examples.ASHREA140.CompareDynamicAndStaticSolarFrac_Case270.mat_Room_dyn.solarRadInRoom.solar_frac_wall[2]/reference.csv b/docs/correct_HTML_issue1147_GenericBoiler/regression/ThermalZones/funnel_comp/AixLib.ThermalZones.HighOrder.Examples.ASHREA140.CompareDynamicAndStaticSolarFrac_Case270.mat_Room_dyn.solarRadInRoom.solar_frac_wall[2]/reference.csv new file mode 100644 index 0000000000..51a56ddfc2 --- /dev/null +++ b/docs/correct_HTML_issue1147_GenericBoiler/regression/ThermalZones/funnel_comp/AixLib.ThermalZones.HighOrder.Examples.ASHREA140.CompareDynamicAndStaticSolarFrac_Case270.mat_Room_dyn.solarRadInRoom.solar_frac_wall[2]/reference.csv @@ -0,0 +1,3 @@ +x,y +0,0.01127040758728981 +86400,0.01127040758728981 diff --git a/docs/correct_HTML_issue1147_GenericBoiler/regression/ThermalZones/funnel_comp/AixLib.ThermalZones.HighOrder.Examples.ASHREA140.CompareDynamicAndStaticSolarFrac_Case270.mat_Room_dyn.solarRadInRoom.solar_frac_wall[2]/test.csv b/docs/correct_HTML_issue1147_GenericBoiler/regression/ThermalZones/funnel_comp/AixLib.ThermalZones.HighOrder.Examples.ASHREA140.CompareDynamicAndStaticSolarFrac_Case270.mat_Room_dyn.solarRadInRoom.solar_frac_wall[2]/test.csv new file mode 100644 index 0000000000..51a56ddfc2 --- /dev/null +++ b/docs/correct_HTML_issue1147_GenericBoiler/regression/ThermalZones/funnel_comp/AixLib.ThermalZones.HighOrder.Examples.ASHREA140.CompareDynamicAndStaticSolarFrac_Case270.mat_Room_dyn.solarRadInRoom.solar_frac_wall[2]/test.csv @@ -0,0 +1,3 @@ +x,y +0,0.01127040758728981 +86400,0.01127040758728981 diff --git a/docs/correct_HTML_issue1147_GenericBoiler/regression/ThermalZones/funnel_comp/AixLib.ThermalZones.HighOrder.Examples.ASHREA140.CompareDynamicAndStaticSolarFrac_Case270.mat_Room_dyn.solarRadInRoom.solar_frac_wall[2]/upperBound.csv b/docs/correct_HTML_issue1147_GenericBoiler/regression/ThermalZones/funnel_comp/AixLib.ThermalZones.HighOrder.Examples.ASHREA140.CompareDynamicAndStaticSolarFrac_Case270.mat_Room_dyn.solarRadInRoom.solar_frac_wall[2]/upperBound.csv new file mode 100644 index 0000000000..cc886b6cc5 --- /dev/null +++ b/docs/correct_HTML_issue1147_GenericBoiler/regression/ThermalZones/funnel_comp/AixLib.ThermalZones.HighOrder.Examples.ASHREA140.CompareDynamicAndStaticSolarFrac_Case270.mat_Room_dyn.solarRadInRoom.solar_frac_wall[2]/upperBound.csv @@ -0,0 +1,3 @@ +x,y +-0.001,0.01227040758728981 +86400.001,0.01227040758728981 diff --git a/docs/correct_HTML_issue1147_GenericBoiler/regression/ThermalZones/funnel_comp/AixLib.ThermalZones.HighOrder.Examples.ASHREA140.CompareDynamicAndStaticSolarFrac_Case270.mat_Room_dyn.solarRadInRoom.solar_frac_wall[3]/errors.csv b/docs/correct_HTML_issue1147_GenericBoiler/regression/ThermalZones/funnel_comp/AixLib.ThermalZones.HighOrder.Examples.ASHREA140.CompareDynamicAndStaticSolarFrac_Case270.mat_Room_dyn.solarRadInRoom.solar_frac_wall[3]/errors.csv new file mode 100644 index 0000000000..9d3b74303d --- /dev/null +++ b/docs/correct_HTML_issue1147_GenericBoiler/regression/ThermalZones/funnel_comp/AixLib.ThermalZones.HighOrder.Examples.ASHREA140.CompareDynamicAndStaticSolarFrac_Case270.mat_Room_dyn.solarRadInRoom.solar_frac_wall[3]/errors.csv @@ -0,0 +1,3 @@ +x,y +0,0 +86400,0 diff --git a/docs/correct_HTML_issue1147_GenericBoiler/regression/ThermalZones/funnel_comp/AixLib.ThermalZones.HighOrder.Examples.ASHREA140.CompareDynamicAndStaticSolarFrac_Case270.mat_Room_dyn.solarRadInRoom.solar_frac_wall[3]/lowerBound.csv b/docs/correct_HTML_issue1147_GenericBoiler/regression/ThermalZones/funnel_comp/AixLib.ThermalZones.HighOrder.Examples.ASHREA140.CompareDynamicAndStaticSolarFrac_Case270.mat_Room_dyn.solarRadInRoom.solar_frac_wall[3]/lowerBound.csv new file mode 100644 index 0000000000..97622c3c31 --- /dev/null +++ b/docs/correct_HTML_issue1147_GenericBoiler/regression/ThermalZones/funnel_comp/AixLib.ThermalZones.HighOrder.Examples.ASHREA140.CompareDynamicAndStaticSolarFrac_Case270.mat_Room_dyn.solarRadInRoom.solar_frac_wall[3]/lowerBound.csv @@ -0,0 +1,3 @@ +x,y +-0.001,0.007452805690467358 +86400.001,0.007452805690467358 diff --git a/docs/correct_HTML_issue1147_GenericBoiler/regression/ThermalZones/funnel_comp/AixLib.ThermalZones.HighOrder.Examples.ASHREA140.CompareDynamicAndStaticSolarFrac_Case270.mat_Room_dyn.solarRadInRoom.solar_frac_wall[3]/reference.csv b/docs/correct_HTML_issue1147_GenericBoiler/regression/ThermalZones/funnel_comp/AixLib.ThermalZones.HighOrder.Examples.ASHREA140.CompareDynamicAndStaticSolarFrac_Case270.mat_Room_dyn.solarRadInRoom.solar_frac_wall[3]/reference.csv new file mode 100644 index 0000000000..f764606a52 --- /dev/null +++ b/docs/correct_HTML_issue1147_GenericBoiler/regression/ThermalZones/funnel_comp/AixLib.ThermalZones.HighOrder.Examples.ASHREA140.CompareDynamicAndStaticSolarFrac_Case270.mat_Room_dyn.solarRadInRoom.solar_frac_wall[3]/reference.csv @@ -0,0 +1,3 @@ +x,y +0,0.008452805690467358 +86400,0.008452805690467358 diff --git a/docs/correct_HTML_issue1147_GenericBoiler/regression/ThermalZones/funnel_comp/AixLib.ThermalZones.HighOrder.Examples.ASHREA140.CompareDynamicAndStaticSolarFrac_Case270.mat_Room_dyn.solarRadInRoom.solar_frac_wall[3]/test.csv b/docs/correct_HTML_issue1147_GenericBoiler/regression/ThermalZones/funnel_comp/AixLib.ThermalZones.HighOrder.Examples.ASHREA140.CompareDynamicAndStaticSolarFrac_Case270.mat_Room_dyn.solarRadInRoom.solar_frac_wall[3]/test.csv new file mode 100644 index 0000000000..f764606a52 --- /dev/null +++ b/docs/correct_HTML_issue1147_GenericBoiler/regression/ThermalZones/funnel_comp/AixLib.ThermalZones.HighOrder.Examples.ASHREA140.CompareDynamicAndStaticSolarFrac_Case270.mat_Room_dyn.solarRadInRoom.solar_frac_wall[3]/test.csv @@ -0,0 +1,3 @@ +x,y +0,0.008452805690467358 +86400,0.008452805690467358 diff --git a/docs/correct_HTML_issue1147_GenericBoiler/regression/ThermalZones/funnel_comp/AixLib.ThermalZones.HighOrder.Examples.ASHREA140.CompareDynamicAndStaticSolarFrac_Case270.mat_Room_dyn.solarRadInRoom.solar_frac_wall[3]/upperBound.csv b/docs/correct_HTML_issue1147_GenericBoiler/regression/ThermalZones/funnel_comp/AixLib.ThermalZones.HighOrder.Examples.ASHREA140.CompareDynamicAndStaticSolarFrac_Case270.mat_Room_dyn.solarRadInRoom.solar_frac_wall[3]/upperBound.csv new file mode 100644 index 0000000000..3a92383a99 --- /dev/null +++ b/docs/correct_HTML_issue1147_GenericBoiler/regression/ThermalZones/funnel_comp/AixLib.ThermalZones.HighOrder.Examples.ASHREA140.CompareDynamicAndStaticSolarFrac_Case270.mat_Room_dyn.solarRadInRoom.solar_frac_wall[3]/upperBound.csv @@ -0,0 +1,3 @@ +x,y +-0.001,0.009452805690467359 +86400.001,0.009452805690467359 diff --git a/docs/correct_HTML_issue1147_GenericBoiler/regression/ThermalZones/funnel_comp/AixLib.ThermalZones.HighOrder.Examples.ASHREA140.CompareDynamicAndStaticSolarFrac_Case270.mat_Room_dyn.solarRadInRoom.solar_frac_wall[4]/errors.csv b/docs/correct_HTML_issue1147_GenericBoiler/regression/ThermalZones/funnel_comp/AixLib.ThermalZones.HighOrder.Examples.ASHREA140.CompareDynamicAndStaticSolarFrac_Case270.mat_Room_dyn.solarRadInRoom.solar_frac_wall[4]/errors.csv new file mode 100644 index 0000000000..9d3b74303d --- /dev/null +++ b/docs/correct_HTML_issue1147_GenericBoiler/regression/ThermalZones/funnel_comp/AixLib.ThermalZones.HighOrder.Examples.ASHREA140.CompareDynamicAndStaticSolarFrac_Case270.mat_Room_dyn.solarRadInRoom.solar_frac_wall[4]/errors.csv @@ -0,0 +1,3 @@ +x,y +0,0 +86400,0 diff --git a/docs/correct_HTML_issue1147_GenericBoiler/regression/ThermalZones/funnel_comp/AixLib.ThermalZones.HighOrder.Examples.ASHREA140.CompareDynamicAndStaticSolarFrac_Case270.mat_Room_dyn.solarRadInRoom.solar_frac_wall[4]/lowerBound.csv b/docs/correct_HTML_issue1147_GenericBoiler/regression/ThermalZones/funnel_comp/AixLib.ThermalZones.HighOrder.Examples.ASHREA140.CompareDynamicAndStaticSolarFrac_Case270.mat_Room_dyn.solarRadInRoom.solar_frac_wall[4]/lowerBound.csv new file mode 100644 index 0000000000..20e6e451d9 --- /dev/null +++ b/docs/correct_HTML_issue1147_GenericBoiler/regression/ThermalZones/funnel_comp/AixLib.ThermalZones.HighOrder.Examples.ASHREA140.CompareDynamicAndStaticSolarFrac_Case270.mat_Room_dyn.solarRadInRoom.solar_frac_wall[4]/lowerBound.csv @@ -0,0 +1,3 @@ +x,y +-0.001,0.01027040758728981 +86400.001,0.01027040758728981 diff --git a/docs/correct_HTML_issue1147_GenericBoiler/regression/ThermalZones/funnel_comp/AixLib.ThermalZones.HighOrder.Examples.ASHREA140.CompareDynamicAndStaticSolarFrac_Case270.mat_Room_dyn.solarRadInRoom.solar_frac_wall[4]/reference.csv b/docs/correct_HTML_issue1147_GenericBoiler/regression/ThermalZones/funnel_comp/AixLib.ThermalZones.HighOrder.Examples.ASHREA140.CompareDynamicAndStaticSolarFrac_Case270.mat_Room_dyn.solarRadInRoom.solar_frac_wall[4]/reference.csv new file mode 100644 index 0000000000..51a56ddfc2 --- /dev/null +++ b/docs/correct_HTML_issue1147_GenericBoiler/regression/ThermalZones/funnel_comp/AixLib.ThermalZones.HighOrder.Examples.ASHREA140.CompareDynamicAndStaticSolarFrac_Case270.mat_Room_dyn.solarRadInRoom.solar_frac_wall[4]/reference.csv @@ -0,0 +1,3 @@ +x,y +0,0.01127040758728981 +86400,0.01127040758728981 diff --git a/docs/correct_HTML_issue1147_GenericBoiler/regression/ThermalZones/funnel_comp/AixLib.ThermalZones.HighOrder.Examples.ASHREA140.CompareDynamicAndStaticSolarFrac_Case270.mat_Room_dyn.solarRadInRoom.solar_frac_wall[4]/test.csv b/docs/correct_HTML_issue1147_GenericBoiler/regression/ThermalZones/funnel_comp/AixLib.ThermalZones.HighOrder.Examples.ASHREA140.CompareDynamicAndStaticSolarFrac_Case270.mat_Room_dyn.solarRadInRoom.solar_frac_wall[4]/test.csv new file mode 100644 index 0000000000..51a56ddfc2 --- /dev/null +++ b/docs/correct_HTML_issue1147_GenericBoiler/regression/ThermalZones/funnel_comp/AixLib.ThermalZones.HighOrder.Examples.ASHREA140.CompareDynamicAndStaticSolarFrac_Case270.mat_Room_dyn.solarRadInRoom.solar_frac_wall[4]/test.csv @@ -0,0 +1,3 @@ +x,y +0,0.01127040758728981 +86400,0.01127040758728981 diff --git a/docs/correct_HTML_issue1147_GenericBoiler/regression/ThermalZones/funnel_comp/AixLib.ThermalZones.HighOrder.Examples.ASHREA140.CompareDynamicAndStaticSolarFrac_Case270.mat_Room_dyn.solarRadInRoom.solar_frac_wall[4]/upperBound.csv b/docs/correct_HTML_issue1147_GenericBoiler/regression/ThermalZones/funnel_comp/AixLib.ThermalZones.HighOrder.Examples.ASHREA140.CompareDynamicAndStaticSolarFrac_Case270.mat_Room_dyn.solarRadInRoom.solar_frac_wall[4]/upperBound.csv new file mode 100644 index 0000000000..cc886b6cc5 --- /dev/null +++ b/docs/correct_HTML_issue1147_GenericBoiler/regression/ThermalZones/funnel_comp/AixLib.ThermalZones.HighOrder.Examples.ASHREA140.CompareDynamicAndStaticSolarFrac_Case270.mat_Room_dyn.solarRadInRoom.solar_frac_wall[4]/upperBound.csv @@ -0,0 +1,3 @@ +x,y +-0.001,0.01227040758728981 +86400.001,0.01227040758728981 diff --git a/docs/correct_HTML_issue1147_GenericBoiler/regression/ThermalZones/funnel_comp/AixLib.ThermalZones.HighOrder.Examples.ASHREA140.CompareDynamicAndStaticSolarFrac_Case270.mat_Room_dyn.solarRadInRoom.solar_frac_win_abs[1]/errors.csv b/docs/correct_HTML_issue1147_GenericBoiler/regression/ThermalZones/funnel_comp/AixLib.ThermalZones.HighOrder.Examples.ASHREA140.CompareDynamicAndStaticSolarFrac_Case270.mat_Room_dyn.solarRadInRoom.solar_frac_win_abs[1]/errors.csv new file mode 100644 index 0000000000..9d3b74303d --- /dev/null +++ b/docs/correct_HTML_issue1147_GenericBoiler/regression/ThermalZones/funnel_comp/AixLib.ThermalZones.HighOrder.Examples.ASHREA140.CompareDynamicAndStaticSolarFrac_Case270.mat_Room_dyn.solarRadInRoom.solar_frac_win_abs[1]/errors.csv @@ -0,0 +1,3 @@ +x,y +0,0 +86400,0 diff --git a/docs/correct_HTML_issue1147_GenericBoiler/regression/ThermalZones/funnel_comp/AixLib.ThermalZones.HighOrder.Examples.ASHREA140.CompareDynamicAndStaticSolarFrac_Case270.mat_Room_dyn.solarRadInRoom.solar_frac_win_abs[1]/lowerBound.csv b/docs/correct_HTML_issue1147_GenericBoiler/regression/ThermalZones/funnel_comp/AixLib.ThermalZones.HighOrder.Examples.ASHREA140.CompareDynamicAndStaticSolarFrac_Case270.mat_Room_dyn.solarRadInRoom.solar_frac_win_abs[1]/lowerBound.csv new file mode 100644 index 0000000000..c8af47c272 --- /dev/null +++ b/docs/correct_HTML_issue1147_GenericBoiler/regression/ThermalZones/funnel_comp/AixLib.ThermalZones.HighOrder.Examples.ASHREA140.CompareDynamicAndStaticSolarFrac_Case270.mat_Room_dyn.solarRadInRoom.solar_frac_win_abs[1]/lowerBound.csv @@ -0,0 +1,3 @@ +x,y +-0.001,-0.0001952884593047202 +86400.001,-0.0001952884593047202 diff --git a/docs/correct_HTML_issue1147_GenericBoiler/regression/ThermalZones/funnel_comp/AixLib.ThermalZones.HighOrder.Examples.ASHREA140.CompareDynamicAndStaticSolarFrac_Case270.mat_Room_dyn.solarRadInRoom.solar_frac_win_abs[1]/reference.csv b/docs/correct_HTML_issue1147_GenericBoiler/regression/ThermalZones/funnel_comp/AixLib.ThermalZones.HighOrder.Examples.ASHREA140.CompareDynamicAndStaticSolarFrac_Case270.mat_Room_dyn.solarRadInRoom.solar_frac_win_abs[1]/reference.csv new file mode 100644 index 0000000000..54226c0ea2 --- /dev/null +++ b/docs/correct_HTML_issue1147_GenericBoiler/regression/ThermalZones/funnel_comp/AixLib.ThermalZones.HighOrder.Examples.ASHREA140.CompareDynamicAndStaticSolarFrac_Case270.mat_Room_dyn.solarRadInRoom.solar_frac_win_abs[1]/reference.csv @@ -0,0 +1,3 @@ +x,y +0,0.0008047115406952798 +86400,0.0008047115406952798 diff --git 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b/docs/correct_HTML_issue1147_GenericBoiler/regression/ThermalZones/simulator-dymola.log @@ -0,0 +1,4560 @@ + = true + + +rCheck = checkModel("AixLib.ThermalZones.ReducedOrder.Examples.ThermalZoneMoistAirSwimmingPool"); +Check of AixLib.ThermalZones.ReducedOrder.Examples.ThermalZoneMoistAirSwimmingPool +The model has the same number of unknowns and equations: 3645 +The model has the same number of unknowns and equations +for the given numerical settings of parameters: 3645 +Check of AixLib.ThermalZones.ReducedOrder.Examples.ThermalZoneMoistAirSwimmingPool successful. +Declaring variable: Boolean rCheck ; + +Modelica.Utilities.Streams.print(" { \"file\" : \"AixLib/Resources/Scripts/Dymola/ThermalZones/ReducedOrder/Examples/ThermalZoneMoistAirSwimmingPool.mos\",", "AixLib.ThermalZones.ReducedOrder.Examples.ThermalZoneMoistAirSwimmingPool.statistics.log"); +Modelica.Utilities.Streams.print(" \"model\" : \"AixLib.ThermalZones.ReducedOrder.Examples.ThermalZoneMoistAirSwimmingPool\",", "AixLib.ThermalZones.ReducedOrder.Examples.ThermalZoneMoistAirSwimmingPool.statistics.log"); +Modelica.Utilities.Streams.print(" \"check\" : {", "AixLib.ThermalZones.ReducedOrder.Examples.ThermalZoneMoistAirSwimmingPool.statistics.log"); +Modelica.Utilities.Streams.print(" \"command\" : \"checkModel(\\\"AixLib.ThermalZones.ReducedOrder.Examples.ThermalZoneMoistAirSwimmingPool\\\");\",", "AixLib.ThermalZones.ReducedOrder.Examples.ThermalZoneMoistAirSwimmingPool.statistics.log"); +Modelica.Utilities.Streams.print(" \"result\" : " + String(rCheck), "AixLib.ThermalZones.ReducedOrder.Examples.ThermalZoneMoistAirSwimmingPool.statistics.log"); +Modelica.Utilities.Streams.print(" },", "AixLib.ThermalZones.ReducedOrder.Examples.ThermalZoneMoistAirSwimmingPool.statistics.log"); + + +rScript=RunScript("modelica://AixLib/Resources/Scripts/Dymola/ThermalZones/ReducedOrder/Examples/ThermalZoneMoistAirSwimmingPool.mos"); +simulateModel("AixLib.ThermalZones.ReducedOrder.Examples.ThermalZoneMoistAirSwimmingPool", tolerance=1e-6, stopTime=3.1536e+007, numberOfIntervals=0, outputInterval=3600, method="CVode", resultFile="AixLib.ThermalZones.ReducedOrder.Examples.ThermalZoneMoistAirSwimmingPool"); +Translation of AixLib.ThermalZones.ReducedOrder.Examples.ThermalZoneMoistAirSwimmingPool +The DAE has 3645 scalar unknowns and 3645 scalar equations. +Redundant consistent initial conditions. +Removed the following equations which are redundant and consistent: + thermalZone.ROM.p_start = thermalZone.p_start; + thermalZone.airFlowMoistureToROM.sou.vol.p_start = thermalZone.airFlowMoistureToROM.sou.p_start; + if (thermalZone.airFlowMoistureToROM.AirLay.dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.FixedInitial) then + if (thermalZone.airFlowMoistureToROM.AirLay.dynBal.initialize_p) then + thermalZone.airFlowMoistureToROM.AirLay.dynBal.medium.p = thermalZone.airFlowMoistureToROM.AirLay.dynBal.p_start; + end if; + else + if (thermalZone.airFlowMoistureToROM.AirLay.dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then + if (thermalZone.airFlowMoistureToROM.AirLay.dynBal.initialize_p) then + der(thermalZone.airFlowMoistureToROM.AirLay.dynBal.medium.p) = 0; + end if; + end if; + end if; + +This required evaluation of +the interactive parameters + sinAir.p(start = 101325) + thermalZone.airFlowMoistureToROM.AirLay.p_start(start = 101325) + thermalZone.airFlowMoistureToROM.sou.p_start(start = 101325) + thermalZone.p_start(start = 101325) + +The redundancies involve +initial equations: + thermalZone.ROM.volMoiAir.dynBal.medium.p = thermalZone.ROM.volMoiAir.dynBal.p_start; + thermalZone.airFlowMoistureToROM.AirLay.dynBal.medium.p = thermalZone.airFlowMoistureToROM.AirLay.dynBal.p_start; + thermalZone.airFlowMoistureToROM.sou.vol.dynBal.medium.p = thermalZone.airFlowMoistureToROM.sou.vol.dynBal.p_start; + + +Statistics + +Original Model + Number of components: 712 + Variables: 6861 + Constants: 169 (169 scalars) + Parameters: 2779 (5151 scalars) + Unknowns: 3913 (3743 scalars) + Differentiated variables: 34 scalars + Equations: 3071 + Nontrivial: 2635 +Translated Model + Constants: 2021 scalars + Free parameters: 2252 scalars + Parameter depending: 1478 scalars + Continuous time states: 25 scalars + Time-varying variables: 1061 scalars + Alias variables: 2251 scalars + Number of mixed real/discrete systems of equations: 0 + Sizes of linear systems of equations: {26, 13, 13, 26, 13, 13, 4, 4} + Sizes after manipulation of the linear systems: {13, 6, 6, 13, 6, 6, 0, 0} + Sizes of nonlinear systems of equations: {57, 1, 1, 1, 1, 1, 1, 1, 1} + Sizes after manipulation of the nonlinear systems: {6, 0, 1, 0, 1, 0, 1, 1, 1} + Number of numerical Jacobians: 0 + Initialization problem + Sizes of nonlinear systems of equations: {1, 1, 68, 1, 1} + Sizes after manipulation of the nonlinear systems: {0, 0, 8, 1, 1} + Number of numerical Jacobians: 0 + +Selected continuous time states +Statically selected continuous time states +thermalZone.airFlowMoistureToROM.AirLay.dynBal.medium.Xi[1] +thermalZone.airFlowMoistureToROM.AirLay.dynBal.U +thermalZone.airFlowMoistureToROM.sou.filter.s[1] +thermalZone.airFlowMoistureToROM.sou.filter.s[2] +thermalZone.airFlowMoistureToROM.sou.vol.dynBal.medium.Xi[1] +thermalZone.airFlowMoistureToROM.sou.vol.dynBal.U +thermalZone.heaterCooler.pITempHeat.PI.I.y +thermalZone.indoorSwimmingPool[1].cirPump.filter.s[1] +thermalZone.indoorSwimmingPool[1].cirPump.filter.s[2] +thermalZone.indoorSwimmingPool[1].cirPump.vol.dynBal.U +thermalZone.indoorSwimmingPool[1].PI.I.y +thermalZone.indoorSwimmingPool[1].poolSto.dynBal.U +thermalZone.indoorSwimmingPool[1].poolWat.dynBal.U +thermalZone.indoorSwimmingPool[2].cirPump.filter.s[1] +thermalZone.indoorSwimmingPool[2].cirPump.filter.s[2] +thermalZone.indoorSwimmingPool[2].cirPump.vol.dynBal.U +thermalZone.indoorSwimmingPool[2].PI.I.y +thermalZone.indoorSwimmingPool[2].poolSto.dynBal.U +thermalZone.indoorSwimmingPool[2].poolWat.dynBal.U +thermalZone.ROM.extWallRC.thermCapExt[1].T +thermalZone.ROM.floorRC.thermCapExt[1].T +thermalZone.ROM.intWallRC.thermCapInt[1].T +thermalZone.ROM.roofRC.thermCapExt[1].T +thermalZone.ROM.volMoiAir.dynBal.medium.Xi[1] +thermalZone.ROM.volMoiAir.dynBal.U +Finished +Finished + = true + + + + + +Declaring variable: Boolean rScript ; + +savelog("AixLib.ThermalZones.ReducedOrder.Examples.ThermalZoneMoistAirSwimmingPool.translation.log"); = true + + +rCheck = checkModel("AixLib.ThermalZones.ReducedOrder.Examples.ThermalZoneMoistAir"); +Check of AixLib.ThermalZones.ReducedOrder.Examples.ThermalZoneMoistAir +The model has the same number of unknowns and equations: 2037 +The model could not be deduced to be symbolically well-posed. +The model has + 1877+29*thermalZone.zoneParam.nOrientations+2*thermalZone.ROM.volMoiAir.dynBal.nPorts +thermalZone.humanTotHeaDependent.productHeatOutput.nu+thermalZone.humanTotHeaDependent.productMoistureOutput.nu +thermalZone.machinesSenHea.productHeatOutput.nu+thermalZone.lights.productHeatOutput.nu +thermalZone.SumQLat1_flow.nu+max([size(internalGains.columns, 1); size( internalGains.offset, 1)]) +scalar unknowns and + 1908+(if weaDat.pAtmSou == AixLib.BoundaryConditions.Types.DataSource.Parameter then 1 else 0)+(if weaDat.TDewPoiSou == AixLib.BoundaryConditions.Types.DataSource. Parameter then 1 else 0)+(if weaDat.TDryBulSou == AixLib.BoundaryConditions.Types.DataSource. Parameter then 1 else 0)+(if weaDat.TBlaSkySou == AixLib.BoundaryConditions.Types.DataSource. Parameter then 1 else 0)+(if weaDat.relHumSou == AixLib.BoundaryConditions.Types.DataSource. Parameter then 1 else 0)+(if weaDat.opaSkyCovSou == AixLib.BoundaryConditions.Types.DataSource. Parameter then 1 else 0)+(if weaDat.ceiHeiSou == AixLib.BoundaryConditions.Types.DataSource. Parameter then 1 else 0)+(if weaDat.totSkyCovSou == AixLib.BoundaryConditions.Types.DataSource. Parameter then 1 else 0)+(if weaDat.winSpeSou == AixLib.BoundaryConditions.Types.DataSource. Parameter then 1 else 0)+(if weaDat.winDirSou == AixLib.BoundaryConditions.Types.DataSource. Parameter then 1 else 0)+(if weaDat.HInfHorSou == AixLib.BoundaryConditions.Types.DataSource. Parameter then 1 else 0)+(if weaDat.HSou == AixLib.BoundaryConditions.Types.RadiationDataSource. Input_HDirNor_HDifHor then 2 else 1)+(if weaDat.HSou == AixLib.BoundaryConditions.Types.RadiationDataSource. Input_HDirNor_HGloHor then 2 else 1)+(if weaDat.HSou == AixLib.BoundaryConditions.Types.RadiationDataSource. Input_HGloHor_HDifHor then 2 else 1)+max([size(internalGains.columns, 1); size (internalGains.offset, 1)])+(if sourcAir.use_Xi_in then 2 else (if sourcAir.use_X_in then 1 else 3))+3*sourcAir.nPorts+(if not sourcAir.use_m_flow_in then 1 else 0)+(if not sourcAir.use_T_in then 1 else 0)+(if sinAir.use_Xi_in then 2 else (if sinAir.use_X_in then 1 else 3))+3*sinAir.nPorts+(if not sinAir.use_p_in then 1 else 0)+(if not sinAir.use_T_in then 1 else 0)+19* thermalZone.zoneParam.nOrientations+(if not thermalZone.eqAirTempWall.TGroundFromInput then 1 else 0)+5*thermalZone.ROM.volMoiAir.dynBal.nPorts +scalar equations. +However, exploiting the given numerical settings of parameters gives the same number of unknowns and equations: + 2037 +Check of AixLib.ThermalZones.ReducedOrder.Examples.ThermalZoneMoistAir successful. +Declaring variable: Boolean rCheck ; + +Modelica.Utilities.Streams.print(" { \"file\" : \"AixLib/Resources/Scripts/Dymola/ThermalZones/ReducedOrder/Examples/ThermalZoneMoistAir.mos\",", "AixLib.ThermalZones.ReducedOrder.Examples.ThermalZoneMoistAir.statistics.log"); +Modelica.Utilities.Streams.print(" \"model\" : \"AixLib.ThermalZones.ReducedOrder.Examples.ThermalZoneMoistAir\",", "AixLib.ThermalZones.ReducedOrder.Examples.ThermalZoneMoistAir.statistics.log"); +Modelica.Utilities.Streams.print(" \"check\" : {", "AixLib.ThermalZones.ReducedOrder.Examples.ThermalZoneMoistAir.statistics.log"); +Modelica.Utilities.Streams.print(" \"command\" : \"checkModel(\\\"AixLib.ThermalZones.ReducedOrder.Examples.ThermalZoneMoistAir\\\");\",", "AixLib.ThermalZones.ReducedOrder.Examples.ThermalZoneMoistAir.statistics.log"); +Modelica.Utilities.Streams.print(" \"result\" : " + String(rCheck), "AixLib.ThermalZones.ReducedOrder.Examples.ThermalZoneMoistAir.statistics.log"); +Modelica.Utilities.Streams.print(" },", "AixLib.ThermalZones.ReducedOrder.Examples.ThermalZoneMoistAir.statistics.log"); + + +rScript=RunScript("modelica://AixLib/Resources/Scripts/Dymola/ThermalZones/ReducedOrder/Examples/ThermalZoneMoistAir.mos"); +simulateModel("AixLib.ThermalZones.ReducedOrder.Examples.ThermalZoneMoistAir", tolerance=1e-6, stopTime=3.1536e+007, numberOfIntervals=0, outputInterval=3600, method="CVode", resultFile="AixLib.ThermalZones.ReducedOrder.Examples.ThermalZoneMoistAir"); +Translation of AixLib.ThermalZones.ReducedOrder.Examples.ThermalZoneMoistAir +The DAE has 2037 scalar unknowns and 2037 scalar equations. +Redundant consistent initial conditions. +Removed the following equations which are redundant and consistent: + if (thermalZone.ROM.volMoiAir.dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (thermalZone.ROM.volMoiAir.dynBal.initialize_p) then + thermalZone.ROM.volMoiAir.dynBal.medium.p = thermalZone.ROM.volMoiAir.dynBal.p_start; + end if; + else + if (thermalZone.ROM.volMoiAir.dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. SteadyStateInitial) then + if (thermalZone.ROM.volMoiAir.dynBal.initialize_p) then + der(thermalZone.ROM.volMoiAir.dynBal.medium.p) = 0; + end if; + end if; + end if; + +This required evaluation of +the interactive parameters + sinAir.p(start = 101325) + thermalZone.p_start(start = 101325) + +The redundancies involve +initial equations: + thermalZone.ROM.volMoiAir.dynBal.medium.p = thermalZone.ROM.volMoiAir.dynBal.p_start; + + +Statistics + +Original Model + Number of components: 310 + Variables: 2805 + Constants: 86 (86 scalars) + Parameters: 792 (2610 scalars) + Unknowns: 1927 (2049 scalars) + Differentiated variables: 5 scalars + Equations: 1377 + Nontrivial: 1271 +Translated Model + Constants: 607 scalars + Free parameters: 1951 scalars + Parameter depending: 328 scalars + Continuous time states: 4 scalars + Time-varying variables: 617 scalars + Alias variables: 1242 scalars + Number of mixed real/discrete systems of equations: 0 + Sizes of linear systems of equations: {4, 29} + Sizes after manipulation of the linear systems: {0, 4} + Sizes of nonlinear systems of equations: {1, 1, 1, 1, 1, 1} + Sizes after manipulation of the nonlinear systems: {0, 1, 0, 1, 0, 1} + Number of numerical Jacobians: 0 + Initialization problem + Sizes of linear systems of equations: {32} + Sizes after manipulation of the linear systems: {5} + +Selected continuous time states +Statically selected continuous time states +thermalZone.ROM.extWallRC.thermCapExt[1].T +thermalZone.ROM.intWallRC.thermCapInt[1].T +thermalZone.ROM.volMoiAir.dynBal.medium.Xi[1] +thermalZone.ROM.volMoiAir.dynBal.U +Finished +Finished + = true + + + +Declaring variable: Boolean rScript ; + +savelog("AixLib.ThermalZones.ReducedOrder.Examples.ThermalZoneMoistAir.translation.log"); = true + + +rCheck = checkModel("AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case600"); +Check of AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case600 +The model has the same number of unknowns and equations: 1585 +The model has the same number of unknowns and equations +for the given numerical settings of parameters: 1585 +Check of AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case600 successful. +Declaring variable: Boolean rCheck ; + +Modelica.Utilities.Streams.print(" { \"file\" : \"AixLib/Resources/Scripts/Dymola/ThermalZones/HighOrder/Validation/ASHRAE140/Case600.mos\",", "AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case600.statistics.log"); +Modelica.Utilities.Streams.print(" \"model\" : \"AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case600\",", "AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case600.statistics.log"); +Modelica.Utilities.Streams.print(" \"check\" : {", "AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case600.statistics.log"); +Modelica.Utilities.Streams.print(" \"command\" : \"checkModel(\\\"AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case600\\\");\",", "AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case600.statistics.log"); +Modelica.Utilities.Streams.print(" \"result\" : " + String(rCheck), "AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case600.statistics.log"); +Modelica.Utilities.Streams.print(" },", "AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case600.statistics.log"); + + +rScript=RunScript("modelica://AixLib/Resources/Scripts/Dymola/ThermalZones/HighOrder/Validation/ASHRAE140/Case600.mos"); +simulateModel("AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case600", startTime=0, stopTime=31539600, outputInterval=1800, tolerance=1e-6, method="dassl", resultFile="AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case600"); +Translation of AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case600 +The DAE has 1585 scalar unknowns and 1585 scalar equations. + +Statistics + +Original Model + Number of components: 352 + Variables: 3082 + Constants: 41 (276 scalars) + Parameters: 1493 (2159 scalars) + Unknowns: 1548 (1585 scalars) + Differentiated variables: 25 scalars + Equations: 1257 + Nontrivial: 1045 +Translated Model + Constants: 780 scalars + Free parameters: 876 scalars + Parameter depending: 909 scalars + Outputs: 5 scalars + Continuous time states: 25 scalars + Time-varying variables: 474 scalars + Alias variables: 981 scalars + Number of mixed real/discrete systems of equations: 0 + Sizes of linear systems of equations: {4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 3, 4, 4, 4, 4} + Sizes after manipulation of the linear systems: {0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0} + Sizes of nonlinear systems of equations: {55} + Sizes after manipulation of the nonlinear systems: {13} + Number of numerical Jacobians: 0 + +Selected continuous time states +Statically selected continuous time states +idealHeaterCooler.pITempCool.PI.I.y +idealHeaterCooler.pITempHeat.PI.I.y +integrator2.y +integratorCool.y +integratorHeat.y +Room.airload.dynBal.m +Room.airload.dynBal.medium.Xi[1] +Room.airload.dynBal.U +Room.ceiling.Wall.simpleNLayer.cap[1].T +Room.ceiling.Wall.simpleNLayer.cap[2].T +Room.ceiling.Wall.simpleNLayer.cap[3].T +Room.floor.Wall.simpleNLayer.cap[1].T +Room.floor.Wall.simpleNLayer.cap[2].T +Room.wallEast.Wall.simpleNLayer.cap[1].T +Room.wallEast.Wall.simpleNLayer.cap[2].T +Room.wallEast.Wall.simpleNLayer.cap[3].T +Room.wallNorth.Wall.simpleNLayer.cap[1].T +Room.wallNorth.Wall.simpleNLayer.cap[2].T +Room.wallNorth.Wall.simpleNLayer.cap[3].T +Room.wallSouth.Wall.simpleNLayer.cap[1].T +Room.wallSouth.Wall.simpleNLayer.cap[2].T +Room.wallSouth.Wall.simpleNLayer.cap[3].T +Room.wallWest.Wall.simpleNLayer.cap[1].T +Room.wallWest.Wall.simpleNLayer.cap[2].T +Room.wallWest.Wall.simpleNLayer.cap[3].T +Finished +Finished + = true + +Declaring variable: Boolean rScript ; + +savelog("AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case600.translation.log"); = true + + +rCheck = checkModel("AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case430"); +Check of AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case430 +The model has the same number of unknowns and equations: 1568 +The model has the same number of unknowns and equations +for the given numerical settings of parameters: 1568 +Check of AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case430 successful. +Declaring variable: Boolean rCheck ; + +Modelica.Utilities.Streams.print(" { \"file\" : \"AixLib/Resources/Scripts/Dymola/ThermalZones/HighOrder/Validation/ASHRAE140/Case430.mos\",", "AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case430.statistics.log"); +Modelica.Utilities.Streams.print(" \"model\" : \"AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case430\",", "AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case430.statistics.log"); +Modelica.Utilities.Streams.print(" \"check\" : {", "AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case430.statistics.log"); +Modelica.Utilities.Streams.print(" \"command\" : \"checkModel(\\\"AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case430\\\");\",", "AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case430.statistics.log"); +Modelica.Utilities.Streams.print(" \"result\" : " + String(rCheck), "AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case430.statistics.log"); +Modelica.Utilities.Streams.print(" },", "AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case430.statistics.log"); + + +rScript=RunScript("modelica://AixLib/Resources/Scripts/Dymola/ThermalZones/HighOrder/Validation/ASHRAE140/Case430.mos"); +simulateModel("AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case430", startTime=0, stopTime=31539600, outputInterval=1800, tolerance=1e-6, method="dassl", resultFile="AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case430"); +Translation of AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case430 +The DAE has 1568 scalar unknowns and 1568 scalar equations. + +Statistics + +Original Model + Number of components: 349 + Variables: 3047 + Constants: 41 (276 scalars) + Parameters: 1474 (2065 scalars) + Unknowns: 1532 (1568 scalars) + Differentiated variables: 25 scalars + Equations: 1252 + Nontrivial: 1041 +Translated Model + Constants: 771 scalars + Free parameters: 794 scalars + Parameter depending: 906 scalars + Outputs: 5 scalars + Continuous time states: 25 scalars + Time-varying variables: 461 scalars + Alias variables: 977 scalars + Number of mixed real/discrete systems of equations: 0 + Sizes of linear systems of equations: {4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 3, 4, 4, 4, 4} + Sizes after manipulation of the linear systems: {0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0} + Sizes of nonlinear systems of equations: {55} + Sizes after manipulation of the nonlinear systems: {13} + Number of numerical Jacobians: 0 + +Selected continuous time states +Statically selected continuous time states +idealHeaterCooler.pITempCool.PI.I.y +idealHeaterCooler.pITempHeat.PI.I.y +integrator2.y +integratorCool.y +integratorHeat.y +Room.airload.dynBal.m +Room.airload.dynBal.medium.Xi[1] +Room.airload.dynBal.U +Room.ceiling.Wall.simpleNLayer.cap[1].T +Room.ceiling.Wall.simpleNLayer.cap[2].T +Room.ceiling.Wall.simpleNLayer.cap[3].T +Room.floor.Wall.simpleNLayer.cap[1].T +Room.floor.Wall.simpleNLayer.cap[2].T +Room.wallEast.Wall.simpleNLayer.cap[1].T +Room.wallEast.Wall.simpleNLayer.cap[2].T +Room.wallEast.Wall.simpleNLayer.cap[3].T +Room.wallNorth.Wall.simpleNLayer.cap[1].T +Room.wallNorth.Wall.simpleNLayer.cap[2].T +Room.wallNorth.Wall.simpleNLayer.cap[3].T +Room.wallSouth.Wall.simpleNLayer.cap[1].T +Room.wallSouth.Wall.simpleNLayer.cap[2].T +Room.wallSouth.Wall.simpleNLayer.cap[3].T +Room.wallWest.Wall.simpleNLayer.cap[1].T +Room.wallWest.Wall.simpleNLayer.cap[2].T +Room.wallWest.Wall.simpleNLayer.cap[3].T +Finished +Finished + = true + +Declaring variable: Boolean rScript ; + +savelog("AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case430.translation.log"); = true + + +rCheck = checkModel("AixLib.ThermalZones.HighOrder.Examples.OFDHeatLoad"); +Check of AixLib.ThermalZones.HighOrder.Examples.OFDHeatLoad +Warning: Base class Medium is not transitively non-replaceable, + since it is a short class equal to a replaceable class. + File: /tmp/tmp-AixLib-0-jodv2jcy/AixLib/ThermalZones/HighOrder/House/OFD_MiddleInnerLoadWall/BuildingEnvelope/WholeHouseBuildingEnvelope.mo, line 193 + Component context: AixLib.ThermalZones.HighOrder.House.OFD_MiddleInnerLoadWall.BuildingEnvelope.WholeHouseBuildingEnvelope.Medium + Component declared as Attic_Ro2Lf5 attic_2Ro_5Rooms in AixLib.ThermalZones.HighOrder.House.OFD_MiddleInnerLoadWall.BuildingEnvelope.WholeHouseBuildingEnvelope +Warning: Base class Medium is not transitively non-replaceable, + since it is a short class equal to a replaceable class. + File: /tmp/tmp-AixLib-0-jodv2jcy/AixLib/ThermalZones/HighOrder/House/OFD_MiddleInnerLoadWall/BuildingEnvelope/WholeHouseBuildingEnvelope.mo, line 193 + Component context: AixLib.ThermalZones.HighOrder.House.OFD_MiddleInnerLoadWall.BuildingEnvelope.WholeHouseBuildingEnvelope.Medium + Component declared as MixingVolumeMoistAir airload in AixLib.ThermalZones.HighOrder.Rooms.BaseClasses.PartialRoom +Warning: Base class Medium is not transitively non-replaceable, + since it is a short class equal to a replaceable class. + File: /tmp/tmp-AixLib-0-jodv2jcy/AixLib/ThermalZones/HighOrder/House/OFD_MiddleInnerLoadWall/BuildingEnvelope/WholeHouseBuildingEnvelope.mo, line 193 + Component context: AixLib.ThermalZones.HighOrder.House.OFD_MiddleInnerLoadWall.BuildingEnvelope.WholeHouseBuildingEnvelope.Medium + Component declared as VesselFluidPorts_b ports in AixLib.Fluid.MixingVolumes.BaseClasses.PartialMixingVolume +Warning: Base class Medium is not transitively non-replaceable, + since it is a short class equal to a replaceable class. + File: /tmp/tmp-AixLib-0-jodv2jcy/AixLib/ThermalZones/HighOrder/House/OFD_MiddleInnerLoadWall/BuildingEnvelope/WholeHouseBuildingEnvelope.mo, line 193 + Component context: AixLib.ThermalZones.HighOrder.House.OFD_MiddleInnerLoadWall.BuildingEnvelope.WholeHouseBuildingEnvelope.Medium + Component declared as VesselFluidPorts_b ports in AixLib.Fluid.MixingVolumes.BaseClasses.PartialMixingVolume +Warning: Base class Medium is not transitively non-replaceable, + since it is a short class equal to a replaceable class. + File: /tmp/tmp-AixLib-0-jodv2jcy/AixLib/ThermalZones/HighOrder/House/OFD_MiddleInnerLoadWall/BuildingEnvelope/WholeHouseBuildingEnvelope.mo, line 193 + Component context: AixLib.ThermalZones.HighOrder.House.OFD_MiddleInnerLoadWall.BuildingEnvelope.WholeHouseBuildingEnvelope.Medium + Component declared as FluidPort_a port_a in AixLib.Fluid.Interfaces.PartialTwoPort +Warning: Base class Medium is not transitively non-replaceable, + since it is a short class equal to a replaceable class. + File: /tmp/tmp-AixLib-0-jodv2jcy/AixLib/ThermalZones/HighOrder/House/OFD_MiddleInnerLoadWall/BuildingEnvelope/WholeHouseBuildingEnvelope.mo, line 193 + Component context: AixLib.ThermalZones.HighOrder.House.OFD_MiddleInnerLoadWall.BuildingEnvelope.WholeHouseBuildingEnvelope.Medium + Component declared as FluidPort_a port_a in AixLib.Fluid.Interfaces.PartialTwoPort +Warning: Base class Medium is not transitively non-replaceable, + since it is a short class equal to a replaceable class. + File: /tmp/tmp-AixLib-0-jodv2jcy/AixLib/ThermalZones/HighOrder/House/OFD_MiddleInnerLoadWall/BuildingEnvelope/WholeHouseBuildingEnvelope.mo, line 193 + Component context: AixLib.ThermalZones.HighOrder.House.OFD_MiddleInnerLoadWall.BuildingEnvelope.WholeHouseBuildingEnvelope.Medium + Component declared as FluidPort_b port_b in AixLib.Fluid.Interfaces.PartialTwoPort +Warning: Base class Medium is not transitively non-replaceable, + since it is a short class equal to a replaceable class. + File: /tmp/tmp-AixLib-0-jodv2jcy/AixLib/ThermalZones/HighOrder/House/OFD_MiddleInnerLoadWall/BuildingEnvelope/WholeHouseBuildingEnvelope.mo, line 193 + Component context: AixLib.ThermalZones.HighOrder.House.OFD_MiddleInnerLoadWall.BuildingEnvelope.WholeHouseBuildingEnvelope.Medium + Component declared as FluidPort_b port_b in AixLib.Fluid.Interfaces.PartialTwoPort +Warning: Base class Medium is not transitively non-replaceable, + since it is a short class equal to a replaceable class. + File: /tmp/tmp-AixLib-0-jodv2jcy/AixLib/ThermalZones/HighOrder/House/OFD_MiddleInnerLoadWall/BuildingEnvelope/WholeHouseBuildingEnvelope.mo, line 193 + Component context: AixLib.ThermalZones.HighOrder.House.OFD_MiddleInnerLoadWall.BuildingEnvelope.WholeHouseBuildingEnvelope.Medium + Component declared as StaticTwoPortConservationEquation steBal in AixLib.Fluid.MixingVolumes.BaseClasses.PartialMixingVolume +Warning: Base class Medium is not transitively non-replaceable, + since it is a short class equal to a replaceable class. + File: /tmp/tmp-AixLib-0-jodv2jcy/AixLib/ThermalZones/HighOrder/House/OFD_MiddleInnerLoadWall/BuildingEnvelope/WholeHouseBuildingEnvelope.mo, line 193 + Component context: AixLib.ThermalZones.HighOrder.House.OFD_MiddleInnerLoadWall.BuildingEnvelope.WholeHouseBuildingEnvelope.Medium + Component declared as StaticTwoPortConservationEquation steBal in AixLib.Fluid.MixingVolumes.BaseClasses.PartialMixingVolume +Warning: Base class Medium is not transitively non-replaceable, + since it is a short class equal to a replaceable class. + File: /tmp/tmp-AixLib-0-jodv2jcy/AixLib/ThermalZones/HighOrder/House/OFD_MiddleInnerLoadWall/BuildingEnvelope/WholeHouseBuildingEnvelope.mo, line 193 + Component context: AixLib.ThermalZones.HighOrder.House.OFD_MiddleInnerLoadWall.BuildingEnvelope.WholeHouseBuildingEnvelope.Medium + Component declared as ConservationEquation dynBal in AixLib.Fluid.MixingVolumes.BaseClasses.PartialMixingVolume +Warning: Base class Medium is not transitively non-replaceable, + since it is a short class equal to a replaceable class. + File: /tmp/tmp-AixLib-0-jodv2jcy/AixLib/ThermalZones/HighOrder/House/OFD_MiddleInnerLoadWall/BuildingEnvelope/WholeHouseBuildingEnvelope.mo, line 193 + Component context: AixLib.ThermalZones.HighOrder.House.OFD_MiddleInnerLoadWall.BuildingEnvelope.WholeHouseBuildingEnvelope.Medium + Component declared as VesselFluidPorts_b ports in AixLib.Fluid.Interfaces.ConservationEquation +Warning: Base class Medium is not transitively non-replaceable, + since it is a short class equal to a replaceable class. + File: /tmp/tmp-AixLib-0-jodv2jcy/AixLib/ThermalZones/HighOrder/House/OFD_MiddleInnerLoadWall/BuildingEnvelope/WholeHouseBuildingEnvelope.mo, line 193 + Component context: AixLib.ThermalZones.HighOrder.House.OFD_MiddleInnerLoadWall.BuildingEnvelope.WholeHouseBuildingEnvelope.Medium + Component declared as VesselFluidPorts_b ports in AixLib.Fluid.Interfaces.ConservationEquation +Warning: Base class Medium is not transitively non-replaceable, + since it is a short class equal to a replaceable class. + File: /tmp/tmp-AixLib-0-jodv2jcy/AixLib/ThermalZones/HighOrder/House/OFD_MiddleInnerLoadWall/BuildingEnvelope/WholeHouseBuildingEnvelope.mo, line 193 + Component context: AixLib.ThermalZones.HighOrder.House.OFD_MiddleInnerLoadWall.BuildingEnvelope.WholeHouseBuildingEnvelope.Medium + Component declared as ConservationEquation dynBal in AixLib.Fluid.MixingVolumes.BaseClasses.PartialMixingVolume +Warning: Base class Medium is not transitively non-replaceable, + since it is a short class equal to a replaceable class. + File: /tmp/tmp-AixLib-0-jodv2jcy/AixLib/ThermalZones/HighOrder/House/OFD_MiddleInnerLoadWall/BuildingEnvelope/WholeHouseBuildingEnvelope.mo, line 193 + Component context: AixLib.ThermalZones.HighOrder.House.OFD_MiddleInnerLoadWall.BuildingEnvelope.WholeHouseBuildingEnvelope.Medium + Component declared as MixingVolumeMoistAir airload in AixLib.ThermalZones.HighOrder.Rooms.BaseClasses.PartialRoom +Warning: Base class Medium is not transitively non-replaceable, + since it is a short class equal to a replaceable class. + File: /tmp/tmp-AixLib-0-jodv2jcy/AixLib/ThermalZones/HighOrder/House/OFD_MiddleInnerLoadWall/BuildingEnvelope/WholeHouseBuildingEnvelope.mo, line 193 + Component context: AixLib.ThermalZones.HighOrder.House.OFD_MiddleInnerLoadWall.BuildingEnvelope.WholeHouseBuildingEnvelope.Medium + Component declared as VesselFluidPorts_b ports in AixLib.ThermalZones.HighOrder.Rooms.BaseClasses.PartialRoom +Warning: Base class Medium is not transitively non-replaceable, + since it is a short class equal to a replaceable class. + File: /tmp/tmp-AixLib-0-jodv2jcy/AixLib/ThermalZones/HighOrder/House/OFD_MiddleInnerLoadWall/BuildingEnvelope/WholeHouseBuildingEnvelope.mo, line 193 + Component context: AixLib.ThermalZones.HighOrder.House.OFD_MiddleInnerLoadWall.BuildingEnvelope.WholeHouseBuildingEnvelope.Medium + Component declared as VesselFluidPorts_b ports in AixLib.ThermalZones.HighOrder.Rooms.BaseClasses.PartialRoom +Warning: Base class Medium is not transitively non-replaceable, + since it is a short class equal to a replaceable class. + File: /tmp/tmp-AixLib-0-jodv2jcy/AixLib/ThermalZones/HighOrder/House/OFD_MiddleInnerLoadWall/BuildingEnvelope/WholeHouseBuildingEnvelope.mo, line 193 + Context: AixLib.ThermalZones.HighOrder.House.OFD_MiddleInnerLoadWall.BuildingEnvelope.WholeHouseBuildingEnvelope.Medium +Warning: Inconsistency for connectors dimensioned using parameter with annotation(Dialog(connectorSizing=true)). + Some connector elements are not connected. +This is either because the connections and/or parameters has been edited textually to an inconsistent state + or because the default for the parameter is not 0. The unconnected connectors are: + wholeHouseBuildingEnvelope.attic_2Ro_5Rooms.ports[1] + wholeHouseBuildingEnvelope.attic_2Ro_5Rooms.ports[2] + +The model has the same number of unknowns and equations: 10085 +The model could not be deduced to be symbolically well-posed. +The model has + 10001+5*varRad.n+nHeatedRooms+2*wholeHouseBuildingEnvelope.groundFloor_Building.Livingroom.airload.dynBal.nPorts +2*wholeHouseBuildingEnvelope.groundFloor_Building.Hobby.airload.dynBal.nPorts +2*wholeHouseBuildingEnvelope.groundFloor_Building.WC_Storage.airload.dynBal.nPorts +2*wholeHouseBuildingEnvelope.groundFloor_Building.Kitchen.airload.dynBal.nPorts +2*wholeHouseBuildingEnvelope.groundFloor_Building.Corridor.airload.dynBal.nPorts +2*wholeHouseBuildingEnvelope.upperFloor_Building.Bedroom.airload.dynBal.nPorts +2*wholeHouseBuildingEnvelope.upperFloor_Building.Children1.airload.dynBal.nPorts +2*wholeHouseBuildingEnvelope.upperFloor_Building.Bath.airload.dynBal.nPorts+2 *wholeHouseBuildingEnvelope.upperFloor_Building.Children2.airload.dynBal.nPorts +2*wholeHouseBuildingEnvelope.upperFloor_Building.Corridor.airload.dynBal.nPorts +2*wholeHouseBuildingEnvelope.attic_2Ro_5Rooms.airload.dynBal.nPorts +scalar unknowns and + 9864+(if not wholeHouseBuildingEnvelope.groundFloor_Building.Livingroom.outside_wall1.Wall.twoStar_RadEx.use_A_in then 1 else 0)+(if wholeHouseBuildingEnvelope.groundFloor_Building.Livingroom.outside_wall1.heatTransfer_Outside.calcMethod == AixLib.ThermalZones.HighOrder.Components.Types.CalcMethodConvectiveHeatTransfer. DIN_6946 then 1 else (if wholeHouseBuildingEnvelope.groundFloor_Building.Livingroom.outside_wall1.heatTransfer_Outside.calcMethod == AixLib.ThermalZones.HighOrder.Components.Types.CalcMethodConvectiveHeatTransfer. ASHRAE_Fundamentals then 1 else 2))+(if not wholeHouseBuildingEnvelope.groundFloor_Building.Livingroom.outside_wall2.Wall.twoStar_RadEx.use_A_in then 1 else 0)+(if wholeHouseBuildingEnvelope.groundFloor_Building.Livingroom.outside_wall2.heatTransfer_Outside.calcMethod == AixLib.ThermalZones.HighOrder.Components.Types.CalcMethodConvectiveHeatTransfer. DIN_6946 then 1 else (if wholeHouseBuildingEnvelope.groundFloor_Building.Livingroom.outside_wall2.heatTransfer_Outside.calcMethod == AixLib.ThermalZones.HighOrder.Components.Types.CalcMethodConvectiveHeatTransfer. ASHRAE_Fundamentals then 1 else 2))+(if not wholeHouseBuildingEnvelope.groundFloor_Building.Livingroom.inside_wall1a.Wall.twoStar_RadEx.use_A_in then 1 else 0)+(if not wholeHouseBuildingEnvelope.groundFloor_Building.Livingroom.inside_wall2.Wall.twoStar_RadEx.use_A_in then 1 else 0)+(if not wholeHouseBuildingEnvelope.groundFloor_Building.Livingroom.Ceiling.Wall.twoStar_RadEx.use_A_in then 1 else 0)+(if not wholeHouseBuildingEnvelope.groundFloor_Building.Livingroom.floor.Wall.twoStar_RadEx.use_A_in then 1 else 0)+(if not wholeHouseBuildingEnvelope.groundFloor_Building.Livingroom.inside_wall1b.Wall.twoStar_RadEx.use_A_in then 1 else 0)+(if not wholeHouseBuildingEnvelope.groundFloor_Building.Hobby.outside_wall1.Wall.twoStar_RadEx.use_A_in then 1 else 0)+(if wholeHouseBuildingEnvelope.groundFloor_Building.Hobby.outside_wall1.heatTransfer_Outside.calcMethod == AixLib.ThermalZones.HighOrder.Components.Types.CalcMethodConvectiveHeatTransfer. DIN_6946 then 1 else (if wholeHouseBuildingEnvelope.groundFloor_Building.Hobby.outside_wall1.heatTransfer_Outside.calcMethod == AixLib.ThermalZones.HighOrder.Components.Types.CalcMethodConvectiveHeatTransfer. ASHRAE_Fundamentals then 1 else 2))+(if not wholeHouseBuildingEnvelope.groundFloor_Building.Hobby.outside_wall2.Wall.twoStar_RadEx.use_A_in then 1 else 0)+(if wholeHouseBuildingEnvelope.groundFloor_Building.Hobby.outside_wall2.heatTransfer_Outside.calcMethod == AixLib.ThermalZones.HighOrder.Components.Types.CalcMethodConvectiveHeatTransfer. DIN_6946 then 1 else (if wholeHouseBuildingEnvelope.groundFloor_Building.Hobby.outside_wall2.heatTransfer_Outside.calcMethod == AixLib.ThermalZones.HighOrder.Components.Types.CalcMethodConvectiveHeatTransfer. ASHRAE_Fundamentals then 1 else 2))+(if not wholeHouseBuildingEnvelope.groundFloor_Building.Hobby.inside_wall1.Wall.twoStar_RadEx.use_A_in then 1 else 0)+(if not wholeHouseBuildingEnvelope.groundFloor_Building.Hobby.inside_wall2.Wall.twoStar_RadEx.use_A_in then 1 else 0)+(if not wholeHouseBuildingEnvelope.groundFloor_Building.Hobby.Ceiling.Wall.twoStar_RadEx.use_A_in then 1 else 0)+(if not wholeHouseBuildingEnvelope.groundFloor_Building.Hobby.floor.Wall.twoStar_RadEx.use_A_in then 1 else 0)+(if not wholeHouseBuildingEnvelope.groundFloor_Building.WC_Storage.outside_wall1.Wall.twoStar_RadEx.use_A_in then 1 else 0)+(if wholeHouseBuildingEnvelope.groundFloor_Building.WC_Storage.outside_wall1.heatTransfer_Outside.calcMethod == AixLib.ThermalZones.HighOrder.Components.Types.CalcMethodConvectiveHeatTransfer. DIN_6946 then 1 else (if wholeHouseBuildingEnvelope.groundFloor_Building.WC_Storage.outside_wall1.heatTransfer_Outside.calcMethod == AixLib.ThermalZones.HighOrder.Components.Types.CalcMethodConvectiveHeatTransfer. ASHRAE_Fundamentals then 1 else 2))+(if not wholeHouseBuildingEnvelope.groundFloor_Building.WC_Storage.outside_wall2.Wall.twoStar_RadEx.use_A_in then 1 else 0)+(if not wholeHouseBuildingEnvelope.groundFloor_Building.WC_Storage.outside_wall2.Door.twoStar_RadEx.use_A_in then 1 else 0)+(if not wholeHouseBuildingEnvelope.groundFloor_Building.WC_Storage.outside_wall2.Door.twoStar_RadEx1.use_A_in then 1 else 0)+(if wholeHouseBuildingEnvelope.groundFloor_Building.WC_Storage.outside_wall2.heatTransfer_Outside.calcMethod == AixLib.ThermalZones.HighOrder.Components.Types.CalcMethodConvectiveHeatTransfer. DIN_6946 then 1 else (if wholeHouseBuildingEnvelope.groundFloor_Building.WC_Storage.outside_wall2.heatTransfer_Outside.calcMethod == AixLib.ThermalZones.HighOrder.Components.Types.CalcMethodConvectiveHeatTransfer. ASHRAE_Fundamentals then 1 else 2))+(if not wholeHouseBuildingEnvelope.groundFloor_Building.WC_Storage.inside_wall1.Wall.twoStar_RadEx.use_A_in then 1 else 0)+(if not wholeHouseBuildingEnvelope.groundFloor_Building.WC_Storage.inside_wall2.Wall.twoStar_RadEx.use_A_in then 1 else 0)+(if not wholeHouseBuildingEnvelope.groundFloor_Building.WC_Storage.Ceiling.Wall.twoStar_RadEx.use_A_in then 1 else 0)+(if not wholeHouseBuildingEnvelope.groundFloor_Building.WC_Storage.floor.Wall.twoStar_RadEx.use_A_in then 1 else 0)+(if not wholeHouseBuildingEnvelope.groundFloor_Building.Kitchen.outside_wall1.Wall.twoStar_RadEx.use_A_in then 1 else 0)+(if wholeHouseBuildingEnvelope.groundFloor_Building.Kitchen.outside_wall1.heatTransfer_Outside.calcMethod == AixLib.ThermalZones.HighOrder.Components.Types.CalcMethodConvectiveHeatTransfer. DIN_6946 then 1 else (if wholeHouseBuildingEnvelope.groundFloor_Building.Kitchen.outside_wall1.heatTransfer_Outside.calcMethod == AixLib.ThermalZones.HighOrder.Components.Types.CalcMethodConvectiveHeatTransfer. ASHRAE_Fundamentals then 1 else 2))+(if not wholeHouseBuildingEnvelope.groundFloor_Building.Kitchen.outside_wall2.Wall.twoStar_RadEx.use_A_in then 1 else 0)+(if wholeHouseBuildingEnvelope.groundFloor_Building.Kitchen.outside_wall2.heatTransfer_Outside.calcMethod == AixLib.ThermalZones.HighOrder.Components.Types.CalcMethodConvectiveHeatTransfer. DIN_6946 then 1 else (if wholeHouseBuildingEnvelope.groundFloor_Building.Kitchen.outside_wall2.heatTransfer_Outside.calcMethod == AixLib.ThermalZones.HighOrder.Components.Types.CalcMethodConvectiveHeatTransfer. ASHRAE_Fundamentals then 1 else 2))+(if not wholeHouseBuildingEnvelope.groundFloor_Building.Kitchen.inside_wall1a.Wall.twoStar_RadEx.use_A_in then 1 else 0)+(if not wholeHouseBuildingEnvelope.groundFloor_Building.Kitchen.inside_wall2.Wall.twoStar_RadEx.use_A_in then 1 else 0)+(if not wholeHouseBuildingEnvelope.groundFloor_Building.Kitchen.Ceiling.Wall.twoStar_RadEx.use_A_in then 1 else 0)+(if not wholeHouseBuildingEnvelope.groundFloor_Building.Kitchen.floor.Wall.twoStar_RadEx.use_A_in then 1 else 0)+(if not wholeHouseBuildingEnvelope.groundFloor_Building.Kitchen.inside_wall1b.Wall.twoStar_RadEx.use_A_in then 1 else 0)+(if not wholeHouseBuildingEnvelope.groundFloor_Building.Corridor.outside_wall1.Wall.twoStar_RadEx.use_A_in then 1 else 0)+(if not wholeHouseBuildingEnvelope.groundFloor_Building.Corridor.outside_wall1.Door.twoStar_RadEx.use_A_in then 1 else 0)+(if not wholeHouseBuildingEnvelope.groundFloor_Building.Corridor.outside_wall1.Door.twoStar_RadEx1.use_A_in then 1 else 0)+(if wholeHouseBuildingEnvelope.groundFloor_Building.Corridor.outside_wall1.heatTransfer_Outside.calcMethod == AixLib.ThermalZones.HighOrder.Components.Types.CalcMethodConvectiveHeatTransfer. DIN_6946 then 1 else (if wholeHouseBuildingEnvelope.groundFloor_Building.Corridor.outside_wall1.heatTransfer_Outside.calcMethod == AixLib.ThermalZones.HighOrder.Components.Types.CalcMethodConvectiveHeatTransfer. ASHRAE_Fundamentals then 1 else 2))+(if not wholeHouseBuildingEnvelope.groundFloor_Building.Corridor.inside_wall1.Wall.twoStar_RadEx.use_A_in then 1 else 0)+(if not wholeHouseBuildingEnvelope.groundFloor_Building.Corridor.inside_wall2a.Wall.twoStar_RadEx.use_A_in then 1 else 0)+(if not wholeHouseBuildingEnvelope.groundFloor_Building.Corridor.inside_wall3.Wall.twoStar_RadEx.use_A_in then 1 else 0)+(if not wholeHouseBuildingEnvelope.groundFloor_Building.Corridor.Ceiling.Wall.twoStar_RadEx.use_A_in then 1 else 0)+(if not wholeHouseBuildingEnvelope.groundFloor_Building.Corridor.floor.Wall.twoStar_RadEx.use_A_in then 1 else 0)+(if not wholeHouseBuildingEnvelope.groundFloor_Building.Corridor.inside_wall2b.Wall.twoStar_RadEx.use_A_in then 1 else 0)+(if not wholeHouseBuildingEnvelope.upperFloor_Building.Bedroom.outside_wall1.Wall.twoStar_RadEx.use_A_in then 1 else 0)+(if wholeHouseBuildingEnvelope.upperFloor_Building.Bedroom.outside_wall1.heatTransfer_Outside.calcMethod == AixLib.ThermalZones.HighOrder.Components.Types.CalcMethodConvectiveHeatTransfer. DIN_6946 then 1 else (if wholeHouseBuildingEnvelope.upperFloor_Building.Bedroom.outside_wall1.heatTransfer_Outside.calcMethod == AixLib.ThermalZones.HighOrder.Components.Types.CalcMethodConvectiveHeatTransfer. ASHRAE_Fundamentals then 1 else 2))+(if not wholeHouseBuildingEnvelope.upperFloor_Building.Bedroom.outside_wall2.Wall.twoStar_RadEx.use_A_in then 1 else 0)+(if wholeHouseBuildingEnvelope.upperFloor_Building.Bedroom.outside_wall2.heatTransfer_Outside.calcMethod == AixLib.ThermalZones.HighOrder.Components.Types.CalcMethodConvectiveHeatTransfer. DIN_6946 then 1 else (if wholeHouseBuildingEnvelope.upperFloor_Building.Bedroom.outside_wall2.heatTransfer_Outside.calcMethod == AixLib.ThermalZones.HighOrder.Components.Types.CalcMethodConvectiveHeatTransfer. ASHRAE_Fundamentals then 1 else 2))+(if not wholeHouseBuildingEnvelope.upperFloor_Building.Bedroom.inside_wall1a.Wall.twoStar_RadEx.use_A_in then 1 else 0)+(if not wholeHouseBuildingEnvelope.upperFloor_Building.Bedroom.inside_wall2.Wall.twoStar_RadEx.use_A_in then 1 else 0)+(if not wholeHouseBuildingEnvelope.upperFloor_Building.Bedroom.Ceiling.Wall.twoStar_RadEx.use_A_in then 1 else 0)+(if not wholeHouseBuildingEnvelope.upperFloor_Building.Bedroom.floor.Wall.twoStar_RadEx.use_A_in then 1 else 0)+(if not wholeHouseBuildingEnvelope.upperFloor_Building.Bedroom.roof.Wall.twoStar_RadEx.use_A_in then 1 else 0)+(if wholeHouseBuildingEnvelope.upperFloor_Building.Bedroom.roof.heatTransfer_Outside.calcMethod == AixLib.ThermalZones.HighOrder.Components.Types.CalcMethodConvectiveHeatTransfer. DIN_6946 then 1 else (if wholeHouseBuildingEnvelope.upperFloor_Building.Bedroom.roof.heatTransfer_Outside.calcMethod == AixLib.ThermalZones.HighOrder.Components.Types.CalcMethodConvectiveHeatTransfer. ASHRAE_Fundamentals then 1 else 2))+(if not wholeHouseBuildingEnvelope.upperFloor_Building.Bedroom.inside_wall1b.Wall.twoStar_RadEx.use_A_in then 1 else 0)+(if not wholeHouseBuildingEnvelope.upperFloor_Building.Children1.outside_wall1.Wall.twoStar_RadEx.use_A_in then 1 else 0)+(if wholeHouseBuildingEnvelope.upperFloor_Building.Children1.outside_wall1.heatTransfer_Outside.calcMethod == AixLib.ThermalZones.HighOrder.Components.Types.CalcMethodConvectiveHeatTransfer. DIN_6946 then 1 else (if wholeHouseBuildingEnvelope.upperFloor_Building.Children1.outside_wall1.heatTransfer_Outside.calcMethod == AixLib.ThermalZones.HighOrder.Components.Types.CalcMethodConvectiveHeatTransfer. ASHRAE_Fundamentals then 1 else 2))+(if not wholeHouseBuildingEnvelope.upperFloor_Building.Children1.outside_wall2.Wall.twoStar_RadEx.use_A_in then 1 else 0)+(if wholeHouseBuildingEnvelope.upperFloor_Building.Children1.outside_wall2.heatTransfer_Outside.calcMethod == AixLib.ThermalZones.HighOrder.Components.Types.CalcMethodConvectiveHeatTransfer. DIN_6946 then 1 else (if wholeHouseBuildingEnvelope.upperFloor_Building.Children1.outside_wall2.heatTransfer_Outside.calcMethod == AixLib.ThermalZones.HighOrder.Components.Types.CalcMethodConvectiveHeatTransfer. ASHRAE_Fundamentals then 1 else 2))+(if not wholeHouseBuildingEnvelope.upperFloor_Building.Children1.inside_wall1.Wall.twoStar_RadEx.use_A_in then 1 else 0)+(if not wholeHouseBuildingEnvelope.upperFloor_Building.Children1.inside_wall2.Wall.twoStar_RadEx.use_A_in then 1 else 0)+(if not wholeHouseBuildingEnvelope.upperFloor_Building.Children1.Ceiling.Wall.twoStar_RadEx.use_A_in then 1 else 0)+(if not wholeHouseBuildingEnvelope.upperFloor_Building.Children1.floor.Wall.twoStar_RadEx.use_A_in then 1 else 0)+(if not wholeHouseBuildingEnvelope.upperFloor_Building.Children1.roof.Wall.twoStar_RadEx.use_A_in then 1 else 0)+(if wholeHouseBuildingEnvelope.upperFloor_Building.Children1.roof.heatTransfer_Outside.calcMethod == AixLib.ThermalZones.HighOrder.Components.Types.CalcMethodConvectiveHeatTransfer. DIN_6946 then 1 else (if wholeHouseBuildingEnvelope.upperFloor_Building.Children1.roof.heatTransfer_Outside.calcMethod == AixLib.ThermalZones.HighOrder.Components.Types.CalcMethodConvectiveHeatTransfer. ASHRAE_Fundamentals then 1 else 2))+(if not wholeHouseBuildingEnvelope.upperFloor_Building.Bath.outside_wall1.Wall.twoStar_RadEx.use_A_in then 1 else 0)+(if wholeHouseBuildingEnvelope.upperFloor_Building.Bath.outside_wall1.heatTransfer_Outside.calcMethod == AixLib.ThermalZones.HighOrder.Components.Types.CalcMethodConvectiveHeatTransfer. DIN_6946 then 1 else (if wholeHouseBuildingEnvelope.upperFloor_Building.Bath.outside_wall1.heatTransfer_Outside.calcMethod == AixLib.ThermalZones.HighOrder.Components.Types.CalcMethodConvectiveHeatTransfer. ASHRAE_Fundamentals then 1 else 2))+(if not wholeHouseBuildingEnvelope.upperFloor_Building.Bath.outside_wall2.Wall.twoStar_RadEx.use_A_in then 1 else 0)+(if wholeHouseBuildingEnvelope.upperFloor_Building.Bath.outside_wall2.heatTransfer_Outside.calcMethod == AixLib.ThermalZones.HighOrder.Components.Types.CalcMethodConvectiveHeatTransfer. DIN_6946 then 1 else (if wholeHouseBuildingEnvelope.upperFloor_Building.Bath.outside_wall2.heatTransfer_Outside.calcMethod == AixLib.ThermalZones.HighOrder.Components.Types.CalcMethodConvectiveHeatTransfer. ASHRAE_Fundamentals then 1 else 2))+(if not wholeHouseBuildingEnvelope.upperFloor_Building.Bath.inside_wall1.Wall.twoStar_RadEx.use_A_in then 1 else 0)+(if not wholeHouseBuildingEnvelope.upperFloor_Building.Bath.inside_wall2.Wall.twoStar_RadEx.use_A_in then 1 else 0)+(if not wholeHouseBuildingEnvelope.upperFloor_Building.Bath.Ceiling.Wall.twoStar_RadEx.use_A_in then 1 else 0)+(if not wholeHouseBuildingEnvelope.upperFloor_Building.Bath.floor.Wall.twoStar_RadEx.use_A_in then 1 else 0)+(if not wholeHouseBuildingEnvelope.upperFloor_Building.Bath.roof.Wall.twoStar_RadEx.use_A_in then 1 else 0)+(if wholeHouseBuildingEnvelope.upperFloor_Building.Bath.roof.heatTransfer_Outside.calcMethod == AixLib.ThermalZones.HighOrder.Components.Types.CalcMethodConvectiveHeatTransfer. DIN_6946 then 1 else (if wholeHouseBuildingEnvelope.upperFloor_Building.Bath.roof.heatTransfer_Outside.calcMethod == AixLib.ThermalZones.HighOrder.Components.Types.CalcMethodConvectiveHeatTransfer. ASHRAE_Fundamentals then 1 else 2))+(if not wholeHouseBuildingEnvelope.upperFloor_Building.Children2.outside_wall1.Wall.twoStar_RadEx.use_A_in then 1 else 0)+(if wholeHouseBuildingEnvelope.upperFloor_Building.Children2.outside_wall1.heatTransfer_Outside.calcMethod == AixLib.ThermalZones.HighOrder.Components.Types.CalcMethodConvectiveHeatTransfer. DIN_6946 then 1 else (if wholeHouseBuildingEnvelope.upperFloor_Building.Children2.outside_wall1.heatTransfer_Outside.calcMethod == AixLib.ThermalZones.HighOrder.Components.Types.CalcMethodConvectiveHeatTransfer. ASHRAE_Fundamentals then 1 else 2))+(if not wholeHouseBuildingEnvelope.upperFloor_Building.Children2.outside_wall2.Wall.twoStar_RadEx.use_A_in then 1 else 0)+(if wholeHouseBuildingEnvelope.upperFloor_Building.Children2.outside_wall2.heatTransfer_Outside.calcMethod == AixLib.ThermalZones.HighOrder.Components.Types.CalcMethodConvectiveHeatTransfer. DIN_6946 then 1 else (if wholeHouseBuildingEnvelope.upperFloor_Building.Children2.outside_wall2.heatTransfer_Outside.calcMethod == AixLib.ThermalZones.HighOrder.Components.Types.CalcMethodConvectiveHeatTransfer. ASHRAE_Fundamentals then 1 else 2))+(if not wholeHouseBuildingEnvelope.upperFloor_Building.Children2.inside_wall1a.Wall.twoStar_RadEx.use_A_in then 1 else 0)+(if not wholeHouseBuildingEnvelope.upperFloor_Building.Children2.inside_wall2.Wall.twoStar_RadEx.use_A_in then 1 else 0)+(if not wholeHouseBuildingEnvelope.upperFloor_Building.Children2.Ceiling.Wall.twoStar_RadEx.use_A_in then 1 else 0)+(if not wholeHouseBuildingEnvelope.upperFloor_Building.Children2.floor.Wall.twoStar_RadEx.use_A_in then 1 else 0)+(if not wholeHouseBuildingEnvelope.upperFloor_Building.Children2.roof.Wall.twoStar_RadEx.use_A_in then 1 else 0)+(if wholeHouseBuildingEnvelope.upperFloor_Building.Children2.roof.heatTransfer_Outside.calcMethod == AixLib.ThermalZones.HighOrder.Components.Types.CalcMethodConvectiveHeatTransfer. DIN_6946 then 1 else (if wholeHouseBuildingEnvelope.upperFloor_Building.Children2.roof.heatTransfer_Outside.calcMethod == AixLib.ThermalZones.HighOrder.Components.Types.CalcMethodConvectiveHeatTransfer. ASHRAE_Fundamentals then 1 else 2))+(if not wholeHouseBuildingEnvelope.upperFloor_Building.Children2.inside_wall1b.Wall.twoStar_RadEx.use_A_in then 1 else 0)+(if not wholeHouseBuildingEnvelope.upperFloor_Building.Corridor.outside_wall1.Wall.twoStar_RadEx.use_A_in then 1 else 0)+(if wholeHouseBuildingEnvelope.upperFloor_Building.Corridor.outside_wall1.heatTransfer_Outside.calcMethod == AixLib.ThermalZones.HighOrder.Components.Types.CalcMethodConvectiveHeatTransfer. DIN_6946 then 1 else (if wholeHouseBuildingEnvelope.upperFloor_Building.Corridor.outside_wall1.heatTransfer_Outside.calcMethod == AixLib.ThermalZones.HighOrder.Components.Types.CalcMethodConvectiveHeatTransfer. ASHRAE_Fundamentals then 1 else 2))+(if not wholeHouseBuildingEnvelope.upperFloor_Building.Corridor.inner_wall1.Wall.twoStar_RadEx.use_A_in then 1 else 0)+(if not wholeHouseBuildingEnvelope.upperFloor_Building.Corridor.inside_wall2a.Wall.twoStar_RadEx.use_A_in then 1 else 0)+(if not wholeHouseBuildingEnvelope.upperFloor_Building.Corridor.inside_wall3.Wall.twoStar_RadEx.use_A_in then 1 else 0)+(if not wholeHouseBuildingEnvelope.upperFloor_Building.Corridor.Ceiling.Wall.twoStar_RadEx.use_A_in then 1 else 0)+(if not wholeHouseBuildingEnvelope.upperFloor_Building.Corridor.floor.Wall.twoStar_RadEx.use_A_in then 1 else 0)+(if not wholeHouseBuildingEnvelope.upperFloor_Building.Corridor.inside_wall2b.Wall.twoStar_RadEx.use_A_in then 1 else 0)+(if not wholeHouseBuildingEnvelope.upperFloor_Building.Corridor.roof.Wall.twoStar_RadEx.use_A_in then 1 else 0)+(if wholeHouseBuildingEnvelope.upperFloor_Building.Corridor.roof.heatTransfer_Outside.calcMethod == AixLib.ThermalZones.HighOrder.Components.Types.CalcMethodConvectiveHeatTransfer. DIN_6946 then 1 else (if wholeHouseBuildingEnvelope.upperFloor_Building.Corridor.roof.heatTransfer_Outside.calcMethod == AixLib.ThermalZones.HighOrder.Components.Types.CalcMethodConvectiveHeatTransfer. ASHRAE_Fundamentals then 1 else 2))+(if not wholeHouseBuildingEnvelope.attic_2Ro_5Rooms.roof1.Wall.twoStar_RadEx.use_A_in then 1 else 0)+(if wholeHouseBuildingEnvelope.attic_2Ro_5Rooms.roof1.heatTransfer_Outside.calcMethod == AixLib.ThermalZones.HighOrder.Components.Types.CalcMethodConvectiveHeatTransfer. DIN_6946 then 1 else (if wholeHouseBuildingEnvelope.attic_2Ro_5Rooms.roof1.heatTransfer_Outside.calcMethod == AixLib.ThermalZones.HighOrder.Components.Types.CalcMethodConvectiveHeatTransfer. ASHRAE_Fundamentals then 1 else 2))+(if not wholeHouseBuildingEnvelope.attic_2Ro_5Rooms.roof2.Wall.twoStar_RadEx.use_A_in then 1 else 0)+(if wholeHouseBuildingEnvelope.attic_2Ro_5Rooms.roof2.heatTransfer_Outside.calcMethod == AixLib.ThermalZones.HighOrder.Components.Types.CalcMethodConvectiveHeatTransfer. DIN_6946 then 1 else (if wholeHouseBuildingEnvelope.attic_2Ro_5Rooms.roof2.heatTransfer_Outside.calcMethod == AixLib.ThermalZones.HighOrder.Components.Types.CalcMethodConvectiveHeatTransfer. ASHRAE_Fundamentals then 1 else 2))+(if not wholeHouseBuildingEnvelope.attic_2Ro_5Rooms.floorRoom2.Wall.twoStar_RadEx.use_A_in then 1 else 0)+(if not wholeHouseBuildingEnvelope.attic_2Ro_5Rooms.floorRoom1.Wall.twoStar_RadEx.use_A_in then 1 else 0)+(if not wholeHouseBuildingEnvelope.attic_2Ro_5Rooms.floorRoom3.Wall.twoStar_RadEx.use_A_in then 1 else 0)+(if not wholeHouseBuildingEnvelope.attic_2Ro_5Rooms.floorRoom4.Wall.twoStar_RadEx.use_A_in then 1 else 0)+(if not wholeHouseBuildingEnvelope.attic_2Ro_5Rooms.floorRoom5.Wall.twoStar_RadEx.use_A_in then 1 else 0)+(if not wholeHouseBuildingEnvelope.attic_2Ro_5Rooms.OW1.Wall.twoStar_RadEx.use_A_in then 1 else 0)+(if wholeHouseBuildingEnvelope.attic_2Ro_5Rooms.OW1.heatTransfer_Outside.calcMethod == AixLib.ThermalZones.HighOrder.Components.Types.CalcMethodConvectiveHeatTransfer. DIN_6946 then 1 else (if wholeHouseBuildingEnvelope.attic_2Ro_5Rooms.OW1.heatTransfer_Outside.calcMethod == AixLib.ThermalZones.HighOrder.Components.Types.CalcMethodConvectiveHeatTransfer. ASHRAE_Fundamentals then 1 else 2))+(if not wholeHouseBuildingEnvelope.attic_2Ro_5Rooms.OW2.Wall.twoStar_RadEx.use_A_in then 1 else 0)+(if wholeHouseBuildingEnvelope.attic_2Ro_5Rooms.OW2.heatTransfer_Outside.calcMethod == AixLib.ThermalZones.HighOrder.Components.Types.CalcMethodConvectiveHeatTransfer. DIN_6946 then 1 else (if wholeHouseBuildingEnvelope.attic_2Ro_5Rooms.OW2.heatTransfer_Outside.calcMethod == AixLib.ThermalZones.HighOrder.Components.Types.CalcMethodConvectiveHeatTransfer. ASHRAE_Fundamentals then 1 else 2))+5*wholeHouseBuildingEnvelope.groundFloor_Building.Livingroom.airload.dynBal.nPorts +5*wholeHouseBuildingEnvelope.groundFloor_Building.Hobby.airload.dynBal.nPorts +5*wholeHouseBuildingEnvelope.groundFloor_Building.WC_Storage.airload.dynBal.nPorts +5*wholeHouseBuildingEnvelope.groundFloor_Building.Kitchen.airload.dynBal.nPorts +5*wholeHouseBuildingEnvelope.groundFloor_Building.Corridor.airload.dynBal.nPorts +5*wholeHouseBuildingEnvelope.upperFloor_Building.Bedroom.airload.dynBal.nPorts +5*wholeHouseBuildingEnvelope.upperFloor_Building.Children1.airload.dynBal.nPorts +5*wholeHouseBuildingEnvelope.upperFloor_Building.Bath.airload.dynBal.nPorts+5 *wholeHouseBuildingEnvelope.upperFloor_Building.Children2.airload.dynBal.nPorts +5*wholeHouseBuildingEnvelope.upperFloor_Building.Corridor.airload.dynBal.nPorts +5*wholeHouseBuildingEnvelope.attic_2Ro_5Rooms.airload.dynBal.nPorts +scalar equations. +However, exploiting the given numerical settings of parameters gives the same number of unknowns and equations: + 10085 +Check of AixLib.ThermalZones.HighOrder.Examples.OFDHeatLoad successful. +Warning: WARNINGS have been issued. +Declaring variable: Boolean rCheck ; + +Modelica.Utilities.Streams.print(" { \"file\" : \"AixLib/Resources/Scripts/Dymola/ThermalZones/HighOrder/Examples/OFDHeatLoad.mos\",", "AixLib.ThermalZones.HighOrder.Examples.OFDHeatLoad.statistics.log"); +Modelica.Utilities.Streams.print(" \"model\" : \"AixLib.ThermalZones.HighOrder.Examples.OFDHeatLoad\",", "AixLib.ThermalZones.HighOrder.Examples.OFDHeatLoad.statistics.log"); +Modelica.Utilities.Streams.print(" \"check\" : {", "AixLib.ThermalZones.HighOrder.Examples.OFDHeatLoad.statistics.log"); +Modelica.Utilities.Streams.print(" \"command\" : \"checkModel(\\\"AixLib.ThermalZones.HighOrder.Examples.OFDHeatLoad\\\");\",", "AixLib.ThermalZones.HighOrder.Examples.OFDHeatLoad.statistics.log"); +Modelica.Utilities.Streams.print(" \"result\" : " + String(rCheck), "AixLib.ThermalZones.HighOrder.Examples.OFDHeatLoad.statistics.log"); +Modelica.Utilities.Streams.print(" },", "AixLib.ThermalZones.HighOrder.Examples.OFDHeatLoad.statistics.log"); + + +rScript=RunScript("modelica://AixLib/Resources/Scripts/Dymola/ThermalZones/HighOrder/Examples/OFDHeatLoad.mos"); +simulateModel("AixLib.ThermalZones.HighOrder.Examples.OFDHeatLoad", startTime=0, stopTime=25920000, outputInterval=3600, tolerance=1e-6, method="dassl", resultFile="AixLib.ThermalZones.HighOrder.Examples.OFDHeatLoad"); +Translation of AixLib.ThermalZones.HighOrder.Examples.OFDHeatLoad +Warning: Base class Medium is not transitively non-replaceable, + since it is a short class equal to a replaceable class. + File: /tmp/tmp-AixLib-0-jodv2jcy/AixLib/ThermalZones/HighOrder/House/OFD_MiddleInnerLoadWall/BuildingEnvelope/WholeHouseBuildingEnvelope.mo, line 193 + Component context: AixLib.ThermalZones.HighOrder.House.OFD_MiddleInnerLoadWall.BuildingEnvelope.WholeHouseBuildingEnvelope.Medium + Component declared as Attic_Ro2Lf5 attic_2Ro_5Rooms in AixLib.ThermalZones.HighOrder.House.OFD_MiddleInnerLoadWall.BuildingEnvelope.WholeHouseBuildingEnvelope +Warning: Base class Medium is not transitively non-replaceable, + since it is a short class equal to a replaceable class. + File: /tmp/tmp-AixLib-0-jodv2jcy/AixLib/ThermalZones/HighOrder/House/OFD_MiddleInnerLoadWall/BuildingEnvelope/WholeHouseBuildingEnvelope.mo, line 193 + Component context: AixLib.ThermalZones.HighOrder.House.OFD_MiddleInnerLoadWall.BuildingEnvelope.WholeHouseBuildingEnvelope.Medium + Component declared as MixingVolumeMoistAir airload in AixLib.ThermalZones.HighOrder.Rooms.BaseClasses.PartialRoom +Warning: Base class Medium is not transitively non-replaceable, + since it is a short class equal to a replaceable class. + File: /tmp/tmp-AixLib-0-jodv2jcy/AixLib/ThermalZones/HighOrder/House/OFD_MiddleInnerLoadWall/BuildingEnvelope/WholeHouseBuildingEnvelope.mo, line 193 + Component context: AixLib.ThermalZones.HighOrder.House.OFD_MiddleInnerLoadWall.BuildingEnvelope.WholeHouseBuildingEnvelope.Medium + Component declared as VesselFluidPorts_b ports in AixLib.Fluid.MixingVolumes.BaseClasses.PartialMixingVolume +Warning: Base class Medium is not transitively non-replaceable, + since it is a short class equal to a replaceable class. + File: /tmp/tmp-AixLib-0-jodv2jcy/AixLib/ThermalZones/HighOrder/House/OFD_MiddleInnerLoadWall/BuildingEnvelope/WholeHouseBuildingEnvelope.mo, line 193 + Component context: AixLib.ThermalZones.HighOrder.House.OFD_MiddleInnerLoadWall.BuildingEnvelope.WholeHouseBuildingEnvelope.Medium + Component declared as VesselFluidPorts_b ports in AixLib.Fluid.MixingVolumes.BaseClasses.PartialMixingVolume +Warning: Base class Medium is not transitively non-replaceable, + since it is a short class equal to a replaceable class. + File: /tmp/tmp-AixLib-0-jodv2jcy/AixLib/ThermalZones/HighOrder/House/OFD_MiddleInnerLoadWall/BuildingEnvelope/WholeHouseBuildingEnvelope.mo, line 193 + Component context: AixLib.ThermalZones.HighOrder.House.OFD_MiddleInnerLoadWall.BuildingEnvelope.WholeHouseBuildingEnvelope.Medium + Component declared as FluidPort_a port_a in AixLib.Fluid.Interfaces.PartialTwoPort +Warning: Base class Medium is not transitively non-replaceable, + since it is a short class equal to a replaceable class. + File: /tmp/tmp-AixLib-0-jodv2jcy/AixLib/ThermalZones/HighOrder/House/OFD_MiddleInnerLoadWall/BuildingEnvelope/WholeHouseBuildingEnvelope.mo, line 193 + Component context: AixLib.ThermalZones.HighOrder.House.OFD_MiddleInnerLoadWall.BuildingEnvelope.WholeHouseBuildingEnvelope.Medium + Component declared as FluidPort_a port_a in AixLib.Fluid.Interfaces.PartialTwoPort +Warning: Base class Medium is not transitively non-replaceable, + since it is a short class equal to a replaceable class. + File: /tmp/tmp-AixLib-0-jodv2jcy/AixLib/ThermalZones/HighOrder/House/OFD_MiddleInnerLoadWall/BuildingEnvelope/WholeHouseBuildingEnvelope.mo, line 193 + Component context: AixLib.ThermalZones.HighOrder.House.OFD_MiddleInnerLoadWall.BuildingEnvelope.WholeHouseBuildingEnvelope.Medium + Component declared as FluidPort_b port_b in AixLib.Fluid.Interfaces.PartialTwoPort +Warning: Base class Medium is not transitively non-replaceable, + since it is a short class equal to a replaceable class. + File: /tmp/tmp-AixLib-0-jodv2jcy/AixLib/ThermalZones/HighOrder/House/OFD_MiddleInnerLoadWall/BuildingEnvelope/WholeHouseBuildingEnvelope.mo, line 193 + Component context: AixLib.ThermalZones.HighOrder.House.OFD_MiddleInnerLoadWall.BuildingEnvelope.WholeHouseBuildingEnvelope.Medium + Component declared as FluidPort_b port_b in AixLib.Fluid.Interfaces.PartialTwoPort +Warning: Base class Medium is not transitively non-replaceable, + since it is a short class equal to a replaceable class. + File: /tmp/tmp-AixLib-0-jodv2jcy/AixLib/ThermalZones/HighOrder/House/OFD_MiddleInnerLoadWall/BuildingEnvelope/WholeHouseBuildingEnvelope.mo, line 193 + Component context: AixLib.ThermalZones.HighOrder.House.OFD_MiddleInnerLoadWall.BuildingEnvelope.WholeHouseBuildingEnvelope.Medium + Component declared as StaticTwoPortConservationEquation steBal in AixLib.Fluid.MixingVolumes.BaseClasses.PartialMixingVolume +Warning: Base class Medium is not transitively non-replaceable, + since it is a short class equal to a replaceable class. + File: /tmp/tmp-AixLib-0-jodv2jcy/AixLib/ThermalZones/HighOrder/House/OFD_MiddleInnerLoadWall/BuildingEnvelope/WholeHouseBuildingEnvelope.mo, line 193 + Component context: AixLib.ThermalZones.HighOrder.House.OFD_MiddleInnerLoadWall.BuildingEnvelope.WholeHouseBuildingEnvelope.Medium + Component declared as StaticTwoPortConservationEquation steBal in AixLib.Fluid.MixingVolumes.BaseClasses.PartialMixingVolume +Warning: Base class Medium is not transitively non-replaceable, + since it is a short class equal to a replaceable class. + File: /tmp/tmp-AixLib-0-jodv2jcy/AixLib/ThermalZones/HighOrder/House/OFD_MiddleInnerLoadWall/BuildingEnvelope/WholeHouseBuildingEnvelope.mo, line 193 + Component context: AixLib.ThermalZones.HighOrder.House.OFD_MiddleInnerLoadWall.BuildingEnvelope.WholeHouseBuildingEnvelope.Medium + Component declared as ConservationEquation dynBal in AixLib.Fluid.MixingVolumes.BaseClasses.PartialMixingVolume +Warning: Base class Medium is not transitively non-replaceable, + since it is a short class equal to a replaceable class. + File: /tmp/tmp-AixLib-0-jodv2jcy/AixLib/ThermalZones/HighOrder/House/OFD_MiddleInnerLoadWall/BuildingEnvelope/WholeHouseBuildingEnvelope.mo, line 193 + Component context: AixLib.ThermalZones.HighOrder.House.OFD_MiddleInnerLoadWall.BuildingEnvelope.WholeHouseBuildingEnvelope.Medium + Component declared as VesselFluidPorts_b ports in AixLib.Fluid.Interfaces.ConservationEquation +Warning: Base class Medium is not transitively non-replaceable, + since it is a short class equal to a replaceable class. + File: /tmp/tmp-AixLib-0-jodv2jcy/AixLib/ThermalZones/HighOrder/House/OFD_MiddleInnerLoadWall/BuildingEnvelope/WholeHouseBuildingEnvelope.mo, line 193 + Component context: AixLib.ThermalZones.HighOrder.House.OFD_MiddleInnerLoadWall.BuildingEnvelope.WholeHouseBuildingEnvelope.Medium + Component declared as VesselFluidPorts_b ports in AixLib.Fluid.Interfaces.ConservationEquation +Warning: Base class Medium is not transitively non-replaceable, + since it is a short class equal to a replaceable class. + File: /tmp/tmp-AixLib-0-jodv2jcy/AixLib/ThermalZones/HighOrder/House/OFD_MiddleInnerLoadWall/BuildingEnvelope/WholeHouseBuildingEnvelope.mo, line 193 + Component context: AixLib.ThermalZones.HighOrder.House.OFD_MiddleInnerLoadWall.BuildingEnvelope.WholeHouseBuildingEnvelope.Medium + Component declared as ConservationEquation dynBal in AixLib.Fluid.MixingVolumes.BaseClasses.PartialMixingVolume +Warning: Base class Medium is not transitively non-replaceable, + since it is a short class equal to a replaceable class. + File: /tmp/tmp-AixLib-0-jodv2jcy/AixLib/ThermalZones/HighOrder/House/OFD_MiddleInnerLoadWall/BuildingEnvelope/WholeHouseBuildingEnvelope.mo, line 193 + Component context: AixLib.ThermalZones.HighOrder.House.OFD_MiddleInnerLoadWall.BuildingEnvelope.WholeHouseBuildingEnvelope.Medium + Component declared as MixingVolumeMoistAir airload in AixLib.ThermalZones.HighOrder.Rooms.BaseClasses.PartialRoom +Warning: Base class Medium is not transitively non-replaceable, + since it is a short class equal to a replaceable class. + File: /tmp/tmp-AixLib-0-jodv2jcy/AixLib/ThermalZones/HighOrder/House/OFD_MiddleInnerLoadWall/BuildingEnvelope/WholeHouseBuildingEnvelope.mo, line 193 + Component context: AixLib.ThermalZones.HighOrder.House.OFD_MiddleInnerLoadWall.BuildingEnvelope.WholeHouseBuildingEnvelope.Medium + Component declared as VesselFluidPorts_b ports in AixLib.ThermalZones.HighOrder.Rooms.BaseClasses.PartialRoom +Warning: Base class Medium is not transitively non-replaceable, + since it is a short class equal to a replaceable class. + File: /tmp/tmp-AixLib-0-jodv2jcy/AixLib/ThermalZones/HighOrder/House/OFD_MiddleInnerLoadWall/BuildingEnvelope/WholeHouseBuildingEnvelope.mo, line 193 + Component context: AixLib.ThermalZones.HighOrder.House.OFD_MiddleInnerLoadWall.BuildingEnvelope.WholeHouseBuildingEnvelope.Medium + Component declared as VesselFluidPorts_b ports in AixLib.ThermalZones.HighOrder.Rooms.BaseClasses.PartialRoom +Warning: Base class Medium is not transitively non-replaceable, + since it is a short class equal to a replaceable class. + File: /tmp/tmp-AixLib-0-jodv2jcy/AixLib/ThermalZones/HighOrder/House/OFD_MiddleInnerLoadWall/BuildingEnvelope/WholeHouseBuildingEnvelope.mo, line 193 + Context: AixLib.ThermalZones.HighOrder.House.OFD_MiddleInnerLoadWall.BuildingEnvelope.WholeHouseBuildingEnvelope.Medium +Warning: Inconsistency for connectors dimensioned using parameter with annotation(Dialog(connectorSizing=true)). + Some connector elements are not connected. +This is either because the connections and/or parameters has been edited textually to an inconsistent state + or because the default for the parameter is not 0. The unconnected connectors are: + wholeHouseBuildingEnvelope.attic_2Ro_5Rooms.ports[1] + wholeHouseBuildingEnvelope.attic_2Ro_5Rooms.ports[2] + +The DAE has 10085 scalar unknowns and 10085 scalar equations. +Redundant consistent initial conditions. +Removed the following equations which are redundant and consistent: + wholeHouseBuildingEnvelope.upperFloor_Building.Children2.airload.T = temperature_phX_Unique5(wholeHouseBuildingEnvelope.upperFloor_Building.Children2.airload.p, wholeHouseBuildingEnvelope.upperFloor_Building.Children2.airload.hOut_internal, cat(1, wholeHouseBuildingEnvelope.upperFloor_Building.Children2.airload.Xi, {1-sum(wholeHouseBuildingEnvelope.upperFloor_Building.Children2.airload.Xi)})); + wholeHouseBuildingEnvelope.groundFloor_Building.Livingroom.airload.T = temperature_phX_Unique5(wholeHouseBuildingEnvelope.groundFloor_Building.Livingroom.airload.p, wholeHouseBuildingEnvelope.groundFloor_Building.Livingroom.airload.hOut_internal, cat(1, wholeHouseBuildingEnvelope.groundFloor_Building.Livingroom.airload.Xi, {1-sum(wholeHouseBuildingEnvelope.groundFloor_Building.Livingroom.airload.Xi)})); + wholeHouseBuildingEnvelope.groundFloor_Building.Hobby.airload.T = temperature_phX_Unique5(wholeHouseBuildingEnvelope.groundFloor_Building.Hobby.airload.p, wholeHouseBuildingEnvelope.groundFloor_Building.Hobby.airload.hOut_internal, cat(1, wholeHouseBuildingEnvelope.groundFloor_Building.Hobby.airload.Xi, {1 -sum(wholeHouseBuildingEnvelope.groundFloor_Building.Hobby.airload.Xi)})); + wholeHouseBuildingEnvelope.groundFloor_Building.Corridor.airload.T = temperature_phX_Unique5(wholeHouseBuildingEnvelope.groundFloor_Building.Corridor.airload.p, wholeHouseBuildingEnvelope.groundFloor_Building.Corridor.airload.hOut_internal, cat(1, wholeHouseBuildingEnvelope.groundFloor_Building.Corridor.airload.Xi, {1-sum(wholeHouseBuildingEnvelope.groundFloor_Building.Corridor.airload.Xi)})); + wholeHouseBuildingEnvelope.groundFloor_Building.WC_Storage.airload.T = temperature_phX_Unique5(wholeHouseBuildingEnvelope.groundFloor_Building.WC_Storage.airload.p, wholeHouseBuildingEnvelope.groundFloor_Building.WC_Storage.airload.hOut_internal, cat(1, wholeHouseBuildingEnvelope.groundFloor_Building.WC_Storage.airload.Xi, {1-sum(wholeHouseBuildingEnvelope.groundFloor_Building.WC_Storage.airload.Xi)})); + wholeHouseBuildingEnvelope.groundFloor_Building.Kitchen.airload.T = temperature_phX_Unique5(wholeHouseBuildingEnvelope.groundFloor_Building.Kitchen.airload.p, wholeHouseBuildingEnvelope.groundFloor_Building.Kitchen.airload.hOut_internal, cat(1, wholeHouseBuildingEnvelope.groundFloor_Building.Kitchen.airload.Xi, {1-sum(wholeHouseBuildingEnvelope.groundFloor_Building.Kitchen.airload.Xi)})); + wholeHouseBuildingEnvelope.upperFloor_Building.Bedroom.airload.T = temperature_phX_Unique5(wholeHouseBuildingEnvelope.upperFloor_Building.Bedroom.airload.p, wholeHouseBuildingEnvelope.upperFloor_Building.Bedroom.airload.hOut_internal, cat(1, wholeHouseBuildingEnvelope.upperFloor_Building.Bedroom.airload.Xi, {1 -sum(wholeHouseBuildingEnvelope.upperFloor_Building.Bedroom.airload.Xi)})); + wholeHouseBuildingEnvelope.upperFloor_Building.Children1.airload.T = temperature_phX_Unique5(wholeHouseBuildingEnvelope.upperFloor_Building.Children1.airload.p, wholeHouseBuildingEnvelope.upperFloor_Building.Children1.airload.hOut_internal, cat(1, wholeHouseBuildingEnvelope.upperFloor_Building.Children1.airload.Xi, {1-sum(wholeHouseBuildingEnvelope.upperFloor_Building.Children1.airload.Xi)})); + wholeHouseBuildingEnvelope.upperFloor_Building.Corridor.airload.T = temperature_phX_Unique5(wholeHouseBuildingEnvelope.upperFloor_Building.Corridor.airload.p, wholeHouseBuildingEnvelope.upperFloor_Building.Corridor.airload.hOut_internal, cat(1, wholeHouseBuildingEnvelope.upperFloor_Building.Corridor.airload.Xi, {1-sum(wholeHouseBuildingEnvelope.upperFloor_Building.Corridor.airload.Xi)})); + wholeHouseBuildingEnvelope.upperFloor_Building.Bath.airload.T = temperature_phX_Unique5(wholeHouseBuildingEnvelope.upperFloor_Building.Bath.airload.p, wholeHouseBuildingEnvelope.upperFloor_Building.Bath.airload.hOut_internal, cat(1, wholeHouseBuildingEnvelope.upperFloor_Building.Bath.airload.Xi, {1- sum(wholeHouseBuildingEnvelope.upperFloor_Building.Bath.airload.Xi)})); + +This required evaluation of +the interactive parameters + constRooms[1].k(start = 293.15) + constRooms[2].k(start = 293.15) + constRooms[3].k(start = 288.15) + constRooms[4].k(start = 293.15) + constRooms[5].k(start = 293.15) + constRooms[6].k(start = 293.15) + constRooms[7].k(start = 293.15) + constRooms[8].k(start = 288.15) + constRooms[9].k(start = 297.15) + constRooms[10].k(start = 293.15) + wholeHouseBuildingEnvelope.groundFloor_Building.Corridor.T0_air(start = 288.15) + wholeHouseBuildingEnvelope.groundFloor_Building.Corridor.X_start[1](start = 0.01) + wholeHouseBuildingEnvelope.groundFloor_Building.Hobby.X_start[1](start = 0.01) + wholeHouseBuildingEnvelope.groundFloor_Building.Kitchen.X_start[1](start = 0.01) + wholeHouseBuildingEnvelope.groundFloor_Building.Livingroom.X_start[1](start = 0.01) + wholeHouseBuildingEnvelope.groundFloor_Building.WC_Storage.X_start[1](start = 0.01) + wholeHouseBuildingEnvelope.T0_air(start = 293.15) + wholeHouseBuildingEnvelope.upperFloor_Building.Bath.T0_air(start = 297.15) + wholeHouseBuildingEnvelope.upperFloor_Building.Bath.X_start[1](start = 0.01) + wholeHouseBuildingEnvelope.upperFloor_Building.Bedroom.X_start[1](start = 0.01) + wholeHouseBuildingEnvelope.upperFloor_Building.Children1.X_start[1](start = 0.01) + wholeHouseBuildingEnvelope.upperFloor_Building.Children2.X_start[1](start = 0.01) + wholeHouseBuildingEnvelope.upperFloor_Building.Corridor.T0_air(start = 288.15) + wholeHouseBuildingEnvelope.upperFloor_Building.Corridor.X_start[1](start = 0.01) + +The redundancies involve +initial equations: + wholeHouseBuildingEnvelope.groundFloor_Building.Livingroom.airload.dynBal.medium.T = wholeHouseBuildingEnvelope.groundFloor_Building.Livingroom.airload.dynBal.T_start; + wholeHouseBuildingEnvelope.groundFloor_Building.Livingroom.airload.dynBal.medium.Xi[1] = wholeHouseBuildingEnvelope.groundFloor_Building.Livingroom.airload.dynBal.X_start[1]; + wholeHouseBuildingEnvelope.groundFloor_Building.Hobby.airload.dynBal.medium.T = wholeHouseBuildingEnvelope.groundFloor_Building.Hobby.airload.dynBal.T_start; + wholeHouseBuildingEnvelope.groundFloor_Building.Hobby.airload.dynBal.medium.Xi[1] = wholeHouseBuildingEnvelope.groundFloor_Building.Hobby.airload.dynBal.X_start[1]; + wholeHouseBuildingEnvelope.groundFloor_Building.WC_Storage.airload.dynBal.medium.T = wholeHouseBuildingEnvelope.groundFloor_Building.WC_Storage.airload.dynBal.T_start; + wholeHouseBuildingEnvelope.groundFloor_Building.WC_Storage.airload.dynBal.medium.Xi[1] = wholeHouseBuildingEnvelope.groundFloor_Building.WC_Storage.airload.dynBal.X_start[1]; + wholeHouseBuildingEnvelope.groundFloor_Building.Kitchen.airload.dynBal.medium.T = wholeHouseBuildingEnvelope.groundFloor_Building.Kitchen.airload.dynBal.T_start; + wholeHouseBuildingEnvelope.groundFloor_Building.Kitchen.airload.dynBal.medium.Xi[1] = wholeHouseBuildingEnvelope.groundFloor_Building.Kitchen.airload.dynBal.X_start[1]; + wholeHouseBuildingEnvelope.groundFloor_Building.Corridor.airload.dynBal.medium.T = wholeHouseBuildingEnvelope.groundFloor_Building.Corridor.airload.dynBal.T_start; + wholeHouseBuildingEnvelope.groundFloor_Building.Corridor.airload.dynBal.medium.Xi[1] = wholeHouseBuildingEnvelope.groundFloor_Building.Corridor.airload.dynBal.X_start[1]; + wholeHouseBuildingEnvelope.upperFloor_Building.Bedroom.airload.dynBal.medium.T = wholeHouseBuildingEnvelope.upperFloor_Building.Bedroom.airload.dynBal.T_start; + wholeHouseBuildingEnvelope.upperFloor_Building.Bedroom.airload.dynBal.medium.Xi[1] = wholeHouseBuildingEnvelope.upperFloor_Building.Bedroom.airload.dynBal.X_start[1]; + wholeHouseBuildingEnvelope.upperFloor_Building.Children1.airload.dynBal.medium.T = wholeHouseBuildingEnvelope.upperFloor_Building.Children1.airload.dynBal.T_start; + wholeHouseBuildingEnvelope.upperFloor_Building.Children1.airload.dynBal.medium.Xi[1] = wholeHouseBuildingEnvelope.upperFloor_Building.Children1.airload.dynBal.X_start[1]; + wholeHouseBuildingEnvelope.upperFloor_Building.Bath.airload.dynBal.medium.T = wholeHouseBuildingEnvelope.upperFloor_Building.Bath.airload.dynBal.T_start; + wholeHouseBuildingEnvelope.upperFloor_Building.Bath.airload.dynBal.medium.Xi[1] = wholeHouseBuildingEnvelope.upperFloor_Building.Bath.airload.dynBal.X_start[1]; + wholeHouseBuildingEnvelope.upperFloor_Building.Children2.airload.dynBal.medium.T = wholeHouseBuildingEnvelope.upperFloor_Building.Children2.airload.dynBal.T_start; + wholeHouseBuildingEnvelope.upperFloor_Building.Children2.airload.dynBal.medium.Xi[1] = wholeHouseBuildingEnvelope.upperFloor_Building.Children2.airload.dynBal.X_start[1]; + wholeHouseBuildingEnvelope.upperFloor_Building.Corridor.airload.dynBal.medium.T = wholeHouseBuildingEnvelope.upperFloor_Building.Corridor.airload.dynBal.T_start; + wholeHouseBuildingEnvelope.upperFloor_Building.Corridor.airload.dynBal.medium.Xi[1] = wholeHouseBuildingEnvelope.upperFloor_Building.Corridor.airload.dynBal.X_start[1]; + + +Statistics + +Original Model + Number of components: 2249 + Variables: 21077 + Constants: 100 (100 scalars) + Parameters: 10792 (14111 scalars) + Unknowns: 10185 (10213 scalars) + Differentiated variables: 261 scalars + Equations: 8021 + Nontrivial: 6915 +Translated Model + Constants: 4198 scalars + Free parameters: 1111 scalars + Parameter depending: 10065 scalars + Outputs: 11 scalars + Continuous time states: 251 scalars + Time-varying variables: 2306 scalars + Alias variables: 6744 scalars + Number of mixed real/discrete systems of equations: 0 + Sizes of linear systems of equations: {4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4} + Sizes after manipulation of the linear systems: {0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0} + Sizes of nonlinear systems of equations: {5, 48, 5, 43, 5, 36, 5, 41, 5, 38, 5, 43, 5, 48, 5, 43, 5, 44, 5, 41, 52} + Sizes after manipulation of the nonlinear systems: {4, 9, 4, 8, 4, 7, 4, 8, 4, 7, 4, 8, 4, 9, 4, 8, 4, 9, 4, 8, 10} + Number of numerical Jacobians: 0 + Initialization problem + Sizes of nonlinear systems of equations: {1, 1, 1, 1} + Sizes after manipulation of the nonlinear systems: {0, 1, 0, 1} + Number of numerical Jacobians: 0 + +Sparse solvers enabled: false +Enabled for integrator Jacobian: false +Model sparse and large enough: true. +Sparse solvers are available for dassl, lsodar, cvode, ida, radau, esdirk*, sdirk*. +Enable sparse solvers by setting Advanced.Translation.SparseActivate. +Selected continuous time states +Statically selected continuous time states +wholeHouseBuildingEnvelope.attic_2Ro_5Rooms.airload.dynBal.m +wholeHouseBuildingEnvelope.attic_2Ro_5Rooms.airload.dynBal.medium.Xi[1] +wholeHouseBuildingEnvelope.attic_2Ro_5Rooms.airload.dynBal.U +wholeHouseBuildingEnvelope.attic_2Ro_5Rooms.floorRoom1.Wall.simpleNLayer.cap[1].T +wholeHouseBuildingEnvelope.attic_2Ro_5Rooms.floorRoom1.Wall.simpleNLayer.cap[2].T +wholeHouseBuildingEnvelope.attic_2Ro_5Rooms.floorRoom2.Wall.simpleNLayer.cap[1].T +wholeHouseBuildingEnvelope.attic_2Ro_5Rooms.floorRoom2.Wall.simpleNLayer.cap[2].T +wholeHouseBuildingEnvelope.attic_2Ro_5Rooms.floorRoom3.Wall.simpleNLayer.cap[1].T +wholeHouseBuildingEnvelope.attic_2Ro_5Rooms.floorRoom3.Wall.simpleNLayer.cap[2].T +wholeHouseBuildingEnvelope.attic_2Ro_5Rooms.floorRoom4.Wall.simpleNLayer.cap[1].T +wholeHouseBuildingEnvelope.attic_2Ro_5Rooms.floorRoom4.Wall.simpleNLayer.cap[2].T +wholeHouseBuildingEnvelope.attic_2Ro_5Rooms.floorRoom5.Wall.simpleNLayer.cap[1].T +wholeHouseBuildingEnvelope.attic_2Ro_5Rooms.floorRoom5.Wall.simpleNLayer.cap[2].T +wholeHouseBuildingEnvelope.attic_2Ro_5Rooms.OW1.Wall.simpleNLayer.cap[1].T +wholeHouseBuildingEnvelope.attic_2Ro_5Rooms.OW1.Wall.simpleNLayer.cap[2].T +wholeHouseBuildingEnvelope.attic_2Ro_5Rooms.OW1.Wall.simpleNLayer.cap[3].T +wholeHouseBuildingEnvelope.attic_2Ro_5Rooms.OW1.Wall.simpleNLayer.cap[4].T +wholeHouseBuildingEnvelope.attic_2Ro_5Rooms.OW2.Wall.simpleNLayer.cap[1].T +wholeHouseBuildingEnvelope.attic_2Ro_5Rooms.OW2.Wall.simpleNLayer.cap[2].T +wholeHouseBuildingEnvelope.attic_2Ro_5Rooms.OW2.Wall.simpleNLayer.cap[3].T +wholeHouseBuildingEnvelope.attic_2Ro_5Rooms.OW2.Wall.simpleNLayer.cap[4].T +wholeHouseBuildingEnvelope.attic_2Ro_5Rooms.roof1.Wall.simpleNLayer.cap[1].T +wholeHouseBuildingEnvelope.attic_2Ro_5Rooms.roof2.Wall.simpleNLayer.cap[1].T +wholeHouseBuildingEnvelope.groPlateLowPart[1].cap[1].T +wholeHouseBuildingEnvelope.groPlateLowPart[1].cap[2].T +wholeHouseBuildingEnvelope.groPlateLowPart[1].cap[3].T +wholeHouseBuildingEnvelope.groPlateLowPart[2].cap[1].T +wholeHouseBuildingEnvelope.groPlateLowPart[2].cap[2].T +wholeHouseBuildingEnvelope.groPlateLowPart[2].cap[3].T +wholeHouseBuildingEnvelope.groPlateLowPart[3].cap[1].T +wholeHouseBuildingEnvelope.groPlateLowPart[3].cap[2].T +wholeHouseBuildingEnvelope.groPlateLowPart[3].cap[3].T +wholeHouseBuildingEnvelope.groPlateLowPart[4].cap[1].T +wholeHouseBuildingEnvelope.groPlateLowPart[4].cap[2].T +wholeHouseBuildingEnvelope.groPlateLowPart[4].cap[3].T +wholeHouseBuildingEnvelope.groPlateLowPart[5].cap[1].T +wholeHouseBuildingEnvelope.groPlateLowPart[5].cap[2].T +wholeHouseBuildingEnvelope.groPlateLowPart[5].cap[3].T +wholeHouseBuildingEnvelope.groundFloor_Building.Corridor.Ceiling.Wall.simpleNLayer.cap[1].T +wholeHouseBuildingEnvelope.groundFloor_Building.Corridor.Ceiling.Wall.simpleNLayer.cap[2].T +wholeHouseBuildingEnvelope.groundFloor_Building.Corridor.Ceiling.Wall.simpleNLayer.cap[3].T +wholeHouseBuildingEnvelope.groundFloor_Building.Corridor.floor.Wall.simpleNLayer.cap[1].T +wholeHouseBuildingEnvelope.groundFloor_Building.Corridor.floor.Wall.simpleNLayer.cap[2].T +wholeHouseBuildingEnvelope.groundFloor_Building.Corridor.inside_wall1.Wall.simpleNLayer.cap[1].T +wholeHouseBuildingEnvelope.groundFloor_Building.Corridor.inside_wall1.Wall.simpleNLayer.cap[2].T +wholeHouseBuildingEnvelope.groundFloor_Building.Corridor.inside_wall2a.Wall.simpleNLayer.cap[1].T +wholeHouseBuildingEnvelope.groundFloor_Building.Corridor.inside_wall2a.Wall.simpleNLayer.cap[2].T +wholeHouseBuildingEnvelope.groundFloor_Building.Corridor.inside_wall2b.Wall.simpleNLayer.cap[1].T +wholeHouseBuildingEnvelope.groundFloor_Building.Corridor.inside_wall2b.Wall.simpleNLayer.cap[2].T +wholeHouseBuildingEnvelope.groundFloor_Building.Corridor.inside_wall3.Wall.simpleNLayer.cap[1].T +wholeHouseBuildingEnvelope.groundFloor_Building.Corridor.inside_wall3.Wall.simpleNLayer.cap[2].T +wholeHouseBuildingEnvelope.groundFloor_Building.Corridor.outside_wall1.Wall.simpleNLayer.cap[1].T +wholeHouseBuildingEnvelope.groundFloor_Building.Corridor.outside_wall1.Wall.simpleNLayer.cap[2].T +wholeHouseBuildingEnvelope.groundFloor_Building.Corridor.outside_wall1.Wall.simpleNLayer.cap[3].T +wholeHouseBuildingEnvelope.groundFloor_Building.Corridor.outside_wall1.Wall.simpleNLayer.cap[4].T +wholeHouseBuildingEnvelope.groundFloor_Building.Hobby.Ceiling.Wall.simpleNLayer.cap[1].T +wholeHouseBuildingEnvelope.groundFloor_Building.Hobby.Ceiling.Wall.simpleNLayer.cap[2].T +wholeHouseBuildingEnvelope.groundFloor_Building.Hobby.Ceiling.Wall.simpleNLayer.cap[3].T +wholeHouseBuildingEnvelope.groundFloor_Building.Hobby.floor.Wall.simpleNLayer.cap[1].T +wholeHouseBuildingEnvelope.groundFloor_Building.Hobby.floor.Wall.simpleNLayer.cap[2].T +wholeHouseBuildingEnvelope.groundFloor_Building.Hobby.inside_wall1.Wall.simpleNLayer.cap[1].T +wholeHouseBuildingEnvelope.groundFloor_Building.Hobby.inside_wall1.Wall.simpleNLayer.cap[2].T +wholeHouseBuildingEnvelope.groundFloor_Building.Hobby.inside_wall2.Wall.simpleNLayer.cap[1].T +wholeHouseBuildingEnvelope.groundFloor_Building.Hobby.inside_wall2.Wall.simpleNLayer.cap[2].T +wholeHouseBuildingEnvelope.groundFloor_Building.Hobby.outside_wall1.Wall.simpleNLayer.cap[1].T +wholeHouseBuildingEnvelope.groundFloor_Building.Hobby.outside_wall1.Wall.simpleNLayer.cap[2].T +wholeHouseBuildingEnvelope.groundFloor_Building.Hobby.outside_wall1.Wall.simpleNLayer.cap[3].T +wholeHouseBuildingEnvelope.groundFloor_Building.Hobby.outside_wall1.Wall.simpleNLayer.cap[4].T +wholeHouseBuildingEnvelope.groundFloor_Building.Hobby.outside_wall2.Wall.simpleNLayer.cap[1].T +wholeHouseBuildingEnvelope.groundFloor_Building.Hobby.outside_wall2.Wall.simpleNLayer.cap[2].T +wholeHouseBuildingEnvelope.groundFloor_Building.Hobby.outside_wall2.Wall.simpleNLayer.cap[3].T +wholeHouseBuildingEnvelope.groundFloor_Building.Hobby.outside_wall2.Wall.simpleNLayer.cap[4].T +wholeHouseBuildingEnvelope.groundFloor_Building.Kitchen.Ceiling.Wall.simpleNLayer.cap[1].T +wholeHouseBuildingEnvelope.groundFloor_Building.Kitchen.Ceiling.Wall.simpleNLayer.cap[2].T +wholeHouseBuildingEnvelope.groundFloor_Building.Kitchen.Ceiling.Wall.simpleNLayer.cap[3].T +wholeHouseBuildingEnvelope.groundFloor_Building.Kitchen.floor.Wall.simpleNLayer.cap[1].T +wholeHouseBuildingEnvelope.groundFloor_Building.Kitchen.floor.Wall.simpleNLayer.cap[2].T +wholeHouseBuildingEnvelope.groundFloor_Building.Kitchen.inside_wall1a.Wall.simpleNLayer.cap[1].T +wholeHouseBuildingEnvelope.groundFloor_Building.Kitchen.inside_wall1a.Wall.simpleNLayer.cap[2].T +wholeHouseBuildingEnvelope.groundFloor_Building.Kitchen.inside_wall1b.Wall.simpleNLayer.cap[1].T +wholeHouseBuildingEnvelope.groundFloor_Building.Kitchen.inside_wall1b.Wall.simpleNLayer.cap[2].T +wholeHouseBuildingEnvelope.groundFloor_Building.Kitchen.inside_wall2.Wall.simpleNLayer.cap[1].T +wholeHouseBuildingEnvelope.groundFloor_Building.Kitchen.inside_wall2.Wall.simpleNLayer.cap[2].T +wholeHouseBuildingEnvelope.groundFloor_Building.Kitchen.outside_wall1.Wall.simpleNLayer.cap[1].T +wholeHouseBuildingEnvelope.groundFloor_Building.Kitchen.outside_wall1.Wall.simpleNLayer.cap[2].T +wholeHouseBuildingEnvelope.groundFloor_Building.Kitchen.outside_wall1.Wall.simpleNLayer.cap[3].T +wholeHouseBuildingEnvelope.groundFloor_Building.Kitchen.outside_wall1.Wall.simpleNLayer.cap[4].T +wholeHouseBuildingEnvelope.groundFloor_Building.Kitchen.outside_wall2.Wall.simpleNLayer.cap[1].T +wholeHouseBuildingEnvelope.groundFloor_Building.Kitchen.outside_wall2.Wall.simpleNLayer.cap[2].T +wholeHouseBuildingEnvelope.groundFloor_Building.Kitchen.outside_wall2.Wall.simpleNLayer.cap[3].T +wholeHouseBuildingEnvelope.groundFloor_Building.Kitchen.outside_wall2.Wall.simpleNLayer.cap[4].T +wholeHouseBuildingEnvelope.groundFloor_Building.Livingroom.Ceiling.Wall.simpleNLayer.cap[1].T +wholeHouseBuildingEnvelope.groundFloor_Building.Livingroom.Ceiling.Wall.simpleNLayer.cap[2].T +wholeHouseBuildingEnvelope.groundFloor_Building.Livingroom.Ceiling.Wall.simpleNLayer.cap[3].T +wholeHouseBuildingEnvelope.groundFloor_Building.Livingroom.floor.Wall.simpleNLayer.cap[1].T +wholeHouseBuildingEnvelope.groundFloor_Building.Livingroom.floor.Wall.simpleNLayer.cap[2].T +wholeHouseBuildingEnvelope.groundFloor_Building.Livingroom.inside_wall1a.Wall.simpleNLayer.cap[1].T +wholeHouseBuildingEnvelope.groundFloor_Building.Livingroom.inside_wall1a.Wall.simpleNLayer.cap[2].T +wholeHouseBuildingEnvelope.groundFloor_Building.Livingroom.inside_wall1b.Wall.simpleNLayer.cap[1].T +wholeHouseBuildingEnvelope.groundFloor_Building.Livingroom.inside_wall1b.Wall.simpleNLayer.cap[2].T +wholeHouseBuildingEnvelope.groundFloor_Building.Livingroom.inside_wall2.Wall.simpleNLayer.cap[1].T +wholeHouseBuildingEnvelope.groundFloor_Building.Livingroom.inside_wall2.Wall.simpleNLayer.cap[2].T +wholeHouseBuildingEnvelope.groundFloor_Building.Livingroom.outside_wall1.Wall.simpleNLayer.cap[1].T +wholeHouseBuildingEnvelope.groundFloor_Building.Livingroom.outside_wall1.Wall.simpleNLayer.cap[2].T +wholeHouseBuildingEnvelope.groundFloor_Building.Livingroom.outside_wall1.Wall.simpleNLayer.cap[3].T +wholeHouseBuildingEnvelope.groundFloor_Building.Livingroom.outside_wall1.Wall.simpleNLayer.cap[4].T +wholeHouseBuildingEnvelope.groundFloor_Building.Livingroom.outside_wall2.Wall.simpleNLayer.cap[1].T +wholeHouseBuildingEnvelope.groundFloor_Building.Livingroom.outside_wall2.Wall.simpleNLayer.cap[2].T +wholeHouseBuildingEnvelope.groundFloor_Building.Livingroom.outside_wall2.Wall.simpleNLayer.cap[3].T +wholeHouseBuildingEnvelope.groundFloor_Building.Livingroom.outside_wall2.Wall.simpleNLayer.cap[4].T +wholeHouseBuildingEnvelope.groundFloor_Building.WC_Storage.Ceiling.Wall.simpleNLayer.cap[1].T +wholeHouseBuildingEnvelope.groundFloor_Building.WC_Storage.Ceiling.Wall.simpleNLayer.cap[2].T +wholeHouseBuildingEnvelope.groundFloor_Building.WC_Storage.Ceiling.Wall.simpleNLayer.cap[3].T +wholeHouseBuildingEnvelope.groundFloor_Building.WC_Storage.floor.Wall.simpleNLayer.cap[1].T +wholeHouseBuildingEnvelope.groundFloor_Building.WC_Storage.floor.Wall.simpleNLayer.cap[2].T +wholeHouseBuildingEnvelope.groundFloor_Building.WC_Storage.inside_wall1.Wall.simpleNLayer.cap[1].T +wholeHouseBuildingEnvelope.groundFloor_Building.WC_Storage.inside_wall1.Wall.simpleNLayer.cap[2].T +wholeHouseBuildingEnvelope.groundFloor_Building.WC_Storage.inside_wall2.Wall.simpleNLayer.cap[1].T +wholeHouseBuildingEnvelope.groundFloor_Building.WC_Storage.inside_wall2.Wall.simpleNLayer.cap[2].T +wholeHouseBuildingEnvelope.groundFloor_Building.WC_Storage.outside_wall1.Wall.simpleNLayer.cap[1].T +wholeHouseBuildingEnvelope.groundFloor_Building.WC_Storage.outside_wall1.Wall.simpleNLayer.cap[2].T +wholeHouseBuildingEnvelope.groundFloor_Building.WC_Storage.outside_wall1.Wall.simpleNLayer.cap[3].T +wholeHouseBuildingEnvelope.groundFloor_Building.WC_Storage.outside_wall1.Wall.simpleNLayer.cap[4].T +wholeHouseBuildingEnvelope.groundFloor_Building.WC_Storage.outside_wall2.Wall.simpleNLayer.cap[1].T +wholeHouseBuildingEnvelope.groundFloor_Building.WC_Storage.outside_wall2.Wall.simpleNLayer.cap[2].T +wholeHouseBuildingEnvelope.groundFloor_Building.WC_Storage.outside_wall2.Wall.simpleNLayer.cap[3].T +wholeHouseBuildingEnvelope.groundFloor_Building.WC_Storage.outside_wall2.Wall.simpleNLayer.cap[4].T +wholeHouseBuildingEnvelope.upperFloor_Building.Bath.Ceiling.Wall.simpleNLayer.cap[1].T +wholeHouseBuildingEnvelope.upperFloor_Building.Bath.Ceiling.Wall.simpleNLayer.cap[2].T +wholeHouseBuildingEnvelope.upperFloor_Building.Bath.Ceiling.Wall.simpleNLayer.cap[3].T +wholeHouseBuildingEnvelope.upperFloor_Building.Bath.floor.Wall.simpleNLayer.cap[1].T +wholeHouseBuildingEnvelope.upperFloor_Building.Bath.floor.Wall.simpleNLayer.cap[2].T +wholeHouseBuildingEnvelope.upperFloor_Building.Bath.inside_wall1.Wall.simpleNLayer.cap[1].T +wholeHouseBuildingEnvelope.upperFloor_Building.Bath.inside_wall1.Wall.simpleNLayer.cap[2].T +wholeHouseBuildingEnvelope.upperFloor_Building.Bath.inside_wall2.Wall.simpleNLayer.cap[1].T +wholeHouseBuildingEnvelope.upperFloor_Building.Bath.inside_wall2.Wall.simpleNLayer.cap[2].T +wholeHouseBuildingEnvelope.upperFloor_Building.Bath.outside_wall1.Wall.simpleNLayer.cap[1].T +wholeHouseBuildingEnvelope.upperFloor_Building.Bath.outside_wall1.Wall.simpleNLayer.cap[2].T +wholeHouseBuildingEnvelope.upperFloor_Building.Bath.outside_wall1.Wall.simpleNLayer.cap[3].T +wholeHouseBuildingEnvelope.upperFloor_Building.Bath.outside_wall1.Wall.simpleNLayer.cap[4].T +wholeHouseBuildingEnvelope.upperFloor_Building.Bath.outside_wall2.Wall.simpleNLayer.cap[1].T +wholeHouseBuildingEnvelope.upperFloor_Building.Bath.outside_wall2.Wall.simpleNLayer.cap[2].T +wholeHouseBuildingEnvelope.upperFloor_Building.Bath.outside_wall2.Wall.simpleNLayer.cap[3].T +wholeHouseBuildingEnvelope.upperFloor_Building.Bath.outside_wall2.Wall.simpleNLayer.cap[4].T +wholeHouseBuildingEnvelope.upperFloor_Building.Bath.roof.Wall.simpleNLayer.cap[1].T +wholeHouseBuildingEnvelope.upperFloor_Building.Bath.roof.Wall.simpleNLayer.cap[2].T +wholeHouseBuildingEnvelope.upperFloor_Building.Bath.roof.Wall.simpleNLayer.cap[3].T +wholeHouseBuildingEnvelope.upperFloor_Building.Bedroom.Ceiling.Wall.simpleNLayer.cap[1].T +wholeHouseBuildingEnvelope.upperFloor_Building.Bedroom.Ceiling.Wall.simpleNLayer.cap[2].T +wholeHouseBuildingEnvelope.upperFloor_Building.Bedroom.Ceiling.Wall.simpleNLayer.cap[3].T +wholeHouseBuildingEnvelope.upperFloor_Building.Bedroom.floor.Wall.simpleNLayer.cap[1].T +wholeHouseBuildingEnvelope.upperFloor_Building.Bedroom.floor.Wall.simpleNLayer.cap[2].T +wholeHouseBuildingEnvelope.upperFloor_Building.Bedroom.inside_wall1a.Wall.simpleNLayer.cap[1].T +wholeHouseBuildingEnvelope.upperFloor_Building.Bedroom.inside_wall1a.Wall.simpleNLayer.cap[2].T +wholeHouseBuildingEnvelope.upperFloor_Building.Bedroom.inside_wall1b.Wall.simpleNLayer.cap[1].T +wholeHouseBuildingEnvelope.upperFloor_Building.Bedroom.inside_wall1b.Wall.simpleNLayer.cap[2].T +wholeHouseBuildingEnvelope.upperFloor_Building.Bedroom.inside_wall2.Wall.simpleNLayer.cap[1].T +wholeHouseBuildingEnvelope.upperFloor_Building.Bedroom.inside_wall2.Wall.simpleNLayer.cap[2].T +wholeHouseBuildingEnvelope.upperFloor_Building.Bedroom.outside_wall1.Wall.simpleNLayer.cap[1].T +wholeHouseBuildingEnvelope.upperFloor_Building.Bedroom.outside_wall1.Wall.simpleNLayer.cap[2].T +wholeHouseBuildingEnvelope.upperFloor_Building.Bedroom.outside_wall1.Wall.simpleNLayer.cap[3].T +wholeHouseBuildingEnvelope.upperFloor_Building.Bedroom.outside_wall1.Wall.simpleNLayer.cap[4].T +wholeHouseBuildingEnvelope.upperFloor_Building.Bedroom.outside_wall2.Wall.simpleNLayer.cap[1].T +wholeHouseBuildingEnvelope.upperFloor_Building.Bedroom.outside_wall2.Wall.simpleNLayer.cap[2].T +wholeHouseBuildingEnvelope.upperFloor_Building.Bedroom.outside_wall2.Wall.simpleNLayer.cap[3].T +wholeHouseBuildingEnvelope.upperFloor_Building.Bedroom.outside_wall2.Wall.simpleNLayer.cap[4].T +wholeHouseBuildingEnvelope.upperFloor_Building.Bedroom.roof.Wall.simpleNLayer.cap[1].T +wholeHouseBuildingEnvelope.upperFloor_Building.Bedroom.roof.Wall.simpleNLayer.cap[2].T +wholeHouseBuildingEnvelope.upperFloor_Building.Bedroom.roof.Wall.simpleNLayer.cap[3].T +wholeHouseBuildingEnvelope.upperFloor_Building.Children1.Ceiling.Wall.simpleNLayer.cap[1].T +wholeHouseBuildingEnvelope.upperFloor_Building.Children1.Ceiling.Wall.simpleNLayer.cap[2].T +wholeHouseBuildingEnvelope.upperFloor_Building.Children1.Ceiling.Wall.simpleNLayer.cap[3].T +wholeHouseBuildingEnvelope.upperFloor_Building.Children1.floor.Wall.simpleNLayer.cap[1].T +wholeHouseBuildingEnvelope.upperFloor_Building.Children1.floor.Wall.simpleNLayer.cap[2].T +wholeHouseBuildingEnvelope.upperFloor_Building.Children1.inside_wall1.Wall.simpleNLayer.cap[1].T +wholeHouseBuildingEnvelope.upperFloor_Building.Children1.inside_wall1.Wall.simpleNLayer.cap[2].T +wholeHouseBuildingEnvelope.upperFloor_Building.Children1.inside_wall2.Wall.simpleNLayer.cap[1].T +wholeHouseBuildingEnvelope.upperFloor_Building.Children1.inside_wall2.Wall.simpleNLayer.cap[2].T +wholeHouseBuildingEnvelope.upperFloor_Building.Children1.outside_wall1.Wall.simpleNLayer.cap[1].T +wholeHouseBuildingEnvelope.upperFloor_Building.Children1.outside_wall1.Wall.simpleNLayer.cap[2].T +wholeHouseBuildingEnvelope.upperFloor_Building.Children1.outside_wall1.Wall.simpleNLayer.cap[3].T +wholeHouseBuildingEnvelope.upperFloor_Building.Children1.outside_wall1.Wall.simpleNLayer.cap[4].T +wholeHouseBuildingEnvelope.upperFloor_Building.Children1.outside_wall2.Wall.simpleNLayer.cap[1].T +wholeHouseBuildingEnvelope.upperFloor_Building.Children1.outside_wall2.Wall.simpleNLayer.cap[2].T +wholeHouseBuildingEnvelope.upperFloor_Building.Children1.outside_wall2.Wall.simpleNLayer.cap[3].T +wholeHouseBuildingEnvelope.upperFloor_Building.Children1.outside_wall2.Wall.simpleNLayer.cap[4].T +wholeHouseBuildingEnvelope.upperFloor_Building.Children1.roof.Wall.simpleNLayer.cap[1].T +wholeHouseBuildingEnvelope.upperFloor_Building.Children1.roof.Wall.simpleNLayer.cap[2].T +wholeHouseBuildingEnvelope.upperFloor_Building.Children1.roof.Wall.simpleNLayer.cap[3].T +wholeHouseBuildingEnvelope.upperFloor_Building.Children2.Ceiling.Wall.simpleNLayer.cap[1].T +wholeHouseBuildingEnvelope.upperFloor_Building.Children2.Ceiling.Wall.simpleNLayer.cap[2].T +wholeHouseBuildingEnvelope.upperFloor_Building.Children2.Ceiling.Wall.simpleNLayer.cap[3].T +wholeHouseBuildingEnvelope.upperFloor_Building.Children2.floor.Wall.simpleNLayer.cap[1].T +wholeHouseBuildingEnvelope.upperFloor_Building.Children2.floor.Wall.simpleNLayer.cap[2].T +wholeHouseBuildingEnvelope.upperFloor_Building.Children2.inside_wall1a.Wall.simpleNLayer.cap[1].T +wholeHouseBuildingEnvelope.upperFloor_Building.Children2.inside_wall1a.Wall.simpleNLayer.cap[2].T +wholeHouseBuildingEnvelope.upperFloor_Building.Children2.inside_wall1b.Wall.simpleNLayer.cap[1].T +wholeHouseBuildingEnvelope.upperFloor_Building.Children2.inside_wall1b.Wall.simpleNLayer.cap[2].T +wholeHouseBuildingEnvelope.upperFloor_Building.Children2.inside_wall2.Wall.simpleNLayer.cap[1].T +wholeHouseBuildingEnvelope.upperFloor_Building.Children2.inside_wall2.Wall.simpleNLayer.cap[2].T +wholeHouseBuildingEnvelope.upperFloor_Building.Children2.outside_wall1.Wall.simpleNLayer.cap[1].T +wholeHouseBuildingEnvelope.upperFloor_Building.Children2.outside_wall1.Wall.simpleNLayer.cap[2].T +wholeHouseBuildingEnvelope.upperFloor_Building.Children2.outside_wall1.Wall.simpleNLayer.cap[3].T +wholeHouseBuildingEnvelope.upperFloor_Building.Children2.outside_wall1.Wall.simpleNLayer.cap[4].T +wholeHouseBuildingEnvelope.upperFloor_Building.Children2.outside_wall2.Wall.simpleNLayer.cap[1].T +wholeHouseBuildingEnvelope.upperFloor_Building.Children2.outside_wall2.Wall.simpleNLayer.cap[2].T +wholeHouseBuildingEnvelope.upperFloor_Building.Children2.outside_wall2.Wall.simpleNLayer.cap[3].T +wholeHouseBuildingEnvelope.upperFloor_Building.Children2.outside_wall2.Wall.simpleNLayer.cap[4].T +wholeHouseBuildingEnvelope.upperFloor_Building.Children2.roof.Wall.simpleNLayer.cap[1].T +wholeHouseBuildingEnvelope.upperFloor_Building.Children2.roof.Wall.simpleNLayer.cap[2].T +wholeHouseBuildingEnvelope.upperFloor_Building.Children2.roof.Wall.simpleNLayer.cap[3].T +wholeHouseBuildingEnvelope.upperFloor_Building.Corridor.Ceiling.Wall.simpleNLayer.cap[1].T +wholeHouseBuildingEnvelope.upperFloor_Building.Corridor.Ceiling.Wall.simpleNLayer.cap[2].T +wholeHouseBuildingEnvelope.upperFloor_Building.Corridor.Ceiling.Wall.simpleNLayer.cap[3].T +wholeHouseBuildingEnvelope.upperFloor_Building.Corridor.floor.Wall.simpleNLayer.cap[1].T +wholeHouseBuildingEnvelope.upperFloor_Building.Corridor.floor.Wall.simpleNLayer.cap[2].T +wholeHouseBuildingEnvelope.upperFloor_Building.Corridor.inner_wall1.Wall.simpleNLayer.cap[1].T +wholeHouseBuildingEnvelope.upperFloor_Building.Corridor.inner_wall1.Wall.simpleNLayer.cap[2].T +wholeHouseBuildingEnvelope.upperFloor_Building.Corridor.inside_wall2a.Wall.simpleNLayer.cap[1].T +wholeHouseBuildingEnvelope.upperFloor_Building.Corridor.inside_wall2a.Wall.simpleNLayer.cap[2].T +wholeHouseBuildingEnvelope.upperFloor_Building.Corridor.inside_wall2b.Wall.simpleNLayer.cap[1].T +wholeHouseBuildingEnvelope.upperFloor_Building.Corridor.inside_wall2b.Wall.simpleNLayer.cap[2].T +wholeHouseBuildingEnvelope.upperFloor_Building.Corridor.inside_wall3.Wall.simpleNLayer.cap[1].T +wholeHouseBuildingEnvelope.upperFloor_Building.Corridor.inside_wall3.Wall.simpleNLayer.cap[2].T +wholeHouseBuildingEnvelope.upperFloor_Building.Corridor.outside_wall1.Wall.simpleNLayer.cap[1].T +wholeHouseBuildingEnvelope.upperFloor_Building.Corridor.outside_wall1.Wall.simpleNLayer.cap[2].T +wholeHouseBuildingEnvelope.upperFloor_Building.Corridor.outside_wall1.Wall.simpleNLayer.cap[3].T +wholeHouseBuildingEnvelope.upperFloor_Building.Corridor.outside_wall1.Wall.simpleNLayer.cap[4].T +wholeHouseBuildingEnvelope.upperFloor_Building.Corridor.roof.Wall.simpleNLayer.cap[1].T +wholeHouseBuildingEnvelope.upperFloor_Building.Corridor.roof.Wall.simpleNLayer.cap[2].T +wholeHouseBuildingEnvelope.upperFloor_Building.Corridor.roof.Wall.simpleNLayer.cap[3].T +Dynamically selected continuous time states +There are 10 sets of dynamic state selection. +From set 1 there are 2 states to be selected from: +wholeHouseBuildingEnvelope.upperFloor_Building.Children2.airload.dynBal.m +wholeHouseBuildingEnvelope.upperFloor_Building.Children2.airload.dynBal.medium.Xi[] +wholeHouseBuildingEnvelope.upperFloor_Building.Children2.airload.dynBal.U +wholeHouseBuildingEnvelope.upperFloor_Building.portVent_in[5].h_outflow +From set 2 there are 2 states to be selected from: +wholeHouseBuildingEnvelope.groundFloor_Building.Livingroom.airload.dynBal.m +wholeHouseBuildingEnvelope.groundFloor_Building.Livingroom.airload.dynBal.medium.Xi[] +wholeHouseBuildingEnvelope.groundFloor_Building.Livingroom.airload.dynBal.U +wholeHouseBuildingEnvelope.groundFloor_Building.portVent_in[1].h_outflow +From set 3 there are 2 states to be selected from: +wholeHouseBuildingEnvelope.groundFloor_Building.Hobby.airload.dynBal.m +wholeHouseBuildingEnvelope.groundFloor_Building.Hobby.airload.dynBal.medium.Xi[] +wholeHouseBuildingEnvelope.groundFloor_Building.Hobby.airload.dynBal.U +wholeHouseBuildingEnvelope.groundFloor_Building.portVent_in[2].h_outflow +From set 4 there are 2 states to be selected from: +wholeHouseBuildingEnvelope.groundFloor_Building.Corridor.airload.dynBal.m +wholeHouseBuildingEnvelope.groundFloor_Building.Corridor.airload.dynBal.medium.Xi[] +wholeHouseBuildingEnvelope.groundFloor_Building.Corridor.airload.dynBal.U +wholeHouseBuildingEnvelope.groundFloor_Building.portVent_in[3].h_outflow +From set 5 there are 2 states to be selected from: +wholeHouseBuildingEnvelope.groundFloor_Building.portVent_in[4].h_outflow +wholeHouseBuildingEnvelope.groundFloor_Building.WC_Storage.airload.dynBal.m +wholeHouseBuildingEnvelope.groundFloor_Building.WC_Storage.airload.dynBal.medium.Xi[] +wholeHouseBuildingEnvelope.groundFloor_Building.WC_Storage.airload.dynBal.U +From set 6 there are 2 states to be selected from: +wholeHouseBuildingEnvelope.groundFloor_Building.Kitchen.airload.dynBal.m +wholeHouseBuildingEnvelope.groundFloor_Building.Kitchen.airload.dynBal.medium.Xi[] +wholeHouseBuildingEnvelope.groundFloor_Building.Kitchen.airload.dynBal.U +wholeHouseBuildingEnvelope.groundFloor_Building.portVent_in[5].h_outflow +From set 7 there are 2 states to be selected from: +wholeHouseBuildingEnvelope.upperFloor_Building.Bedroom.airload.dynBal.m +wholeHouseBuildingEnvelope.upperFloor_Building.Bedroom.airload.dynBal.medium.Xi[] +wholeHouseBuildingEnvelope.upperFloor_Building.Bedroom.airload.dynBal.U +wholeHouseBuildingEnvelope.upperFloor_Building.portVent_in[1].h_outflow +From set 8 there are 2 states to be selected from: +wholeHouseBuildingEnvelope.upperFloor_Building.Children1.airload.dynBal.m +wholeHouseBuildingEnvelope.upperFloor_Building.Children1.airload.dynBal.medium.Xi[] +wholeHouseBuildingEnvelope.upperFloor_Building.Children1.airload.dynBal.U +wholeHouseBuildingEnvelope.upperFloor_Building.portVent_in[2].h_outflow +From set 9 there are 2 states to be selected from: +wholeHouseBuildingEnvelope.upperFloor_Building.Corridor.airload.dynBal.m +wholeHouseBuildingEnvelope.upperFloor_Building.Corridor.airload.dynBal.medium.Xi[] +wholeHouseBuildingEnvelope.upperFloor_Building.Corridor.airload.dynBal.U +wholeHouseBuildingEnvelope.upperFloor_Building.portVent_in[3].h_outflow +From set 10 there are 2 states to be selected from: +wholeHouseBuildingEnvelope.upperFloor_Building.Bath.airload.dynBal.m +wholeHouseBuildingEnvelope.upperFloor_Building.Bath.airload.dynBal.medium.Xi[] +wholeHouseBuildingEnvelope.upperFloor_Building.Bath.airload.dynBal.U +wholeHouseBuildingEnvelope.upperFloor_Building.portVent_in[4].h_outflow +Finished +Warning: WARNINGS have been issued. +Finished + = true + +Declaring variable: Boolean rScript ; + +savelog("AixLib.ThermalZones.HighOrder.Examples.OFDHeatLoad.translation.log"); = true + + +rCheck = checkModel("AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case280"); +Check of AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case280 +The model has the same number of unknowns and equations: 1585 +The model has the same number of unknowns and equations +for the given numerical settings of parameters: 1585 +Check of AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case280 successful. +Declaring variable: Boolean rCheck ; + +Modelica.Utilities.Streams.print(" { \"file\" : \"AixLib/Resources/Scripts/Dymola/ThermalZones/HighOrder/Validation/ASHRAE140/Case280.mos\",", "AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case280.statistics.log"); +Modelica.Utilities.Streams.print(" \"model\" : \"AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case280\",", "AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case280.statistics.log"); +Modelica.Utilities.Streams.print(" \"check\" : {", "AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case280.statistics.log"); +Modelica.Utilities.Streams.print(" \"command\" : \"checkModel(\\\"AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case280\\\");\",", "AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case280.statistics.log"); +Modelica.Utilities.Streams.print(" \"result\" : " + String(rCheck), "AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case280.statistics.log"); +Modelica.Utilities.Streams.print(" },", "AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case280.statistics.log"); + + +rScript=RunScript("modelica://AixLib/Resources/Scripts/Dymola/ThermalZones/HighOrder/Validation/ASHRAE140/Case280.mos"); +simulateModel("AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case280", startTime=0, stopTime=31539600, outputInterval=1800, tolerance=1e-6, method="dassl", resultFile="AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case280"); +Translation of AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case280 +The DAE has 1585 scalar unknowns and 1585 scalar equations. + +Statistics + +Original Model + Number of components: 352 + Variables: 3082 + Constants: 41 (276 scalars) + Parameters: 1493 (2159 scalars) + Unknowns: 1548 (1585 scalars) + Differentiated variables: 25 scalars + Equations: 1257 + Nontrivial: 1045 +Translated Model + Constants: 780 scalars + Free parameters: 876 scalars + Parameter depending: 909 scalars + Outputs: 5 scalars + Continuous time states: 25 scalars + Time-varying variables: 474 scalars + Alias variables: 981 scalars + Number of mixed real/discrete systems of equations: 0 + Sizes of linear systems of equations: {4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 3, 4, 4, 4, 4} + Sizes after manipulation of the linear systems: {0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0} + Sizes of nonlinear systems of equations: {55} + Sizes after manipulation of the nonlinear systems: {13} + Number of numerical Jacobians: 0 + +Selected continuous time states +Statically selected continuous time states +idealHeaterCooler.pITempCool.PI.I.y +idealHeaterCooler.pITempHeat.PI.I.y +integrator2.y +integratorCool.y +integratorHeat.y +Room.airload.dynBal.m +Room.airload.dynBal.medium.Xi[1] +Room.airload.dynBal.U +Room.ceiling.Wall.simpleNLayer.cap[1].T +Room.ceiling.Wall.simpleNLayer.cap[2].T +Room.ceiling.Wall.simpleNLayer.cap[3].T +Room.floor.Wall.simpleNLayer.cap[1].T +Room.floor.Wall.simpleNLayer.cap[2].T +Room.wallEast.Wall.simpleNLayer.cap[1].T +Room.wallEast.Wall.simpleNLayer.cap[2].T +Room.wallEast.Wall.simpleNLayer.cap[3].T +Room.wallNorth.Wall.simpleNLayer.cap[1].T +Room.wallNorth.Wall.simpleNLayer.cap[2].T +Room.wallNorth.Wall.simpleNLayer.cap[3].T +Room.wallSouth.Wall.simpleNLayer.cap[1].T +Room.wallSouth.Wall.simpleNLayer.cap[2].T +Room.wallSouth.Wall.simpleNLayer.cap[3].T +Room.wallWest.Wall.simpleNLayer.cap[1].T +Room.wallWest.Wall.simpleNLayer.cap[2].T +Room.wallWest.Wall.simpleNLayer.cap[3].T +Finished +Finished + = true + +Declaring variable: Boolean rScript ; + +savelog("AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case280.translation.log"); = true + + +rCheck = checkModel("AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case230"); +Check of AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case230 +The model has the same number of unknowns and equations: 1568 +The model has the same number of unknowns and equations +for the given numerical settings of parameters: 1568 +Check of AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case230 successful. +Declaring variable: Boolean rCheck ; + +Modelica.Utilities.Streams.print(" { \"file\" : \"AixLib/Resources/Scripts/Dymola/ThermalZones/HighOrder/Validation/ASHRAE140/Case230.mos\",", "AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case230.statistics.log"); +Modelica.Utilities.Streams.print(" \"model\" : \"AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case230\",", "AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case230.statistics.log"); +Modelica.Utilities.Streams.print(" \"check\" : {", "AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case230.statistics.log"); +Modelica.Utilities.Streams.print(" \"command\" : \"checkModel(\\\"AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case230\\\");\",", "AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case230.statistics.log"); +Modelica.Utilities.Streams.print(" \"result\" : " + String(rCheck), "AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case230.statistics.log"); +Modelica.Utilities.Streams.print(" },", "AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case230.statistics.log"); + + +rScript=RunScript("modelica://AixLib/Resources/Scripts/Dymola/ThermalZones/HighOrder/Validation/ASHRAE140/Case230.mos"); +simulateModel("AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case230", startTime=0, stopTime=31539600, outputInterval=1800, tolerance=1e-6, method="dassl", resultFile="AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case230"); +Translation of AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case230 +The DAE has 1568 scalar unknowns and 1568 scalar equations. + +Statistics + +Original Model + Number of components: 349 + Variables: 3047 + Constants: 41 (276 scalars) + Parameters: 1474 (2065 scalars) + Unknowns: 1532 (1568 scalars) + Differentiated variables: 25 scalars + Equations: 1252 + Nontrivial: 1041 +Translated Model + Constants: 771 scalars + Free parameters: 794 scalars + Parameter depending: 906 scalars + Outputs: 5 scalars + Continuous time states: 25 scalars + Time-varying variables: 461 scalars + Alias variables: 977 scalars + Number of mixed real/discrete systems of equations: 0 + Sizes of linear systems of equations: {4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 3, 4, 4, 4, 4} + Sizes after manipulation of the linear systems: {0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0} + Sizes of nonlinear systems of equations: {55} + Sizes after manipulation of the nonlinear systems: {13} + Number of numerical Jacobians: 0 + +Selected continuous time states +Statically selected continuous time states +idealHeaterCooler.pITempCool.PI.I.y +idealHeaterCooler.pITempHeat.PI.I.y +integrator2.y +integratorCool.y +integratorHeat.y +Room.airload.dynBal.m +Room.airload.dynBal.medium.Xi[1] +Room.airload.dynBal.U +Room.ceiling.Wall.simpleNLayer.cap[1].T +Room.ceiling.Wall.simpleNLayer.cap[2].T +Room.ceiling.Wall.simpleNLayer.cap[3].T +Room.floor.Wall.simpleNLayer.cap[1].T +Room.floor.Wall.simpleNLayer.cap[2].T +Room.wallEast.Wall.simpleNLayer.cap[1].T +Room.wallEast.Wall.simpleNLayer.cap[2].T +Room.wallEast.Wall.simpleNLayer.cap[3].T +Room.wallNorth.Wall.simpleNLayer.cap[1].T +Room.wallNorth.Wall.simpleNLayer.cap[2].T +Room.wallNorth.Wall.simpleNLayer.cap[3].T +Room.wallSouth.Wall.simpleNLayer.cap[1].T +Room.wallSouth.Wall.simpleNLayer.cap[2].T +Room.wallSouth.Wall.simpleNLayer.cap[3].T +Room.wallWest.Wall.simpleNLayer.cap[1].T +Room.wallWest.Wall.simpleNLayer.cap[2].T +Room.wallWest.Wall.simpleNLayer.cap[3].T +Finished +Finished + = true + +Declaring variable: Boolean rScript ; + +savelog("AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case230.translation.log"); = true + + +rCheck = checkModel("AixLib.ThermalZones.ReducedOrder.Examples.MultizoneMoistAirCO2"); +Warning: Can not resolve link "AixLib.ThermalZones.ReducedOrder.Multizone.MultizoneMoistAirEquipped" in AixLib.ThermalZones.ReducedOrder.Examples.MultizoneMoistAirCO2 +Check of AixLib.ThermalZones.ReducedOrder.Examples.MultizoneMoistAirCO2 +The model has the same number of unknowns and equations: 10232 +The model has the same number of unknowns and equations +for the given numerical settings of parameters: 10232 +Check of AixLib.ThermalZones.ReducedOrder.Examples.MultizoneMoistAirCO2 successful. +Declaring variable: Boolean rCheck ; + +Modelica.Utilities.Streams.print(" { \"file\" : \"AixLib/Resources/Scripts/Dymola/ThermalZones/ReducedOrder/Examples/MultizoneMoistAirCO2.mos\",", "AixLib.ThermalZones.ReducedOrder.Examples.MultizoneMoistAirCO2.statistics.log"); +Modelica.Utilities.Streams.print(" \"model\" : \"AixLib.ThermalZones.ReducedOrder.Examples.MultizoneMoistAirCO2\",", "AixLib.ThermalZones.ReducedOrder.Examples.MultizoneMoistAirCO2.statistics.log"); +Modelica.Utilities.Streams.print(" \"check\" : {", "AixLib.ThermalZones.ReducedOrder.Examples.MultizoneMoistAirCO2.statistics.log"); +Modelica.Utilities.Streams.print(" \"command\" : \"checkModel(\\\"AixLib.ThermalZones.ReducedOrder.Examples.MultizoneMoistAirCO2\\\");\",", "AixLib.ThermalZones.ReducedOrder.Examples.MultizoneMoistAirCO2.statistics.log"); +Modelica.Utilities.Streams.print(" \"result\" : " + String(rCheck), "AixLib.ThermalZones.ReducedOrder.Examples.MultizoneMoistAirCO2.statistics.log"); +Modelica.Utilities.Streams.print(" },", "AixLib.ThermalZones.ReducedOrder.Examples.MultizoneMoistAirCO2.statistics.log"); + + +rScript=RunScript("modelica://AixLib/Resources/Scripts/Dymola/ThermalZones/ReducedOrder/Examples/MultizoneMoistAirCO2.mos"); +simulateModel("AixLib.ThermalZones.ReducedOrder.Examples.MultizoneMoistAirCO2", tolerance=1e-6, stopTime=3.1536e+007, numberOfIntervals=0, outputInterval=3600, method="CVode", resultFile="AixLib.ThermalZones.ReducedOrder.Examples.MultizoneMoistAirCO2"); +Translation of AixLib.ThermalZones.ReducedOrder.Examples.MultizoneMoistAirCO2 +The DAE has 10232 scalar unknowns and 10232 scalar equations. + +Statistics + +Original Model + Number of components: 1537 + Variables: 14814 + Constants: 411 (411 scalars) + Parameters: 4813 (5892 scalars) + Unknowns: 9590 (10232 scalars) + Differentiated variables: 45 scalars + Equations: 6533 + Nontrivial: 6027 +Translated Model + Constants: 3030 scalars + Free parameters: 1342 scalars + Parameter depending: 2740 scalars + Outputs: 23 scalars + Continuous time states: 45 scalars + Time-varying variables: 3050 scalars + Alias variables: 6373 scalars + Number of mixed real/discrete systems of equations: 0 + Sizes of linear systems of equations: {29, 4, 29, 4, 29, 4, 29, 4, 29, 4} + Sizes after manipulation of the linear systems: {4, 0, 4, 0, 4, 0, 4, 0, 4, 0} + Sizes of nonlinear systems of equations: {1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1} + Sizes after manipulation of the nonlinear systems: {0, 1, 0, 1, 0, 1, 0, 1, 0, 1, 0, 1, 0, 1, 0, 1, 0, 1, 0, 1, 0, 1, 0, 1, 0, 1, 0, 1, 0, 1} + Number of numerical Jacobians: 0 + Initialization problem + Sizes of linear systems of equations: {32, 32, 32, 32, 32} + Sizes after manipulation of the linear systems: {5, 5, 5, 5, 5} + +Selected continuous time states +Statically selected continuous time states +multizone.zone[1].heaterCooler.pITempHeat.PI.I.y +multizone.zone[1].ROM.extWallRC.thermCapExt[1].T +multizone.zone[1].ROM.intWallRC.thermCapInt[1].T +multizone.zone[1].ROM.volMoiAir.dynBal.m +multizone.zone[1].ROM.volMoiAir.dynBal.mC[1] +multizone.zone[1].ROM.volMoiAir.dynBal.medium.Xi[1] +multizone.zone[1].ROM.volMoiAir.dynBal.U +multizone.zone[1].ventCont.dEMA.ExpAVG.x[1] +multizone.zone[1].ventCont.dEMA.ExpAVG1.x[1] +multizone.zone[2].heaterCooler.pITempHeat.PI.I.y +multizone.zone[2].ROM.extWallRC.thermCapExt[1].T +multizone.zone[2].ROM.intWallRC.thermCapInt[1].T +multizone.zone[2].ROM.volMoiAir.dynBal.m +multizone.zone[2].ROM.volMoiAir.dynBal.mC[1] +multizone.zone[2].ROM.volMoiAir.dynBal.medium.Xi[1] +multizone.zone[2].ROM.volMoiAir.dynBal.U +multizone.zone[2].ventCont.dEMA.ExpAVG.x[1] +multizone.zone[2].ventCont.dEMA.ExpAVG1.x[1] +multizone.zone[3].heaterCooler.pITempHeat.PI.I.y +multizone.zone[3].ROM.extWallRC.thermCapExt[1].T +multizone.zone[3].ROM.intWallRC.thermCapInt[1].T +multizone.zone[3].ROM.volMoiAir.dynBal.m +multizone.zone[3].ROM.volMoiAir.dynBal.mC[1] +multizone.zone[3].ROM.volMoiAir.dynBal.medium.Xi[1] +multizone.zone[3].ROM.volMoiAir.dynBal.U +multizone.zone[3].ventCont.dEMA.ExpAVG.x[1] +multizone.zone[3].ventCont.dEMA.ExpAVG1.x[1] +multizone.zone[4].heaterCooler.pITempHeat.PI.I.y +multizone.zone[4].ROM.extWallRC.thermCapExt[1].T +multizone.zone[4].ROM.intWallRC.thermCapInt[1].T +multizone.zone[4].ROM.volMoiAir.dynBal.m +multizone.zone[4].ROM.volMoiAir.dynBal.mC[1] +multizone.zone[4].ROM.volMoiAir.dynBal.medium.Xi[1] +multizone.zone[4].ROM.volMoiAir.dynBal.U +multizone.zone[4].ventCont.dEMA.ExpAVG.x[1] +multizone.zone[4].ventCont.dEMA.ExpAVG1.x[1] +multizone.zone[5].heaterCooler.pITempHeat.PI.I.y +multizone.zone[5].ROM.extWallRC.thermCapExt[1].T +multizone.zone[5].ROM.intWallRC.thermCapInt[1].T +multizone.zone[5].ROM.volMoiAir.dynBal.m +multizone.zone[5].ROM.volMoiAir.dynBal.mC[1] +multizone.zone[5].ROM.volMoiAir.dynBal.medium.Xi[1] +multizone.zone[5].ROM.volMoiAir.dynBal.U +multizone.zone[5].ventCont.dEMA.ExpAVG.x[1] +multizone.zone[5].ventCont.dEMA.ExpAVG1.x[1] +Finished +Finished + = true + +Declaring variable: Boolean rScript ; + +savelog("AixLib.ThermalZones.ReducedOrder.Examples.MultizoneMoistAirCO2.translation.log"); = true + + +rCheck = checkModel("AixLib.ThermalZones.HighOrder.Validation.EmpiricalValidation.Warehouse"); +Check of AixLib.ThermalZones.HighOrder.Validation.EmpiricalValidation.Warehouse +The model has the same number of unknowns and equations: 1159 +The model has the same number of unknowns and equations +for the given numerical settings of parameters: 1159 +Check of AixLib.ThermalZones.HighOrder.Validation.EmpiricalValidation.Warehouse successful. +Declaring variable: Boolean rCheck ; + +Modelica.Utilities.Streams.print(" { \"file\" : \"AixLib/Resources/Scripts/Dymola/ThermalZones/HighOrder/Validation/EmpiricalValidation/Warehouse.mos\",", "AixLib.ThermalZones.HighOrder.Validation.EmpiricalValidation.Warehouse.statistics.log"); +Modelica.Utilities.Streams.print(" \"model\" : \"AixLib.ThermalZones.HighOrder.Validation.EmpiricalValidation.Warehouse\",", "AixLib.ThermalZones.HighOrder.Validation.EmpiricalValidation.Warehouse.statistics.log"); +Modelica.Utilities.Streams.print(" \"check\" : {", "AixLib.ThermalZones.HighOrder.Validation.EmpiricalValidation.Warehouse.statistics.log"); +Modelica.Utilities.Streams.print(" \"command\" : \"checkModel(\\\"AixLib.ThermalZones.HighOrder.Validation.EmpiricalValidation.Warehouse\\\");\",", "AixLib.ThermalZones.HighOrder.Validation.EmpiricalValidation.Warehouse.statistics.log"); +Modelica.Utilities.Streams.print(" \"result\" : " + String(rCheck), "AixLib.ThermalZones.HighOrder.Validation.EmpiricalValidation.Warehouse.statistics.log"); +Modelica.Utilities.Streams.print(" },", "AixLib.ThermalZones.HighOrder.Validation.EmpiricalValidation.Warehouse.statistics.log"); + + +rScript=RunScript("modelica://AixLib/Resources/Scripts/Dymola/ThermalZones/HighOrder/Validation/EmpiricalValidation/Warehouse.mos"); +simulateModel("AixLib.ThermalZones.HighOrder.Validation.EmpiricalValidation.Warehouse", startTime=0, stopTime=31536000, outputInterval=1800, tolerance=1e-6, method="dassl", resultFile="AixLib.ThermalZones.HighOrder.Validation.EmpiricalValidation.Warehouse"); +Translation of AixLib.ThermalZones.HighOrder.Validation.EmpiricalValidation.Warehouse +The DAE has 1159 scalar unknowns and 1159 scalar equations. + +Statistics + +Original Model + Number of components: 257 + Variables: 2361 + Constants: 12 (12 scalars) + Parameters: 1203 (1489 scalars) + Unknowns: 1146 (1159 scalars) + Differentiated variables: 25 scalars + Equations: 956 + Nontrivial: 846 +Translated Model + Constants: 453 scalars + Free parameters: 498 scalars + Parameter depending: 608 scalars + Outputs: 10 scalars + Continuous time states: 25 scalars + Time-varying variables: 332 scalars + Alias variables: 769 scalars + Number of mixed real/discrete systems of equations: 0 + Sizes of linear systems of equations: {4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4} + Sizes after manipulation of the linear systems: {0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0} + Sizes of nonlinear systems of equations: {36, 1, 1} + Sizes after manipulation of the nonlinear systems: {7, 0, 1} + Number of numerical Jacobians: 0 + +Selected continuous time states +Statically selected continuous time states +idealHeaterCooler.pITempCool.PI.I.y +idealHeaterCooler.pITempHeat.PI.I.y +integrator1.y +integrator2.y +room.airload.dynBal.m +room.airload.dynBal.medium.Xi[1] +room.airload.dynBal.U +room.ceiling.Wall.simpleNLayer.cap[1].T +room.ceiling.Wall.simpleNLayer.cap[2].T +room.ceiling.Wall.simpleNLayer.cap[3].T +room.floor.Wall.simpleNLayer.cap[1].T +room.floor.Wall.simpleNLayer.cap[2].T +room.interiorThermCap.T +room.wallEast.Wall.simpleNLayer.cap[1].T +room.wallEast.Wall.simpleNLayer.cap[2].T +room.wallEast.Wall.simpleNLayer.cap[3].T +room.wallNorth.Wall.simpleNLayer.cap[1].T +room.wallNorth.Wall.simpleNLayer.cap[2].T +room.wallNorth.Wall.simpleNLayer.cap[3].T +room.wallSouth.Wall.simpleNLayer.cap[1].T +room.wallSouth.Wall.simpleNLayer.cap[2].T +room.wallSouth.Wall.simpleNLayer.cap[3].T +room.wallWest.Wall.simpleNLayer.cap[1].T +room.wallWest.Wall.simpleNLayer.cap[2].T +room.wallWest.Wall.simpleNLayer.cap[3].T +Finished +Finished + = true + +Declaring variable: Boolean rScript ; + +savelog("AixLib.ThermalZones.HighOrder.Validation.EmpiricalValidation.Warehouse.translation.log"); = true + + +rCheck = checkModel("AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case250"); +Check of AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case250 +The model has the same number of unknowns and equations: 1568 +The model has the same number of unknowns and equations +for the given numerical settings of parameters: 1568 +Check of AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case250 successful. +Declaring variable: Boolean rCheck ; + +Modelica.Utilities.Streams.print(" { \"file\" : \"AixLib/Resources/Scripts/Dymola/ThermalZones/HighOrder/Validation/ASHRAE140/Case250.mos\",", "AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case250.statistics.log"); +Modelica.Utilities.Streams.print(" \"model\" : \"AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case250\",", "AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case250.statistics.log"); +Modelica.Utilities.Streams.print(" \"check\" : {", "AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case250.statistics.log"); +Modelica.Utilities.Streams.print(" \"command\" : \"checkModel(\\\"AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case250\\\");\",", "AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case250.statistics.log"); +Modelica.Utilities.Streams.print(" \"result\" : " + String(rCheck), "AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case250.statistics.log"); +Modelica.Utilities.Streams.print(" },", "AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case250.statistics.log"); + + +rScript=RunScript("modelica://AixLib/Resources/Scripts/Dymola/ThermalZones/HighOrder/Validation/ASHRAE140/Case250.mos"); +simulateModel("AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case250", startTime=0, stopTime=31539600, outputInterval=1800, tolerance=1e-6, method="dassl", resultFile="AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case250"); +Translation of AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case250 +The DAE has 1568 scalar unknowns and 1568 scalar equations. + +Statistics + +Original Model + Number of components: 349 + Variables: 3047 + Constants: 41 (276 scalars) + Parameters: 1474 (2065 scalars) + Unknowns: 1532 (1568 scalars) + Differentiated variables: 25 scalars + Equations: 1252 + Nontrivial: 1041 +Translated Model + Constants: 771 scalars + Free parameters: 794 scalars + Parameter depending: 906 scalars + Outputs: 5 scalars + Continuous time states: 25 scalars + Time-varying variables: 461 scalars + Alias variables: 977 scalars + Number of mixed real/discrete systems of equations: 0 + Sizes of linear systems of equations: {4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 3, 4, 4, 4, 4} + Sizes after manipulation of the linear systems: {0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0} + Sizes of nonlinear systems of equations: {55} + Sizes after manipulation of the nonlinear systems: {13} + Number of numerical Jacobians: 0 + +Selected continuous time states +Statically selected continuous time states +idealHeaterCooler.pITempCool.PI.I.y +idealHeaterCooler.pITempHeat.PI.I.y +integrator2.y +integratorCool.y +integratorHeat.y +Room.airload.dynBal.m +Room.airload.dynBal.medium.Xi[1] +Room.airload.dynBal.U +Room.ceiling.Wall.simpleNLayer.cap[1].T +Room.ceiling.Wall.simpleNLayer.cap[2].T +Room.ceiling.Wall.simpleNLayer.cap[3].T +Room.floor.Wall.simpleNLayer.cap[1].T +Room.floor.Wall.simpleNLayer.cap[2].T +Room.wallEast.Wall.simpleNLayer.cap[1].T +Room.wallEast.Wall.simpleNLayer.cap[2].T +Room.wallEast.Wall.simpleNLayer.cap[3].T +Room.wallNorth.Wall.simpleNLayer.cap[1].T +Room.wallNorth.Wall.simpleNLayer.cap[2].T +Room.wallNorth.Wall.simpleNLayer.cap[3].T +Room.wallSouth.Wall.simpleNLayer.cap[1].T +Room.wallSouth.Wall.simpleNLayer.cap[2].T +Room.wallSouth.Wall.simpleNLayer.cap[3].T +Room.wallWest.Wall.simpleNLayer.cap[1].T +Room.wallWest.Wall.simpleNLayer.cap[2].T +Room.wallWest.Wall.simpleNLayer.cap[3].T +Finished +Finished + = true + +Declaring variable: Boolean rScript ; + +savelog("AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case250.translation.log"); = true + + +rCheck = checkModel("AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case920"); +Check of AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case920 +Warning: Local "multiSum" conflict with inherited. Should be identical +Warning: Component multiSum(nu = 2), + but previously multiSum(nu = nWin). + The components are not identical. + + For element multiSum found at + + File: /tmp/tmp-AixLib-0-jodv2jcy/AixLib/ThermalZones/HighOrder/Rooms/ASHRAE140/EastWestFacingWindows.mo, line 82 + Conflict with element from + File: /tmp/tmp-AixLib-0-jodv2jcy/AixLib/ThermalZones/HighOrder/Rooms/BaseClasses/PartialRoomFourWalls.mo, line 211 + Context: AixLib.ThermalZones.HighOrder.Rooms.ASHRAE140.EastWestFacingWindows + File: /tmp/tmp-AixLib-0-jodv2jcy/AixLib/ThermalZones/HighOrder/Validation/ASHRAE140/Case620.mo, line 8 +Warning: Local "multiSum" conflict with inherited. Should be identical +Warning: Component multiSum(nu = 2), + but previously multiSum(nu = nWin). + The components are not identical. + + For element multiSum found at + + File: /tmp/tmp-AixLib-0-jodv2jcy/AixLib/ThermalZones/HighOrder/Rooms/ASHRAE140/EastWestFacingWindows.mo, line 82 + Conflict with element from + File: /tmp/tmp-AixLib-0-jodv2jcy/AixLib/ThermalZones/HighOrder/Rooms/BaseClasses/PartialRoomFourWalls.mo, line 211 + Context: AixLib.ThermalZones.HighOrder.Rooms.ASHRAE140.EastWestFacingWindows + File: /tmp/tmp-AixLib-0-jodv2jcy/AixLib/ThermalZones/HighOrder/Validation/ASHRAE140/Case620.mo, line 8 +The model has the same number of unknowns and equations: 1721 +The model has the same number of unknowns and equations +for the given numerical settings of parameters: 1721 +Check of AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case920 successful. +Declaring variable: Boolean rCheck ; + +Modelica.Utilities.Streams.print(" { \"file\" : \"AixLib/Resources/Scripts/Dymola/ThermalZones/HighOrder/Validation/ASHRAE140/Case920.mos\",", "AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case920.statistics.log"); +Modelica.Utilities.Streams.print(" \"model\" : \"AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case920\",", "AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case920.statistics.log"); +Modelica.Utilities.Streams.print(" \"check\" : {", "AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case920.statistics.log"); +Modelica.Utilities.Streams.print(" \"command\" : \"checkModel(\\\"AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case920\\\");\",", "AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case920.statistics.log"); +Modelica.Utilities.Streams.print(" \"result\" : " + String(rCheck), "AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case920.statistics.log"); +Modelica.Utilities.Streams.print(" },", "AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case920.statistics.log"); + + +rScript=RunScript("modelica://AixLib/Resources/Scripts/Dymola/ThermalZones/HighOrder/Validation/ASHRAE140/Case920.mos"); +simulateModel("AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case920", startTime=0, stopTime=31539600, outputInterval=1800, tolerance=1e-6, method="dassl", resultFile="AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case920"); +Translation of AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case920 +Warning: Local "multiSum" conflict with inherited. Should be identical +Warning: Component multiSum(nu = 2), + but previously multiSum(nu = nWin). + The components are not identical. + + For element multiSum found at + + File: /tmp/tmp-AixLib-0-jodv2jcy/AixLib/ThermalZones/HighOrder/Rooms/ASHRAE140/EastWestFacingWindows.mo, line 82 + Conflict with element from + File: /tmp/tmp-AixLib-0-jodv2jcy/AixLib/ThermalZones/HighOrder/Rooms/BaseClasses/PartialRoomFourWalls.mo, line 211 + Context: AixLib.ThermalZones.HighOrder.Rooms.ASHRAE140.EastWestFacingWindows + File: /tmp/tmp-AixLib-0-jodv2jcy/AixLib/ThermalZones/HighOrder/Validation/ASHRAE140/Case620.mo, line 8 +Warning: Local "multiSum" conflict with inherited. Should be identical +Warning: Component multiSum(nu = 2), + but previously multiSum(nu = nWin). + The components are not identical. + + For element multiSum found at + + File: /tmp/tmp-AixLib-0-jodv2jcy/AixLib/ThermalZones/HighOrder/Rooms/ASHRAE140/EastWestFacingWindows.mo, line 82 + Conflict with element from + File: /tmp/tmp-AixLib-0-jodv2jcy/AixLib/ThermalZones/HighOrder/Rooms/BaseClasses/PartialRoomFourWalls.mo, line 211 + Context: AixLib.ThermalZones.HighOrder.Rooms.ASHRAE140.EastWestFacingWindows + File: /tmp/tmp-AixLib-0-jodv2jcy/AixLib/ThermalZones/HighOrder/Validation/ASHRAE140/Case620.mo, line 8 +The DAE has 1721 scalar unknowns and 1721 scalar equations. + +Statistics + +Original Model + Number of components: 380 + Variables: 3302 + Constants: 41 (276 scalars) + Parameters: 1575 (2317 scalars) + Unknowns: 1686 (1721 scalars) + Differentiated variables: 25 scalars + Equations: 1333 + Nontrivial: 1107 +Translated Model + Constants: 803 scalars + Free parameters: 971 scalars + Parameter depending: 954 scalars + Outputs: 5 scalars + Continuous time states: 25 scalars + Time-varying variables: 513 scalars + Alias variables: 1073 scalars + Number of mixed real/discrete systems of equations: 0 + Sizes of linear systems of equations: {4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 3, 4, 4, 4, 4} + Sizes after manipulation of the linear systems: {0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0} + Sizes of nonlinear systems of equations: {73} + Sizes after manipulation of the nonlinear systems: {19} + Number of numerical Jacobians: 0 + +Selected continuous time states +Statically selected continuous time states +idealHeaterCooler.pITempCool.PI.I.y +idealHeaterCooler.pITempHeat.PI.I.y +integrator2.y +integratorCool.y +integratorHeat.y +Room.airload.dynBal.m +Room.airload.dynBal.medium.Xi[1] +Room.airload.dynBal.U +Room.ceiling.Wall.simpleNLayer.cap[1].T +Room.ceiling.Wall.simpleNLayer.cap[2].T +Room.ceiling.Wall.simpleNLayer.cap[3].T +Room.floor.Wall.simpleNLayer.cap[1].T +Room.floor.Wall.simpleNLayer.cap[2].T +Room.wallEast.Wall.simpleNLayer.cap[1].T +Room.wallEast.Wall.simpleNLayer.cap[2].T +Room.wallEast.Wall.simpleNLayer.cap[3].T +Room.wallNorth.Wall.simpleNLayer.cap[1].T +Room.wallNorth.Wall.simpleNLayer.cap[2].T +Room.wallNorth.Wall.simpleNLayer.cap[3].T +Room.wallSouth.Wall.simpleNLayer.cap[1].T +Room.wallSouth.Wall.simpleNLayer.cap[2].T +Room.wallSouth.Wall.simpleNLayer.cap[3].T +Room.wallWest.Wall.simpleNLayer.cap[1].T +Room.wallWest.Wall.simpleNLayer.cap[2].T +Room.wallWest.Wall.simpleNLayer.cap[3].T +Finished +Warning: WARNINGS have been issued. +Finished + = true + +Declaring variable: Boolean rScript ; + +savelog("AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case920.translation.log"); = true + + +rCheck = checkModel("AixLib.ThermalZones.ReducedOrder.Examples.ThermalZoneMoistCO2AirExchange"); +Warning: Can not resolve link "AixLib.ThermalZones.ReducedOrder.ThermalZone.ThermalZoneMoistAirEquipped" in AixLib.ThermalZones.ReducedOrder.Examples.ThermalZoneMoistCO2AirExchange +Check of AixLib.ThermalZones.ReducedOrder.Examples.ThermalZoneMoistCO2AirExchange +The model has the same number of unknowns and equations: 2112 +The model could not be deduced to be symbolically well-posed. +The model has + 1946+29*thermalZone.zoneParam.nOrientations+3*thermalZone.ROM.volMoiAir.dynBal.nPorts +thermalZone.humanTotHeaDependent.productHeatOutput.nu+thermalZone.humanTotHeaDependent.productMoistureOutput.nu +thermalZone.machinesSenHea.productHeatOutput.nu+thermalZone.lights.productHeatOutput.nu +thermalZone.ventCont.optimalTemp.nin+thermalZone.ventCont.optimalTemp.nout+ thermalZone.ventCont.dEMA.nout+thermalZone.ventCont.dEMA.ExpAVG.n+ thermalZone.ventCont.dEMA.ExpAVG1.n+thermalZone.SumQLat2_flow.nu+max([size( internalGains.columns, 1); size(internalGains.offset, 1)]) +scalar unknowns and + 2004+(if weaDat.pAtmSou == AixLib.BoundaryConditions.Types.DataSource.Parameter then 1 else 0)+(if weaDat.TDewPoiSou == AixLib.BoundaryConditions.Types.DataSource. Parameter then 1 else 0)+(if weaDat.TDryBulSou == AixLib.BoundaryConditions.Types.DataSource. Parameter then 1 else 0)+(if weaDat.TBlaSkySou == AixLib.BoundaryConditions.Types.DataSource. Parameter then 1 else 0)+(if weaDat.relHumSou == AixLib.BoundaryConditions.Types.DataSource. Parameter then 1 else 0)+(if weaDat.opaSkyCovSou == AixLib.BoundaryConditions.Types.DataSource. Parameter then 1 else 0)+(if weaDat.ceiHeiSou == AixLib.BoundaryConditions.Types.DataSource. Parameter then 1 else 0)+(if weaDat.totSkyCovSou == AixLib.BoundaryConditions.Types.DataSource. Parameter then 1 else 0)+(if weaDat.winSpeSou == AixLib.BoundaryConditions.Types.DataSource. Parameter then 1 else 0)+(if weaDat.winDirSou == AixLib.BoundaryConditions.Types.DataSource. Parameter then 1 else 0)+(if weaDat.HInfHorSou == AixLib.BoundaryConditions.Types.DataSource. Parameter then 1 else 0)+(if weaDat.HSou == AixLib.BoundaryConditions.Types.RadiationDataSource. Input_HDirNor_HDifHor then 2 else 1)+(if weaDat.HSou == AixLib.BoundaryConditions.Types.RadiationDataSource. Input_HDirNor_HGloHor then 2 else 1)+(if weaDat.HSou == AixLib.BoundaryConditions.Types.RadiationDataSource. Input_HGloHor_HDifHor then 2 else 1)+max([size(internalGains.columns, 1); size (internalGains.offset, 1)])+(if not humRat.use_p_in then 1 else 0)+19* thermalZone.zoneParam.nOrientations+(if not thermalZone.eqAirTempWall.TGroundFromInput then 1 else 0)+thermalZone.ventCont.optimalTemp.nout+thermalZone.ventCont.dEMA.ExpAVG.n +thermalZone.ventCont.dEMA.ExpAVG1.n+(if not thermalZone.x_pTphi.use_p_in then 1 else 0)+(if not thermalZone.use_C_flow then 1 else 0)+7* thermalZone.ROM.volMoiAir.dynBal.nPorts +scalar equations. +However, exploiting the given numerical settings of parameters gives the same number of unknowns and equations: + 2112 +Check of AixLib.ThermalZones.ReducedOrder.Examples.ThermalZoneMoistCO2AirExchange successful. +Declaring variable: Boolean rCheck ; + +Modelica.Utilities.Streams.print(" { \"file\" : \"AixLib/Resources/Scripts/Dymola/ThermalZones/ReducedOrder/Examples/ThermalZoneMoistCO2AirExchange.mos\",", "AixLib.ThermalZones.ReducedOrder.Examples.ThermalZoneMoistCO2AirExchange.statistics.log"); +Modelica.Utilities.Streams.print(" \"model\" : \"AixLib.ThermalZones.ReducedOrder.Examples.ThermalZoneMoistCO2AirExchange\",", "AixLib.ThermalZones.ReducedOrder.Examples.ThermalZoneMoistCO2AirExchange.statistics.log"); +Modelica.Utilities.Streams.print(" \"check\" : {", "AixLib.ThermalZones.ReducedOrder.Examples.ThermalZoneMoistCO2AirExchange.statistics.log"); +Modelica.Utilities.Streams.print(" \"command\" : \"checkModel(\\\"AixLib.ThermalZones.ReducedOrder.Examples.ThermalZoneMoistCO2AirExchange\\\");\",", "AixLib.ThermalZones.ReducedOrder.Examples.ThermalZoneMoistCO2AirExchange.statistics.log"); +Modelica.Utilities.Streams.print(" \"result\" : " + String(rCheck), "AixLib.ThermalZones.ReducedOrder.Examples.ThermalZoneMoistCO2AirExchange.statistics.log"); +Modelica.Utilities.Streams.print(" },", "AixLib.ThermalZones.ReducedOrder.Examples.ThermalZoneMoistCO2AirExchange.statistics.log"); + + +rScript=RunScript("modelica://AixLib/Resources/Scripts/Dymola/ThermalZones/ReducedOrder/Examples/ThermalZoneMoistCO2AirExchange.mos"); +simulateModel("AixLib.ThermalZones.ReducedOrder.Examples.ThermalZoneMoistCO2AirExchange", tolerance=1e-6, stopTime=3.1536e+007, numberOfIntervals=0, outputInterval=3600, method="CVode", resultFile="AixLib.ThermalZones.ReducedOrder.Examples.ThermalZoneMoistCO2AirExchange"); +Translation of AixLib.ThermalZones.ReducedOrder.Examples.ThermalZoneMoistCO2AirExchange +The DAE has 2112 scalar unknowns and 2112 scalar equations. + +Statistics + +Original Model + Number of components: 327 + Variables: 2902 + Constants: 94 (94 scalars) + Parameters: 826 (2658 scalars) + Unknowns: 1982 (2112 scalars) + Differentiated variables: 8 scalars + Equations: 1407 + Nontrivial: 1298 +Translated Model + Constants: 612 scalars + Free parameters: 1963 scalars + Parameter depending: 340 scalars + Outputs: 23 scalars + Continuous time states: 8 scalars + Time-varying variables: 653 scalars + Alias variables: 1296 scalars + Number of mixed real/discrete systems of equations: 0 + Sizes of linear systems of equations: {29, 4} + Sizes after manipulation of the linear systems: {4, 0} + Sizes of nonlinear systems of equations: {1, 1, 1, 1, 1, 1} + Sizes after manipulation of the nonlinear systems: {0, 1, 0, 1, 0, 1} + Number of numerical Jacobians: 0 + Initialization problem + Sizes of linear systems of equations: {32} + Sizes after manipulation of the linear systems: {5} + +Selected continuous time states +Statically selected continuous time states +thermalZone.ROM.extWallRC.thermCapExt[1].T +thermalZone.ROM.intWallRC.thermCapInt[1].T +thermalZone.ROM.volMoiAir.dynBal.m +thermalZone.ROM.volMoiAir.dynBal.mC[1] +thermalZone.ROM.volMoiAir.dynBal.medium.Xi[1] +thermalZone.ROM.volMoiAir.dynBal.U +thermalZone.ventCont.dEMA.ExpAVG.x[1] +thermalZone.ventCont.dEMA.ExpAVG1.x[1] +Finished +Finished + = true + + + + + + +Declaring variable: Boolean rScript ; + +savelog("AixLib.ThermalZones.ReducedOrder.Examples.ThermalZoneMoistCO2AirExchange.translation.log"); = true + + +rCheck = checkModel("AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case440"); +Check of AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case440 +The model has the same number of unknowns and equations: 1585 +The model has the same number of unknowns and equations +for the given numerical settings of parameters: 1585 +Check of AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case440 successful. +Declaring variable: Boolean rCheck ; + +Modelica.Utilities.Streams.print(" { \"file\" : \"AixLib/Resources/Scripts/Dymola/ThermalZones/HighOrder/Validation/ASHRAE140/Case440.mos\",", "AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case440.statistics.log"); +Modelica.Utilities.Streams.print(" \"model\" : \"AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case440\",", "AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case440.statistics.log"); +Modelica.Utilities.Streams.print(" \"check\" : {", "AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case440.statistics.log"); +Modelica.Utilities.Streams.print(" \"command\" : \"checkModel(\\\"AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case440\\\");\",", "AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case440.statistics.log"); +Modelica.Utilities.Streams.print(" \"result\" : " + String(rCheck), "AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case440.statistics.log"); +Modelica.Utilities.Streams.print(" },", "AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case440.statistics.log"); + + +rScript=RunScript("modelica://AixLib/Resources/Scripts/Dymola/ThermalZones/HighOrder/Validation/ASHRAE140/Case440.mos"); +simulateModel("AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case440", startTime=0, stopTime=31539600, outputInterval=1800, tolerance=1e-6, method="dassl", resultFile="AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case440"); +Translation of AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case440 +The DAE has 1585 scalar unknowns and 1585 scalar equations. + +Statistics + +Original Model + Number of components: 352 + Variables: 3082 + Constants: 41 (276 scalars) + Parameters: 1493 (2159 scalars) + Unknowns: 1548 (1585 scalars) + Differentiated variables: 25 scalars + Equations: 1257 + Nontrivial: 1045 +Translated Model + Constants: 780 scalars + Free parameters: 876 scalars + Parameter depending: 909 scalars + Outputs: 5 scalars + Continuous time states: 25 scalars + Time-varying variables: 474 scalars + Alias variables: 981 scalars + Number of mixed real/discrete systems of equations: 0 + Sizes of linear systems of equations: {4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 3, 4, 4, 4, 4} + Sizes after manipulation of the linear systems: {0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0} + Sizes of nonlinear systems of equations: {55} + Sizes after manipulation of the nonlinear systems: {13} + Number of numerical Jacobians: 0 + +Selected continuous time states +Statically selected continuous time states +idealHeaterCooler.pITempCool.PI.I.y +idealHeaterCooler.pITempHeat.PI.I.y +integrator2.y +integratorCool.y +integratorHeat.y +Room.airload.dynBal.m +Room.airload.dynBal.medium.Xi[1] +Room.airload.dynBal.U +Room.ceiling.Wall.simpleNLayer.cap[1].T +Room.ceiling.Wall.simpleNLayer.cap[2].T +Room.ceiling.Wall.simpleNLayer.cap[3].T +Room.floor.Wall.simpleNLayer.cap[1].T +Room.floor.Wall.simpleNLayer.cap[2].T +Room.wallEast.Wall.simpleNLayer.cap[1].T +Room.wallEast.Wall.simpleNLayer.cap[2].T +Room.wallEast.Wall.simpleNLayer.cap[3].T +Room.wallNorth.Wall.simpleNLayer.cap[1].T +Room.wallNorth.Wall.simpleNLayer.cap[2].T +Room.wallNorth.Wall.simpleNLayer.cap[3].T +Room.wallSouth.Wall.simpleNLayer.cap[1].T +Room.wallSouth.Wall.simpleNLayer.cap[2].T +Room.wallSouth.Wall.simpleNLayer.cap[3].T +Room.wallWest.Wall.simpleNLayer.cap[1].T +Room.wallWest.Wall.simpleNLayer.cap[2].T +Room.wallWest.Wall.simpleNLayer.cap[3].T +Finished +Finished + = true + +Declaring variable: Boolean rScript ; + +savelog("AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case440.translation.log"); = true + + +rCheck = checkModel("AixLib.ThermalZones.HighOrder.Examples.RoomGFOw2_DayNightMode"); +Check of AixLib.ThermalZones.HighOrder.Examples.RoomGFOw2_DayNightMode +Warning: Component type specifier Pump specified an obsolete type: Obsolete model - Use one of the valves in package AixLib.Fluid.Movers.. + File: /tmp/tmp-AixLib-1-4eecnjlx/AixLib/ThermalZones/HighOrder/Examples/RoomGFOw2_DayNightMode.mo, line 50 + Component context: Pump + Component declared as Pump Pump in AixLib.Obsolete.Year2021.Fluid.Movers +The model has the same number of unknowns and equations: 2610 +The model could not be deduced to be symbolically well-posed. +The model has + 2543+2*room_GF_2OW.airload.dynBal.nPorts+max([size(combinedWeather.WeatherData.columns, 1); size(combinedWeather.WeatherData.offset, 1)])+2*combinedWeather.deMultiplex.n1 +2*combinedWeather.deMultiplex.n2+2*combinedWeather.deMultiplex.n3+size( Pump.table_minMaxCharacteristics.columns, 1)+radiator_ML_delta.multiLayer_HE[1].Volume.dynBal.nPorts +radiator_ML_delta.multiLayer_HE[2].Volume.dynBal.nPorts+radiator_ML_delta.multiLayer_HE[3].Volume.dynBal.nPorts +radiator_ML_delta.multiLayer_HE[4].Volume.dynBal.nPorts+radiator_ML_delta.multiLayer_HE[5].Volume.dynBal.nPorts +radiator_ML_delta.multiLayer_HE[6].Volume.dynBal.nPorts+radiator_ML_delta.multiLayer_HE[7].Volume.dynBal.nPorts +radiator_ML_delta.multiLayer_HE[8].Volume.dynBal.nPorts+radiator_ML_delta.multiLayer_HE[9].Volume.dynBal.nPorts +radiator_ML_delta.multiLayer_HE[10].Volume.dynBal.nPorts+radiator_ML_delta.multiLayer_HE[11].Volume.dynBal.nPorts +radiator_ML_delta.multiLayer_HE[12].Volume.dynBal.nPorts+radiator_ML_delta.multiLayer_HE[13].Volume.dynBal.nPorts +radiator_ML_delta.multiLayer_HE[14].Volume.dynBal.nPorts+radiator_ML_delta.multiLayer_HE[15].Volume.dynBal.nPorts +radiator_ML_delta.multiLayer_HE[16].Volume.dynBal.nPorts +scalar unknowns and + 2434+(if not room_GF_2OW.outside_wall1.Wall.twoStar_RadEx.use_A_in then 1 else 0) +(if room_GF_2OW.outside_wall1.heatTransfer_Outside.calcMethod == AixLib.ThermalZones.HighOrder.Components.Types.CalcMethodConvectiveHeatTransfer. DIN_6946 then 1 else (if room_GF_2OW.outside_wall1.heatTransfer_Outside.calcMethod == AixLib.ThermalZones.HighOrder.Components.Types.CalcMethodConvectiveHeatTransfer. ASHRAE_Fundamentals then 1 else 2))+(if not room_GF_2OW.outside_wall2.Wall.twoStar_RadEx.use_A_in then 1 else 0)+(if room_GF_2OW.outside_wall2.heatTransfer_Outside.calcMethod == AixLib.ThermalZones.HighOrder.Components.Types.CalcMethodConvectiveHeatTransfer. DIN_6946 then 1 else (if room_GF_2OW.outside_wall2.heatTransfer_Outside.calcMethod == AixLib.ThermalZones.HighOrder.Components.Types.CalcMethodConvectiveHeatTransfer. ASHRAE_Fundamentals then 1 else 2))+(if not room_GF_2OW.inside_wall1.Wall.twoStar_RadEx.use_A_in then 1 else 0)+(if not room_GF_2OW.inside_wall2.Wall.twoStar_RadEx.use_A_in then 1 else 0)+(if not room_GF_2OW.Ceiling.Wall.twoStar_RadEx.use_A_in then 1 else 0)+(if not room_GF_2OW.floor.Wall.twoStar_RadEx.use_A_in then 1 else 0) +max([size(combinedWeather.WeatherData.columns, 1); size(combinedWeather.WeatherData.offset, 1)])+2*combinedWeather.deMultiplex.n1+2*combinedWeather.deMultiplex.n2+2* combinedWeather.deMultiplex.n3+size(Pump.table_minMaxCharacteristics.columns, 1) +(if tank.use_Xi_in then 1 else (if tank.use_X_in then 0 else 1))+(if not tank.use_p_in then 1 else 0)+2*tank.nPorts+(if not tank.use_h_in then 1 else 0) +(if not radiator_ML_delta.multiLayer_HE[1].twoStar_RadEx.use_A_in then 1 else 0)+(if not radiator_ML_delta.multiLayer_HE[2].twoStar_RadEx.use_A_in then 1 else 0)+(if not radiator_ML_delta.multiLayer_HE[3].twoStar_RadEx.use_A_in then 1 else 0)+(if not radiator_ML_delta.multiLayer_HE[4].twoStar_RadEx.use_A_in then 1 else 0)+(if not radiator_ML_delta.multiLayer_HE[5].twoStar_RadEx.use_A_in then 1 else 0)+(if not radiator_ML_delta.multiLayer_HE[6].twoStar_RadEx.use_A_in then 1 else 0)+(if not radiator_ML_delta.multiLayer_HE[7].twoStar_RadEx.use_A_in then 1 else 0)+(if not radiator_ML_delta.multiLayer_HE[8].twoStar_RadEx.use_A_in then 1 else 0)+(if not radiator_ML_delta.multiLayer_HE[9].twoStar_RadEx.use_A_in then 1 else 0)+(if not radiator_ML_delta.multiLayer_HE[10].twoStar_RadEx.use_A_in then 1 else 0)+(if not radiator_ML_delta.multiLayer_HE[11].twoStar_RadEx.use_A_in then 1 else 0)+(if not radiator_ML_delta.multiLayer_HE[12].twoStar_RadEx.use_A_in then 1 else 0)+(if not radiator_ML_delta.multiLayer_HE[13].twoStar_RadEx.use_A_in then 1 else 0)+(if not radiator_ML_delta.multiLayer_HE[14].twoStar_RadEx.use_A_in then 1 else 0)+(if not radiator_ML_delta.multiLayer_HE[15].twoStar_RadEx.use_A_in then 1 else 0)+(if not radiator_ML_delta.multiLayer_HE[16].twoStar_RadEx.use_A_in then 1 else 0)+5*room_GF_2OW.airload.dynBal.nPorts+(if not radiator_ML_delta.multiLayer_HE[1].Volume.dynBal.use_mWat_flow then 1 else 0)+3*radiator_ML_delta.multiLayer_HE[1].Volume.dynBal.nPorts+(if not radiator_ML_delta.multiLayer_HE[2].Volume.dynBal.use_mWat_flow then 1 else 0)+3*radiator_ML_delta.multiLayer_HE[2].Volume.dynBal.nPorts+(if not radiator_ML_delta.multiLayer_HE[3].Volume.dynBal.use_mWat_flow then 1 else 0)+3 *radiator_ML_delta.multiLayer_HE[3].Volume.dynBal.nPorts+(if not radiator_ML_delta.multiLayer_HE[4].Volume.dynBal.use_mWat_flow then 1 else 0)+3 *radiator_ML_delta.multiLayer_HE[4].Volume.dynBal.nPorts+(if not radiator_ML_delta.multiLayer_HE[5].Volume.dynBal.use_mWat_flow then 1 else 0)+3 *radiator_ML_delta.multiLayer_HE[5].Volume.dynBal.nPorts+(if not radiator_ML_delta.multiLayer_HE[6].Volume.dynBal.use_mWat_flow then 1 else 0)+3 *radiator_ML_delta.multiLayer_HE[6].Volume.dynBal.nPorts+(if not radiator_ML_delta.multiLayer_HE[7].Volume.dynBal.use_mWat_flow then 1 else 0)+3 *radiator_ML_delta.multiLayer_HE[7].Volume.dynBal.nPorts+(if not radiator_ML_delta.multiLayer_HE[8].Volume.dynBal.use_mWat_flow then 1 else 0)+3 *radiator_ML_delta.multiLayer_HE[8].Volume.dynBal.nPorts+(if not radiator_ML_delta.multiLayer_HE[9].Volume.dynBal.use_mWat_flow then 1 else 0)+3 *radiator_ML_delta.multiLayer_HE[9].Volume.dynBal.nPorts+(if not radiator_ML_delta.multiLayer_HE[10].Volume.dynBal.use_mWat_flow then 1 else 0) +3*radiator_ML_delta.multiLayer_HE[10].Volume.dynBal.nPorts+(if not radiator_ML_delta.multiLayer_HE[11].Volume.dynBal.use_mWat_flow then 1 else 0) +3*radiator_ML_delta.multiLayer_HE[11].Volume.dynBal.nPorts+(if not radiator_ML_delta.multiLayer_HE[12].Volume.dynBal.use_mWat_flow then 1 else 0) +3*radiator_ML_delta.multiLayer_HE[12].Volume.dynBal.nPorts+(if not radiator_ML_delta.multiLayer_HE[13].Volume.dynBal.use_mWat_flow then 1 else 0) +3*radiator_ML_delta.multiLayer_HE[13].Volume.dynBal.nPorts+(if not radiator_ML_delta.multiLayer_HE[14].Volume.dynBal.use_mWat_flow then 1 else 0) +3*radiator_ML_delta.multiLayer_HE[14].Volume.dynBal.nPorts+(if not radiator_ML_delta.multiLayer_HE[15].Volume.dynBal.use_mWat_flow then 1 else 0) +3*radiator_ML_delta.multiLayer_HE[15].Volume.dynBal.nPorts+(if not radiator_ML_delta.multiLayer_HE[16].Volume.dynBal.use_mWat_flow then 1 else 0) +3*radiator_ML_delta.multiLayer_HE[16].Volume.dynBal.nPorts +scalar equations. +However, exploiting the given numerical settings of parameters gives the same number of unknowns and equations: + 2610 +Check of AixLib.ThermalZones.HighOrder.Examples.RoomGFOw2_DayNightMode successful. +Declaring variable: Boolean rCheck ; + +Modelica.Utilities.Streams.print(" { \"file\" : \"AixLib/Resources/Scripts/Dymola/ThermalZones/HighOrder/Examples/RoomGFOw2_DayNightMode.mos\",", "AixLib.ThermalZones.HighOrder.Examples.RoomGFOw2_DayNightMode.statistics.log"); +Modelica.Utilities.Streams.print(" \"model\" : \"AixLib.ThermalZones.HighOrder.Examples.RoomGFOw2_DayNightMode\",", "AixLib.ThermalZones.HighOrder.Examples.RoomGFOw2_DayNightMode.statistics.log"); +Modelica.Utilities.Streams.print(" \"check\" : {", "AixLib.ThermalZones.HighOrder.Examples.RoomGFOw2_DayNightMode.statistics.log"); +Modelica.Utilities.Streams.print(" \"command\" : \"checkModel(\\\"AixLib.ThermalZones.HighOrder.Examples.RoomGFOw2_DayNightMode\\\");\",", "AixLib.ThermalZones.HighOrder.Examples.RoomGFOw2_DayNightMode.statistics.log"); +Modelica.Utilities.Streams.print(" \"result\" : " + String(rCheck), "AixLib.ThermalZones.HighOrder.Examples.RoomGFOw2_DayNightMode.statistics.log"); +Modelica.Utilities.Streams.print(" },", "AixLib.ThermalZones.HighOrder.Examples.RoomGFOw2_DayNightMode.statistics.log"); + + +rScript=RunScript("modelica://AixLib/Resources/Scripts/Dymola/ThermalZones/HighOrder/Examples/RoomGFOw2_DayNightMode.mos"); +simulateModel("AixLib.ThermalZones.HighOrder.Examples.RoomGFOw2_DayNightMode", startTime=0, stopTime=86400, outputInterval=60, tolerance=1e-6, method="dassl", resultFile="AixLib.ThermalZones.HighOrder.Examples.RoomGFOw2_DayNightMode"); +Translation of AixLib.ThermalZones.HighOrder.Examples.RoomGFOw2_DayNightMode +Warning: Component type specifier Pump specified an obsolete type: Obsolete model - Use one of the valves in package AixLib.Fluid.Movers.. + File: /tmp/tmp-AixLib-1-4eecnjlx/AixLib/ThermalZones/HighOrder/Examples/RoomGFOw2_DayNightMode.mo, line 50 + Component context: Pump + Component declared as Pump Pump in AixLib.Obsolete.Year2021.Fluid.Movers +The DAE has 2610 scalar unknowns and 2610 scalar equations. +The translated model contains large nonlinear systems of equations. The simulation may run faster in DAE mode. Enable DAE mode by setting the flag Advanced.Define.DAEsolver and use one of the solvers Dassl, Radau IIa, Esdirk*, or Sdirk34hw. + +Statistics + +Original Model + Number of components: 505 + Variables: 6172 + Constants: 85 (85 scalars) + Parameters: 2965 (4257 scalars) + Unknowns: 3122 (2681 scalars) + Differentiated variables: 73 scalars + Equations: 2382 + Nontrivial: 1897 +Translated Model + Constants: 1638 scalars + Free parameters: 888 scalars + Parameter depending: 1976 scalars + Outputs: 4 scalars + Continuous time states: 57 scalars + Time-varying variables: 754 scalars + Alias variables: 1767 scalars + Number of mixed real/discrete systems of equations: 0 + Sizes of linear systems of equations: {4, 4, 4, 4, 3, 4, 3, 4, 4, 4, 4, 4, 3, 4, 4, 4, 3} + Sizes after manipulation of the linear systems: {0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0} + Sizes of nonlinear systems of equations: {149, 11} + Sizes after manipulation of the nonlinear systems: {23, 1} + Number of numerical Jacobians: 0 + Initialization problem + Sizes of nonlinear systems of equations: {278, 11, 1} + Sizes after manipulation of the nonlinear systems: {73, 1, 0} + Sizes of simplified homotopy nonlinear systems of equations: {11, 1} + Sizes after manipulation of the simplified homotopy nonlinear systems: {1, 0} + Number of numerical Jacobians: 0 + +Sparse solvers enabled: false +Enabled for systems of equations: false +Number of systems sparse enough: 0. +Systems close to sparse, but not sparse enough: +System: size, density: +initialization.nonlinear[1]: 73, 0.0467255 + +Set minimum number of variables required using Advanced.Translation.SparseMinimumStates and maximum density allowed using Advanced.Translation.SparseMaximumDensity. +Enable sparse solvers by setting Advanced.Translation.SparseActivate. +Selected continuous time states +Statically selected continuous time states +firstOrder.y +heatValve_new.filter.s[1] +heatValve_new.filter.s[2] +radiator_ML_delta.FlowTemperature.T +radiator_ML_delta.multiLayer_HE[1].radiator_wall.heatCapacitor.T +radiator_ML_delta.multiLayer_HE[1].Volume.dynBal.U +radiator_ML_delta.multiLayer_HE[2].radiator_wall.heatCapacitor.T +radiator_ML_delta.multiLayer_HE[2].Volume.dynBal.U +radiator_ML_delta.multiLayer_HE[3].radiator_wall.heatCapacitor.T +radiator_ML_delta.multiLayer_HE[3].Volume.dynBal.U +radiator_ML_delta.multiLayer_HE[4].radiator_wall.heatCapacitor.T +radiator_ML_delta.multiLayer_HE[4].Volume.dynBal.U +radiator_ML_delta.multiLayer_HE[5].radiator_wall.heatCapacitor.T +radiator_ML_delta.multiLayer_HE[5].Volume.dynBal.U +radiator_ML_delta.multiLayer_HE[6].radiator_wall.heatCapacitor.T +radiator_ML_delta.multiLayer_HE[6].Volume.dynBal.U +radiator_ML_delta.multiLayer_HE[7].radiator_wall.heatCapacitor.T +radiator_ML_delta.multiLayer_HE[7].Volume.dynBal.U +radiator_ML_delta.multiLayer_HE[8].radiator_wall.heatCapacitor.T +radiator_ML_delta.multiLayer_HE[8].Volume.dynBal.U +radiator_ML_delta.multiLayer_HE[9].radiator_wall.heatCapacitor.T +radiator_ML_delta.multiLayer_HE[9].Volume.dynBal.U +radiator_ML_delta.multiLayer_HE[10].radiator_wall.heatCapacitor.T +radiator_ML_delta.multiLayer_HE[10].Volume.dynBal.U +radiator_ML_delta.multiLayer_HE[11].radiator_wall.heatCapacitor.T +radiator_ML_delta.multiLayer_HE[11].Volume.dynBal.U +radiator_ML_delta.multiLayer_HE[12].radiator_wall.heatCapacitor.T +radiator_ML_delta.multiLayer_HE[12].Volume.dynBal.U +radiator_ML_delta.multiLayer_HE[13].radiator_wall.heatCapacitor.T +radiator_ML_delta.multiLayer_HE[13].Volume.dynBal.U +radiator_ML_delta.multiLayer_HE[14].radiator_wall.heatCapacitor.T +radiator_ML_delta.multiLayer_HE[14].Volume.dynBal.U +radiator_ML_delta.multiLayer_HE[15].radiator_wall.heatCapacitor.T +radiator_ML_delta.multiLayer_HE[15].Volume.dynBal.U +radiator_ML_delta.multiLayer_HE[16].radiator_wall.heatCapacitor.T +radiator_ML_delta.multiLayer_HE[16].Volume.dynBal.U +radiator_ML_delta.ReturnTemperature.T +room_GF_2OW.airload.dynBal.m +room_GF_2OW.airload.dynBal.medium.Xi[1] +room_GF_2OW.airload.dynBal.U +room_GF_2OW.Ceiling.Wall.simpleNLayer.cap[1].T +room_GF_2OW.Ceiling.Wall.simpleNLayer.cap[2].T +room_GF_2OW.Ceiling.Wall.simpleNLayer.cap[3].T +room_GF_2OW.floor.Wall.simpleNLayer.cap[1].T +room_GF_2OW.floor.Wall.simpleNLayer.cap[2].T +room_GF_2OW.inside_wall1.Wall.simpleNLayer.cap[1].T +room_GF_2OW.inside_wall1.Wall.simpleNLayer.cap[2].T +room_GF_2OW.inside_wall2.Wall.simpleNLayer.cap[1].T +room_GF_2OW.inside_wall2.Wall.simpleNLayer.cap[2].T +room_GF_2OW.outside_wall1.Wall.simpleNLayer.cap[1].T +room_GF_2OW.outside_wall1.Wall.simpleNLayer.cap[2].T +room_GF_2OW.outside_wall1.Wall.simpleNLayer.cap[3].T +room_GF_2OW.outside_wall1.Wall.simpleNLayer.cap[4].T +room_GF_2OW.outside_wall2.Wall.simpleNLayer.cap[1].T +room_GF_2OW.outside_wall2.Wall.simpleNLayer.cap[2].T +room_GF_2OW.outside_wall2.Wall.simpleNLayer.cap[3].T +room_GF_2OW.outside_wall2.Wall.simpleNLayer.cap[4].T +Finished +Warning: WARNINGS have been issued. +Finished + = true + +Declaring variable: Boolean rScript ; + +savelog("AixLib.ThermalZones.HighOrder.Examples.RoomGFOw2_DayNightMode.translation.log"); = true + + +rCheck = checkModel("AixLib.ThermalZones.ReducedOrder.Examples.MultizoneEquipped"); +Check of AixLib.ThermalZones.ReducedOrder.Examples.MultizoneEquipped +The model has the same number of unknowns and equations: 9930 +The model has the same number of unknowns and equations +for the given numerical settings of parameters: 9930 +Check of AixLib.ThermalZones.ReducedOrder.Examples.MultizoneEquipped successful. +Declaring variable: Boolean rCheck ; + +Modelica.Utilities.Streams.print(" { \"file\" : \"AixLib/Resources/Scripts/Dymola/ThermalZones/ReducedOrder/Examples/MultizoneEquipped.mos\",", "AixLib.ThermalZones.ReducedOrder.Examples.MultizoneEquipped.statistics.log"); +Modelica.Utilities.Streams.print(" \"model\" : \"AixLib.ThermalZones.ReducedOrder.Examples.MultizoneEquipped\",", "AixLib.ThermalZones.ReducedOrder.Examples.MultizoneEquipped.statistics.log"); +Modelica.Utilities.Streams.print(" \"check\" : {", "AixLib.ThermalZones.ReducedOrder.Examples.MultizoneEquipped.statistics.log"); +Modelica.Utilities.Streams.print(" \"command\" : \"checkModel(\\\"AixLib.ThermalZones.ReducedOrder.Examples.MultizoneEquipped\\\");\",", "AixLib.ThermalZones.ReducedOrder.Examples.MultizoneEquipped.statistics.log"); +Modelica.Utilities.Streams.print(" \"result\" : " + String(rCheck), "AixLib.ThermalZones.ReducedOrder.Examples.MultizoneEquipped.statistics.log"); +Modelica.Utilities.Streams.print(" },", "AixLib.ThermalZones.ReducedOrder.Examples.MultizoneEquipped.statistics.log"); + + +rScript=RunScript("modelica://AixLib/Resources/Scripts/Dymola/ThermalZones/ReducedOrder/Examples/MultizoneEquipped.mos"); +simulateModel("AixLib.ThermalZones.ReducedOrder.Examples.MultizoneEquipped", tolerance=1e-6, stopTime=864000, numberOfIntervals=0, outputInterval=3600, method="CVode", resultFile="AixLib.ThermalZones.ReducedOrder.Examples.MultizoneEquipped"); +Translation of AixLib.ThermalZones.ReducedOrder.Examples.MultizoneEquipped +The DAE has 9930 scalar unknowns and 9930 scalar equations. + +Statistics + +Original Model + Number of components: 1462 + Variables: 15306 + Constants: 319 (319 scalars) + Parameters: 5611 (7031 scalars) + Unknowns: 9374 (9975 scalars) + Differentiated variables: 35 scalars + Equations: 6460 + Nontrivial: 5930 +Translated Model + Constants: 2819 scalars + Free parameters: 1654 scalars + Parameter depending: 3663 scalars + Continuous time states: 35 scalars + Time-varying variables: 3131 scalars + Alias variables: 6058 scalars + Number of mixed real/discrete systems of equations: 0 + Sizes of linear systems of equations: {2, 29, 4, 2, 29, 4, 2, 29, 4, 2, 29, 4, 2, 29, 4} + Sizes after manipulation of the linear systems: {0, 4, 0, 0, 4, 0, 0, 4, 0, 0, 4, 0, 0, 4, 0} + Sizes of nonlinear systems of equations: {6, 6, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1} + Sizes after manipulation of the nonlinear systems: {1, 1, 0, 0, 1, 0, 1, 0, 1, 0, 1, 0, 1, 0, 1, 0, 1, 0, 1, 0, 1, 0, 1, 0, 1, 0, 1, 0, 1, 0, 1, 0, 1} + Number of numerical Jacobians: 0 + Initialization problem + Sizes of linear systems of equations: {32, 32, 32, 32, 32} + Sizes after manipulation of the linear systems: {5, 5, 5, 5, 5} + +Selected continuous time states +Statically selected continuous time states +multizone.zone[1].heaterCooler.pITempHeat.PI.I.y +multizone.zone[1].ROM.extWallRC.thermCapExt[1].T +multizone.zone[1].ROM.intWallRC.thermCapInt[1].T +multizone.zone[1].ROM.volAir.dynBal.m +multizone.zone[1].ROM.volAir.dynBal.U +multizone.zone[1].ventCont.dEMA.ExpAVG.x[1] +multizone.zone[1].ventCont.dEMA.ExpAVG1.x[1] +multizone.zone[2].heaterCooler.pITempHeat.PI.I.y +multizone.zone[2].ROM.extWallRC.thermCapExt[1].T +multizone.zone[2].ROM.intWallRC.thermCapInt[1].T +multizone.zone[2].ROM.volAir.dynBal.m +multizone.zone[2].ROM.volAir.dynBal.U +multizone.zone[2].ventCont.dEMA.ExpAVG.x[1] +multizone.zone[2].ventCont.dEMA.ExpAVG1.x[1] +multizone.zone[3].heaterCooler.pITempHeat.PI.I.y +multizone.zone[3].ROM.extWallRC.thermCapExt[1].T +multizone.zone[3].ROM.intWallRC.thermCapInt[1].T +multizone.zone[3].ROM.volAir.dynBal.m +multizone.zone[3].ROM.volAir.dynBal.U +multizone.zone[3].ventCont.dEMA.ExpAVG.x[1] +multizone.zone[3].ventCont.dEMA.ExpAVG1.x[1] +multizone.zone[4].heaterCooler.pITempHeat.PI.I.y +multizone.zone[4].ROM.extWallRC.thermCapExt[1].T +multizone.zone[4].ROM.intWallRC.thermCapInt[1].T +multizone.zone[4].ROM.volAir.dynBal.m +multizone.zone[4].ROM.volAir.dynBal.U +multizone.zone[4].ventCont.dEMA.ExpAVG.x[1] +multizone.zone[4].ventCont.dEMA.ExpAVG1.x[1] +multizone.zone[5].heaterCooler.pITempHeat.PI.I.y +multizone.zone[5].ROM.extWallRC.thermCapExt[1].T +multizone.zone[5].ROM.intWallRC.thermCapInt[1].T +multizone.zone[5].ROM.volAir.dynBal.m +multizone.zone[5].ROM.volAir.dynBal.U +multizone.zone[5].ventCont.dEMA.ExpAVG.x[1] +multizone.zone[5].ventCont.dEMA.ExpAVG1.x[1] +Finished +Finished + = true + +Declaring variable: Boolean rScript ; + +savelog("AixLib.ThermalZones.ReducedOrder.Examples.MultizoneEquipped.translation.log"); = true + + +rCheck = checkModel("AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case950FF"); +Check of AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case950FF +The model has the same number of unknowns and equations: 1434 +The model has the same number of unknowns and equations +for the given numerical settings of parameters: 1434 +Check of AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case950FF successful. +Declaring variable: Boolean rCheck ; + +Modelica.Utilities.Streams.print(" { \"file\" : \"AixLib/Resources/Scripts/Dymola/ThermalZones/HighOrder/Validation/ASHRAE140/Case950FF.mos\",", "AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case950FF.statistics.log"); +Modelica.Utilities.Streams.print(" \"model\" : \"AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case950FF\",", "AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case950FF.statistics.log"); +Modelica.Utilities.Streams.print(" \"check\" : {", "AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case950FF.statistics.log"); +Modelica.Utilities.Streams.print(" \"command\" : \"checkModel(\\\"AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case950FF\\\");\",", "AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case950FF.statistics.log"); +Modelica.Utilities.Streams.print(" \"result\" : " + String(rCheck), "AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case950FF.statistics.log"); +Modelica.Utilities.Streams.print(" },", "AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case950FF.statistics.log"); + + +rScript=RunScript("modelica://AixLib/Resources/Scripts/Dymola/ThermalZones/HighOrder/Validation/ASHRAE140/Case950FF.mos"); +simulateModel("AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case950FF", startTime=0, stopTime=31539600, outputInterval=1800, tolerance=1e-6, method="dassl", resultFile="AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case950FF"); +Translation of AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case950FF +The DAE has 1434 scalar unknowns and 1434 scalar equations. + +Statistics + +Original Model + Number of components: 303 + Variables: 2724 + Constants: 39 (274 scalars) + Parameters: 1288 (1982 scalars) + Unknowns: 1397 (1434 scalars) + Differentiated variables: 21 scalars + Equations: 1107 + Nontrivial: 906 +Translated Model + Constants: 722 scalars + Free parameters: 749 scalars + Parameter depending: 891 scalars + Outputs: 3 scalars + Continuous time states: 21 scalars + Time-varying variables: 438 scalars + Alias variables: 890 scalars + Number of mixed real/discrete systems of equations: 0 + Sizes of linear systems of equations: {4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 3, 4, 4, 4, 4} + Sizes after manipulation of the linear systems: {0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0} + Sizes of nonlinear systems of equations: {55} + Sizes after manipulation of the nonlinear systems: {13} + Number of numerical Jacobians: 0 + +Selected continuous time states +Statically selected continuous time states +integrator2.y +Room.airload.dynBal.m +Room.airload.dynBal.medium.Xi[1] +Room.airload.dynBal.U +Room.ceiling.Wall.simpleNLayer.cap[1].T +Room.ceiling.Wall.simpleNLayer.cap[2].T +Room.ceiling.Wall.simpleNLayer.cap[3].T +Room.floor.Wall.simpleNLayer.cap[1].T +Room.floor.Wall.simpleNLayer.cap[2].T +Room.wallEast.Wall.simpleNLayer.cap[1].T +Room.wallEast.Wall.simpleNLayer.cap[2].T +Room.wallEast.Wall.simpleNLayer.cap[3].T +Room.wallNorth.Wall.simpleNLayer.cap[1].T +Room.wallNorth.Wall.simpleNLayer.cap[2].T +Room.wallNorth.Wall.simpleNLayer.cap[3].T +Room.wallSouth.Wall.simpleNLayer.cap[1].T +Room.wallSouth.Wall.simpleNLayer.cap[2].T +Room.wallSouth.Wall.simpleNLayer.cap[3].T +Room.wallWest.Wall.simpleNLayer.cap[1].T +Room.wallWest.Wall.simpleNLayer.cap[2].T +Room.wallWest.Wall.simpleNLayer.cap[3].T +Finished +Finished + = true + +Declaring variable: Boolean rScript ; + +savelog("AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case950FF.translation.log"); = true + + +rCheck = checkModel("AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case400"); +Check of AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case400 +The model has the same number of unknowns and equations: 1568 +The model has the same number of unknowns and equations +for the given numerical settings of parameters: 1568 +Check of AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case400 successful. +Declaring variable: Boolean rCheck ; + +Modelica.Utilities.Streams.print(" { \"file\" : \"AixLib/Resources/Scripts/Dymola/ThermalZones/HighOrder/Validation/ASHRAE140/Case400.mos\",", "AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case400.statistics.log"); +Modelica.Utilities.Streams.print(" \"model\" : \"AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case400\",", "AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case400.statistics.log"); +Modelica.Utilities.Streams.print(" \"check\" : {", "AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case400.statistics.log"); +Modelica.Utilities.Streams.print(" \"command\" : \"checkModel(\\\"AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case400\\\");\",", "AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case400.statistics.log"); +Modelica.Utilities.Streams.print(" \"result\" : " + String(rCheck), "AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case400.statistics.log"); +Modelica.Utilities.Streams.print(" },", "AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case400.statistics.log"); + + +rScript=RunScript("modelica://AixLib/Resources/Scripts/Dymola/ThermalZones/HighOrder/Validation/ASHRAE140/Case400.mos"); +simulateModel("AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case400", startTime=0, stopTime=31539600, outputInterval=1800, tolerance=1e-6, method="dassl", resultFile="AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case400"); +Translation of AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case400 +The DAE has 1568 scalar unknowns and 1568 scalar equations. + +Statistics + +Original Model + Number of components: 349 + Variables: 3047 + Constants: 41 (276 scalars) + Parameters: 1474 (2065 scalars) + Unknowns: 1532 (1568 scalars) + Differentiated variables: 25 scalars + Equations: 1252 + Nontrivial: 1041 +Translated Model + Constants: 771 scalars + Free parameters: 794 scalars + Parameter depending: 906 scalars + Outputs: 5 scalars + Continuous time states: 25 scalars + Time-varying variables: 461 scalars + Alias variables: 977 scalars + Number of mixed real/discrete systems of equations: 0 + Sizes of linear systems of equations: {4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 3, 4, 4, 4, 4} + Sizes after manipulation of the linear systems: {0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0} + Sizes of nonlinear systems of equations: {55} + Sizes after manipulation of the nonlinear systems: {13} + Number of numerical Jacobians: 0 + +Selected continuous time states +Statically selected continuous time states +idealHeaterCooler.pITempCool.PI.I.y +idealHeaterCooler.pITempHeat.PI.I.y +integrator2.y +integratorCool.y +integratorHeat.y +Room.airload.dynBal.m +Room.airload.dynBal.medium.Xi[1] +Room.airload.dynBal.U +Room.ceiling.Wall.simpleNLayer.cap[1].T +Room.ceiling.Wall.simpleNLayer.cap[2].T +Room.ceiling.Wall.simpleNLayer.cap[3].T +Room.floor.Wall.simpleNLayer.cap[1].T +Room.floor.Wall.simpleNLayer.cap[2].T +Room.wallEast.Wall.simpleNLayer.cap[1].T +Room.wallEast.Wall.simpleNLayer.cap[2].T +Room.wallEast.Wall.simpleNLayer.cap[3].T +Room.wallNorth.Wall.simpleNLayer.cap[1].T +Room.wallNorth.Wall.simpleNLayer.cap[2].T +Room.wallNorth.Wall.simpleNLayer.cap[3].T +Room.wallSouth.Wall.simpleNLayer.cap[1].T +Room.wallSouth.Wall.simpleNLayer.cap[2].T +Room.wallSouth.Wall.simpleNLayer.cap[3].T +Room.wallWest.Wall.simpleNLayer.cap[1].T +Room.wallWest.Wall.simpleNLayer.cap[2].T +Room.wallWest.Wall.simpleNLayer.cap[3].T +Finished +Finished + = true + +Declaring variable: Boolean rScript ; + +savelog("AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case400.translation.log"); = true + + +rCheck = checkModel("AixLib.ThermalZones.ReducedOrder.Examples.ComparisonThermalZoneMoistAndDryAir"); +Warning: Can not resolve link "AixLib.ThermalZones.ReducedOrder.ThermalZone.ThermalZoneMoistAir" in AixLib.ThermalZones.ReducedOrder.Examples.ComparisonThermalZoneMoistAndDryAir +Check of AixLib.ThermalZones.ReducedOrder.Examples.ComparisonThermalZoneMoistAndDryAir +The model has the same number of unknowns and equations: 3863 +The model could not be deduced to be symbolically well-posed. +The model has + 3547+29*thermalZoneMoistAir.zoneParam.nOrientations+2*thermalZoneMoistAir.ROM.volMoiAir.dynBal.nPorts +thermalZoneMoistAir.humanTotHeaDependent.productHeatOutput.nu+ thermalZoneMoistAir.humanTotHeaDependent.productMoistureOutput.nu+ thermalZoneMoistAir.machinesSenHea.productHeatOutput.nu+thermalZoneMoistAir.lights.productHeatOutput.nu +thermalZoneMoistAir.SumQLat1_flow.nu+max([size(internalGains.columns, 1); size(internalGains.offset, 1)])+29*thermalZone.zoneParam.nOrientations+2* thermalZone.ROM.volAir.dynBal.nPorts+thermalZone.humanSenHeaDependent.productHeatOutput.nu +thermalZone.machinesSenHea.productHeatOutput.nu+thermalZone.lights.productHeatOutput.nu +max([size(internalGains1.columns, 1); size(internalGains1.offset, 1)]) +scalar unknowns and + 3608+(if weaDat.pAtmSou == AixLib.BoundaryConditions.Types.DataSource.Parameter then 1 else 0)+(if weaDat.TDewPoiSou == AixLib.BoundaryConditions.Types.DataSource. Parameter then 1 else 0)+(if weaDat.TDryBulSou == AixLib.BoundaryConditions.Types.DataSource. Parameter then 1 else 0)+(if weaDat.TBlaSkySou == AixLib.BoundaryConditions.Types.DataSource. Parameter then 1 else 0)+(if weaDat.relHumSou == AixLib.BoundaryConditions.Types.DataSource. Parameter then 1 else 0)+(if weaDat.opaSkyCovSou == AixLib.BoundaryConditions.Types.DataSource. Parameter then 1 else 0)+(if weaDat.ceiHeiSou == AixLib.BoundaryConditions.Types.DataSource. Parameter then 1 else 0)+(if weaDat.totSkyCovSou == AixLib.BoundaryConditions.Types.DataSource. Parameter then 1 else 0)+(if weaDat.winSpeSou == AixLib.BoundaryConditions.Types.DataSource. Parameter then 1 else 0)+(if weaDat.winDirSou == AixLib.BoundaryConditions.Types.DataSource. Parameter then 1 else 0)+(if weaDat.HInfHorSou == AixLib.BoundaryConditions.Types.DataSource. Parameter then 1 else 0)+(if weaDat.HSou == AixLib.BoundaryConditions.Types.RadiationDataSource. Input_HDirNor_HDifHor then 2 else 1)+(if weaDat.HSou == AixLib.BoundaryConditions.Types.RadiationDataSource. Input_HDirNor_HGloHor then 2 else 1)+(if weaDat.HSou == AixLib.BoundaryConditions.Types.RadiationDataSource. Input_HGloHor_HDifHor then 2 else 1)+max([size(internalGains.columns, 1); size (internalGains.offset, 1)])+(if sourcAir.use_Xi_in then 2 else (if sourcAir.use_X_in then 1 else 3))+3*sourcAir.nPorts+(if not sourcAir.use_m_flow_in then 1 else 0)+(if not sourcAir.use_T_in then 1 else 0)+(if sinAir.use_Xi_in then 2 else (if sinAir.use_X_in then 1 else 3))+3*sinAir.nPorts+(if not sinAir.use_p_in then 1 else 0)+(if not sinAir.use_T_in then 1 else 0)+max([ size(internalGains1.columns, 1); size(internalGains1.offset, 1)])+(if sourcAir1.use_Xi_in then 2 else (if sourcAir1.use_X_in then 1 else 3))+3* sourcAir1.nPorts+(if not sourcAir1.use_m_flow_in then 1 else 0)+(if not sourcAir1.use_T_in then 1 else 0)+(if sinAir1.use_Xi_in then 2 else (if sinAir1.use_X_in then 1 else 3))+3*sinAir1.nPorts+(if not sinAir1.use_p_in then 1 else 0)+(if not sinAir1.use_T_in then 1 else 0)+19*thermalZoneMoistAir.zoneParam.nOrientations +(if not thermalZoneMoistAir.eqAirTempWall.TGroundFromInput then 1 else 0)+19 *thermalZone.zoneParam.nOrientations+(if not thermalZone.eqAirTempWall.TGroundFromInput then 1 else 0)+5*thermalZoneMoistAir.ROM.volMoiAir.dynBal.nPorts+(if not thermalZone.ROM.volAir.dynBal.use_mWat_flow then 1 else 0)+5*thermalZone.ROM.volAir.dynBal.nPorts +scalar equations. +However, exploiting the given numerical settings of parameters gives the same number of unknowns and equations: + 3863 +Check of AixLib.ThermalZones.ReducedOrder.Examples.ComparisonThermalZoneMoistAndDryAir successful. +Declaring variable: Boolean rCheck ; + +Modelica.Utilities.Streams.print(" { \"file\" : \"AixLib/Resources/Scripts/Dymola/ThermalZones/ReducedOrder/Examples/ComparisonThermalZoneMoistAndDryAir.mos\",", "AixLib.ThermalZones.ReducedOrder.Examples.ComparisonThermalZoneMoistAndDryAir.statistics.log"); +Modelica.Utilities.Streams.print(" \"model\" : \"AixLib.ThermalZones.ReducedOrder.Examples.ComparisonThermalZoneMoistAndDryAir\",", "AixLib.ThermalZones.ReducedOrder.Examples.ComparisonThermalZoneMoistAndDryAir.statistics.log"); +Modelica.Utilities.Streams.print(" \"check\" : {", "AixLib.ThermalZones.ReducedOrder.Examples.ComparisonThermalZoneMoistAndDryAir.statistics.log"); +Modelica.Utilities.Streams.print(" \"command\" : \"checkModel(\\\"AixLib.ThermalZones.ReducedOrder.Examples.ComparisonThermalZoneMoistAndDryAir\\\");\",", "AixLib.ThermalZones.ReducedOrder.Examples.ComparisonThermalZoneMoistAndDryAir.statistics.log"); +Modelica.Utilities.Streams.print(" \"result\" : " + String(rCheck), "AixLib.ThermalZones.ReducedOrder.Examples.ComparisonThermalZoneMoistAndDryAir.statistics.log"); +Modelica.Utilities.Streams.print(" },", "AixLib.ThermalZones.ReducedOrder.Examples.ComparisonThermalZoneMoistAndDryAir.statistics.log"); + + +rScript=RunScript("modelica://AixLib/Resources/Scripts/Dymola/ThermalZones/ReducedOrder/Examples/ComparisonThermalZoneMoistAndDryAir.mos"); +simulateModel("AixLib.ThermalZones.ReducedOrder.Examples.ComparisonThermalZoneMoistAndDryAir", tolerance=1e-6, stopTime=3.1536e+007, numberOfIntervals=0, outputInterval=3600, method="CVode", resultFile="AixLib.ThermalZones.ReducedOrder.Examples.ComparisonThermalZoneMoistAndDryAir"); +Translation of AixLib.ThermalZones.ReducedOrder.Examples.ComparisonThermalZoneMoistAndDryAir +The DAE has 3863 scalar unknowns and 3863 scalar equations. +Redundant consistent initial conditions. +Removed the following equations which are redundant and consistent: + if (thermalZoneMoistAir.ROM.volMoiAir.dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (thermalZoneMoistAir.ROM.volMoiAir.dynBal.initialize_p) then + thermalZoneMoistAir.ROM.volMoiAir.dynBal.medium.p = thermalZoneMoistAir.ROM.volMoiAir.dynBal.p_start; + end if; + else + if (thermalZoneMoistAir.ROM.volMoiAir.dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then + if (thermalZoneMoistAir.ROM.volMoiAir.dynBal.initialize_p) then + der(thermalZoneMoistAir.ROM.volMoiAir.dynBal.medium.p) = 0; + end if; + end if; + end if; + if (thermalZone.ROM.volAir.dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (thermalZone.ROM.volAir.dynBal.initialize_p) then + thermalZone.ROM.volAir.dynBal.medium.p = thermalZone.ROM.volAir.dynBal.p_start; + end if; + else + if (thermalZone.ROM.volAir.dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. SteadyStateInitial) then + if (thermalZone.ROM.volAir.dynBal.initialize_p) then + der(thermalZone.ROM.volAir.dynBal.medium.p) = 0; + end if; + end if; + end if; + +This required evaluation of +the interactive parameters + sinAir.p(start = 101325) + sinAir1.p(start = 101325) + thermalZone.p_start(start = 101325) + thermalZoneMoistAir.p_start(start = 101325) + +The redundancies involve +initial equations: + thermalZoneMoistAir.ROM.volMoiAir.dynBal.medium.p = thermalZoneMoistAir.ROM.volMoiAir.dynBal.p_start; + thermalZone.ROM.volAir.dynBal.medium.p = thermalZone.ROM.volAir.dynBal.p_start; + + +Statistics + +Original Model + Number of components: 552 + Variables: 5264 + Constants: 145 (145 scalars) + Parameters: 1448 (5057 scalars) + Unknowns: 3671 (3887 scalars) + Differentiated variables: 10 scalars + Equations: 2524 + Nontrivial: 2332 +Translated Model + Constants: 1083 scalars + Free parameters: 3867 scalars + Parameter depending: 614 scalars + Continuous time states: 8 scalars + Time-varying variables: 1160 scalars + Alias variables: 2365 scalars + Number of mixed real/discrete systems of equations: 0 + Sizes of linear systems of equations: {4, 29, 29, 4} + Sizes after manipulation of the linear systems: {0, 4, 4, 0} + Sizes of nonlinear systems of equations: {1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1} + Sizes after manipulation of the nonlinear systems: {0, 1, 0, 1, 0, 1, 0, 1, 0, 1, 0, 1} + Number of numerical Jacobians: 0 + Initialization problem + Sizes of linear systems of equations: {32, 32} + Sizes after manipulation of the linear systems: {5, 5} + +Selected continuous time states +Statically selected continuous time states +thermalZone.ROM.extWallRC.thermCapExt[1].T +thermalZone.ROM.intWallRC.thermCapInt[1].T +thermalZone.ROM.volAir.dynBal.medium.Xi[1] +thermalZone.ROM.volAir.dynBal.U +thermalZoneMoistAir.ROM.extWallRC.thermCapExt[1].T +thermalZoneMoistAir.ROM.intWallRC.thermCapInt[1].T +thermalZoneMoistAir.ROM.volMoiAir.dynBal.medium.Xi[1] +thermalZoneMoistAir.ROM.volMoiAir.dynBal.U +Finished +Finished + = true + +Declaring variable: Boolean rScript ; + +savelog("AixLib.ThermalZones.ReducedOrder.Examples.ComparisonThermalZoneMoistAndDryAir.translation.log"); = true + + +rCheck = checkModel("AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case410"); +Check of AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case410 +The model has the same number of unknowns and equations: 1568 +The model has the same number of unknowns and equations +for the given numerical settings of parameters: 1568 +Check of AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case410 successful. +Declaring variable: Boolean rCheck ; + +Modelica.Utilities.Streams.print(" { \"file\" : \"AixLib/Resources/Scripts/Dymola/ThermalZones/HighOrder/Validation/ASHRAE140/Case410.mos\",", "AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case410.statistics.log"); +Modelica.Utilities.Streams.print(" \"model\" : \"AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case410\",", "AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case410.statistics.log"); +Modelica.Utilities.Streams.print(" \"check\" : {", "AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case410.statistics.log"); +Modelica.Utilities.Streams.print(" \"command\" : \"checkModel(\\\"AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case410\\\");\",", "AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case410.statistics.log"); +Modelica.Utilities.Streams.print(" \"result\" : " + String(rCheck), "AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case410.statistics.log"); +Modelica.Utilities.Streams.print(" },", "AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case410.statistics.log"); + + +rScript=RunScript("modelica://AixLib/Resources/Scripts/Dymola/ThermalZones/HighOrder/Validation/ASHRAE140/Case410.mos"); +simulateModel("AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case410", startTime=0, stopTime=31539600, outputInterval=1800, tolerance=1e-6, method="dassl", resultFile="AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case410"); +Translation of AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case410 +The DAE has 1568 scalar unknowns and 1568 scalar equations. + +Statistics + +Original Model + Number of components: 349 + Variables: 3047 + Constants: 41 (276 scalars) + Parameters: 1474 (2065 scalars) + Unknowns: 1532 (1568 scalars) + Differentiated variables: 25 scalars + Equations: 1252 + Nontrivial: 1041 +Translated Model + Constants: 771 scalars + Free parameters: 794 scalars + Parameter depending: 906 scalars + Outputs: 5 scalars + Continuous time states: 25 scalars + Time-varying variables: 461 scalars + Alias variables: 977 scalars + Number of mixed real/discrete systems of equations: 0 + Sizes of linear systems of equations: {4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 3, 4, 4, 4, 4} + Sizes after manipulation of the linear systems: {0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0} + Sizes of nonlinear systems of equations: {55} + Sizes after manipulation of the nonlinear systems: {13} + Number of numerical Jacobians: 0 + +Selected continuous time states +Statically selected continuous time states +idealHeaterCooler.pITempCool.PI.I.y +idealHeaterCooler.pITempHeat.PI.I.y +integrator2.y +integratorCool.y +integratorHeat.y +Room.airload.dynBal.m +Room.airload.dynBal.medium.Xi[1] +Room.airload.dynBal.U +Room.ceiling.Wall.simpleNLayer.cap[1].T +Room.ceiling.Wall.simpleNLayer.cap[2].T +Room.ceiling.Wall.simpleNLayer.cap[3].T +Room.floor.Wall.simpleNLayer.cap[1].T +Room.floor.Wall.simpleNLayer.cap[2].T +Room.wallEast.Wall.simpleNLayer.cap[1].T +Room.wallEast.Wall.simpleNLayer.cap[2].T +Room.wallEast.Wall.simpleNLayer.cap[3].T +Room.wallNorth.Wall.simpleNLayer.cap[1].T +Room.wallNorth.Wall.simpleNLayer.cap[2].T +Room.wallNorth.Wall.simpleNLayer.cap[3].T +Room.wallSouth.Wall.simpleNLayer.cap[1].T +Room.wallSouth.Wall.simpleNLayer.cap[2].T +Room.wallSouth.Wall.simpleNLayer.cap[3].T +Room.wallWest.Wall.simpleNLayer.cap[1].T +Room.wallWest.Wall.simpleNLayer.cap[2].T +Room.wallWest.Wall.simpleNLayer.cap[3].T +Finished +Finished + = true + +Declaring variable: Boolean rScript ; + +savelog("AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case410.translation.log"); = true + + +rCheck = checkModel("AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case240"); +Check of AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case240 +The model has the same number of unknowns and equations: 1568 +The model has the same number of unknowns and equations +for the given numerical settings of parameters: 1568 +Check of AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case240 successful. +Declaring variable: Boolean rCheck ; + +Modelica.Utilities.Streams.print(" { \"file\" : \"AixLib/Resources/Scripts/Dymola/ThermalZones/HighOrder/Validation/ASHRAE140/Case240.mos\",", "AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case240.statistics.log"); +Modelica.Utilities.Streams.print(" \"model\" : \"AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case240\",", "AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case240.statistics.log"); +Modelica.Utilities.Streams.print(" \"check\" : {", "AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case240.statistics.log"); +Modelica.Utilities.Streams.print(" \"command\" : \"checkModel(\\\"AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case240\\\");\",", "AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case240.statistics.log"); +Modelica.Utilities.Streams.print(" \"result\" : " + String(rCheck), "AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case240.statistics.log"); +Modelica.Utilities.Streams.print(" },", "AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case240.statistics.log"); + + +rScript=RunScript("modelica://AixLib/Resources/Scripts/Dymola/ThermalZones/HighOrder/Validation/ASHRAE140/Case240.mos"); +simulateModel("AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case240", startTime=0, stopTime=31539600, outputInterval=1800, tolerance=1e-6, method="dassl", resultFile="AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case240"); +Translation of AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case240 +The DAE has 1568 scalar unknowns and 1568 scalar equations. + +Statistics + +Original Model + Number of components: 349 + Variables: 3047 + Constants: 41 (276 scalars) + Parameters: 1474 (2065 scalars) + Unknowns: 1532 (1568 scalars) + Differentiated variables: 25 scalars + Equations: 1252 + Nontrivial: 1041 +Translated Model + Constants: 771 scalars + Free parameters: 794 scalars + Parameter depending: 906 scalars + Outputs: 5 scalars + Continuous time states: 25 scalars + Time-varying variables: 461 scalars + Alias variables: 977 scalars + Number of mixed real/discrete systems of equations: 0 + Sizes of linear systems of equations: {4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 3, 4, 4, 4, 4} + Sizes after manipulation of the linear systems: {0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0} + Sizes of nonlinear systems of equations: {55} + Sizes after manipulation of the nonlinear systems: {13} + Number of numerical Jacobians: 0 + +Selected continuous time states +Statically selected continuous time states +idealHeaterCooler.pITempCool.PI.I.y +idealHeaterCooler.pITempHeat.PI.I.y +integrator2.y +integratorCool.y +integratorHeat.y +Room.airload.dynBal.m +Room.airload.dynBal.medium.Xi[1] +Room.airload.dynBal.U +Room.ceiling.Wall.simpleNLayer.cap[1].T +Room.ceiling.Wall.simpleNLayer.cap[2].T +Room.ceiling.Wall.simpleNLayer.cap[3].T +Room.floor.Wall.simpleNLayer.cap[1].T +Room.floor.Wall.simpleNLayer.cap[2].T +Room.wallEast.Wall.simpleNLayer.cap[1].T +Room.wallEast.Wall.simpleNLayer.cap[2].T +Room.wallEast.Wall.simpleNLayer.cap[3].T +Room.wallNorth.Wall.simpleNLayer.cap[1].T +Room.wallNorth.Wall.simpleNLayer.cap[2].T +Room.wallNorth.Wall.simpleNLayer.cap[3].T +Room.wallSouth.Wall.simpleNLayer.cap[1].T +Room.wallSouth.Wall.simpleNLayer.cap[2].T +Room.wallSouth.Wall.simpleNLayer.cap[3].T +Room.wallWest.Wall.simpleNLayer.cap[1].T +Room.wallWest.Wall.simpleNLayer.cap[2].T +Room.wallWest.Wall.simpleNLayer.cap[3].T +Finished +Finished + = true + +Declaring variable: Boolean rScript ; + +savelog("AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case240.translation.log"); = true + + +rCheck = checkModel("AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case270"); +Check of AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case270 +The model has the same number of unknowns and equations: 1585 +The model has the same number of unknowns and equations +for the given numerical settings of parameters: 1585 +Check of AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case270 successful. +Declaring variable: Boolean rCheck ; + +Modelica.Utilities.Streams.print(" { \"file\" : \"AixLib/Resources/Scripts/Dymola/ThermalZones/HighOrder/Validation/ASHRAE140/Case270.mos\",", "AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case270.statistics.log"); +Modelica.Utilities.Streams.print(" \"model\" : \"AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case270\",", "AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case270.statistics.log"); +Modelica.Utilities.Streams.print(" \"check\" : {", "AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case270.statistics.log"); +Modelica.Utilities.Streams.print(" \"command\" : \"checkModel(\\\"AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case270\\\");\",", "AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case270.statistics.log"); +Modelica.Utilities.Streams.print(" \"result\" : " + String(rCheck), "AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case270.statistics.log"); +Modelica.Utilities.Streams.print(" },", "AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case270.statistics.log"); + + +rScript=RunScript("modelica://AixLib/Resources/Scripts/Dymola/ThermalZones/HighOrder/Validation/ASHRAE140/Case270.mos"); +simulateModel("AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case270", startTime=0, stopTime=31539600, outputInterval=1800, tolerance=1e-6, method="dassl", resultFile="AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case270"); +Translation of AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case270 +The DAE has 1585 scalar unknowns and 1585 scalar equations. + +Statistics + +Original Model + Number of components: 352 + Variables: 3082 + Constants: 41 (276 scalars) + Parameters: 1493 (2159 scalars) + Unknowns: 1548 (1585 scalars) + Differentiated variables: 25 scalars + Equations: 1257 + Nontrivial: 1045 +Translated Model + Constants: 780 scalars + Free parameters: 876 scalars + Parameter depending: 909 scalars + Outputs: 5 scalars + Continuous time states: 25 scalars + Time-varying variables: 474 scalars + Alias variables: 981 scalars + Number of mixed real/discrete systems of equations: 0 + Sizes of linear systems of equations: {4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 3, 4, 4, 4, 4} + Sizes after manipulation of the linear systems: {0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0} + Sizes of nonlinear systems of equations: {55} + Sizes after manipulation of the nonlinear systems: {13} + Number of numerical Jacobians: 0 + +Selected continuous time states +Statically selected continuous time states +idealHeaterCooler.pITempCool.PI.I.y +idealHeaterCooler.pITempHeat.PI.I.y +integrator2.y +integratorCool.y +integratorHeat.y +Room.airload.dynBal.m +Room.airload.dynBal.medium.Xi[1] +Room.airload.dynBal.U +Room.ceiling.Wall.simpleNLayer.cap[1].T +Room.ceiling.Wall.simpleNLayer.cap[2].T +Room.ceiling.Wall.simpleNLayer.cap[3].T +Room.floor.Wall.simpleNLayer.cap[1].T +Room.floor.Wall.simpleNLayer.cap[2].T +Room.wallEast.Wall.simpleNLayer.cap[1].T +Room.wallEast.Wall.simpleNLayer.cap[2].T +Room.wallEast.Wall.simpleNLayer.cap[3].T +Room.wallNorth.Wall.simpleNLayer.cap[1].T +Room.wallNorth.Wall.simpleNLayer.cap[2].T +Room.wallNorth.Wall.simpleNLayer.cap[3].T +Room.wallSouth.Wall.simpleNLayer.cap[1].T +Room.wallSouth.Wall.simpleNLayer.cap[2].T +Room.wallSouth.Wall.simpleNLayer.cap[3].T +Room.wallWest.Wall.simpleNLayer.cap[1].T +Room.wallWest.Wall.simpleNLayer.cap[2].T +Room.wallWest.Wall.simpleNLayer.cap[3].T +Finished +Finished + = true + +Declaring variable: Boolean rScript ; + +savelog("AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case270.translation.log"); = true + + +rCheck = checkModel("AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case220"); +Check of AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case220 +The model has the same number of unknowns and equations: 1568 +The model has the same number of unknowns and equations +for the given numerical settings of parameters: 1568 +Check of AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case220 successful. +Declaring variable: Boolean rCheck ; + +Modelica.Utilities.Streams.print(" { \"file\" : \"AixLib/Resources/Scripts/Dymola/ThermalZones/HighOrder/Validation/ASHRAE140/Case220.mos\",", "AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case220.statistics.log"); +Modelica.Utilities.Streams.print(" \"model\" : \"AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case220\",", "AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case220.statistics.log"); +Modelica.Utilities.Streams.print(" \"check\" : {", "AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case220.statistics.log"); +Modelica.Utilities.Streams.print(" \"command\" : \"checkModel(\\\"AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case220\\\");\",", "AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case220.statistics.log"); +Modelica.Utilities.Streams.print(" \"result\" : " + String(rCheck), "AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case220.statistics.log"); +Modelica.Utilities.Streams.print(" },", "AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case220.statistics.log"); + + +rScript=RunScript("modelica://AixLib/Resources/Scripts/Dymola/ThermalZones/HighOrder/Validation/ASHRAE140/Case220.mos"); +simulateModel("AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case220", startTime=0, stopTime=31539600, outputInterval=1800, tolerance=1e-6, method="dassl", resultFile="AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case220"); +Translation of AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case220 +The DAE has 1568 scalar unknowns and 1568 scalar equations. + +Statistics + +Original Model + Number of components: 349 + Variables: 3047 + Constants: 41 (276 scalars) + Parameters: 1474 (2065 scalars) + Unknowns: 1532 (1568 scalars) + Differentiated variables: 25 scalars + Equations: 1252 + Nontrivial: 1041 +Translated Model + Constants: 771 scalars + Free parameters: 794 scalars + Parameter depending: 906 scalars + Outputs: 5 scalars + Continuous time states: 25 scalars + Time-varying variables: 461 scalars + Alias variables: 977 scalars + Number of mixed real/discrete systems of equations: 0 + Sizes of linear systems of equations: {4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 3, 4, 4, 4, 4} + Sizes after manipulation of the linear systems: {0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0} + Sizes of nonlinear systems of equations: {55} + Sizes after manipulation of the nonlinear systems: {13} + Number of numerical Jacobians: 0 + +Selected continuous time states +Statically selected continuous time states +idealHeaterCooler.pITempCool.PI.I.y +idealHeaterCooler.pITempHeat.PI.I.y +integrator2.y +integratorCool.y +integratorHeat.y +Room.airload.dynBal.m +Room.airload.dynBal.medium.Xi[1] +Room.airload.dynBal.U +Room.ceiling.Wall.simpleNLayer.cap[1].T +Room.ceiling.Wall.simpleNLayer.cap[2].T +Room.ceiling.Wall.simpleNLayer.cap[3].T +Room.floor.Wall.simpleNLayer.cap[1].T +Room.floor.Wall.simpleNLayer.cap[2].T +Room.wallEast.Wall.simpleNLayer.cap[1].T +Room.wallEast.Wall.simpleNLayer.cap[2].T +Room.wallEast.Wall.simpleNLayer.cap[3].T +Room.wallNorth.Wall.simpleNLayer.cap[1].T +Room.wallNorth.Wall.simpleNLayer.cap[2].T +Room.wallNorth.Wall.simpleNLayer.cap[3].T +Room.wallSouth.Wall.simpleNLayer.cap[1].T +Room.wallSouth.Wall.simpleNLayer.cap[2].T +Room.wallSouth.Wall.simpleNLayer.cap[3].T +Room.wallWest.Wall.simpleNLayer.cap[1].T +Room.wallWest.Wall.simpleNLayer.cap[2].T +Room.wallWest.Wall.simpleNLayer.cap[3].T +Finished +Finished + = true + +Declaring variable: Boolean rScript ; + +savelog("AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case220.translation.log"); = true + + +rCheck = checkModel("AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case950"); +Check of AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case950 +The model has the same number of unknowns and equations: 1522 +The model has the same number of unknowns and equations +for the given numerical settings of parameters: 1522 +Check of AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case950 successful. +Declaring variable: Boolean rCheck ; + +Modelica.Utilities.Streams.print(" { \"file\" : \"AixLib/Resources/Scripts/Dymola/ThermalZones/HighOrder/Validation/ASHRAE140/Case950.mos\",", "AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case950.statistics.log"); +Modelica.Utilities.Streams.print(" \"model\" : \"AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case950\",", "AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case950.statistics.log"); +Modelica.Utilities.Streams.print(" \"check\" : {", "AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case950.statistics.log"); +Modelica.Utilities.Streams.print(" \"command\" : \"checkModel(\\\"AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case950\\\");\",", "AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case950.statistics.log"); +Modelica.Utilities.Streams.print(" \"result\" : " + String(rCheck), "AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case950.statistics.log"); +Modelica.Utilities.Streams.print(" },", "AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case950.statistics.log"); + + +rScript=RunScript("modelica://AixLib/Resources/Scripts/Dymola/ThermalZones/HighOrder/Validation/ASHRAE140/Case950.mos"); +simulateModel("AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case950", startTime=0, stopTime=31539600, outputInterval=1800, tolerance=1e-6, method="dassl", resultFile="AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case950"); +Translation of AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case950 +The DAE has 1522 scalar unknowns and 1522 scalar equations. + +Statistics + +Original Model + Number of components: 334 + Variables: 3002 + Constants: 40 (275 scalars) + Parameters: 1477 (2187 scalars) + Unknowns: 1485 (1522 scalars) + Differentiated variables: 24 scalars + Equations: 1198 + Nontrivial: 992 +Translated Model + Constants: 777 scalars + Free parameters: 881 scalars + Parameter depending: 926 scalars + Outputs: 5 scalars + Continuous time states: 24 scalars + Time-varying variables: 464 scalars + Alias variables: 936 scalars + Number of mixed real/discrete systems of equations: 0 + Sizes of linear systems of equations: {4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 3, 4, 4, 4, 4} + Sizes after manipulation of the linear systems: {0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0} + Sizes of nonlinear systems of equations: {55} + Sizes after manipulation of the nonlinear systems: {13} + Number of numerical Jacobians: 0 + +Selected continuous time states +Statically selected continuous time states +idealHeaterCooler.pITempCool.PI.I.y +integrator2.y +integratorCool.y +integratorHeat.y +Room.airload.dynBal.m +Room.airload.dynBal.medium.Xi[1] +Room.airload.dynBal.U +Room.ceiling.Wall.simpleNLayer.cap[1].T +Room.ceiling.Wall.simpleNLayer.cap[2].T +Room.ceiling.Wall.simpleNLayer.cap[3].T +Room.floor.Wall.simpleNLayer.cap[1].T +Room.floor.Wall.simpleNLayer.cap[2].T +Room.wallEast.Wall.simpleNLayer.cap[1].T +Room.wallEast.Wall.simpleNLayer.cap[2].T +Room.wallEast.Wall.simpleNLayer.cap[3].T +Room.wallNorth.Wall.simpleNLayer.cap[1].T +Room.wallNorth.Wall.simpleNLayer.cap[2].T +Room.wallNorth.Wall.simpleNLayer.cap[3].T +Room.wallSouth.Wall.simpleNLayer.cap[1].T +Room.wallSouth.Wall.simpleNLayer.cap[2].T +Room.wallSouth.Wall.simpleNLayer.cap[3].T +Room.wallWest.Wall.simpleNLayer.cap[1].T +Room.wallWest.Wall.simpleNLayer.cap[2].T +Room.wallWest.Wall.simpleNLayer.cap[3].T +Finished +Finished + = true + +Declaring variable: Boolean rScript ; + +savelog("AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case950.translation.log"); = true + + +rCheck = checkModel("AixLib.ThermalZones.ReducedOrder.Examples.MultizoneMoistAirCO2EquippedSwimmingFacility"); +Check of AixLib.ThermalZones.ReducedOrder.Examples.MultizoneMoistAirCO2EquippedSwimmingFacility +The model has the same number of unknowns and equations: 13468 +The model has the same number of unknowns and equations +for the given numerical settings of parameters: 13468 +Check of AixLib.ThermalZones.ReducedOrder.Examples.MultizoneMoistAirCO2EquippedSwimmingFacility successful. +Declaring variable: Boolean rCheck ; + +Modelica.Utilities.Streams.print(" { \"file\" : \"AixLib/Resources/Scripts/Dymola/ThermalZones/ReducedOrder/Examples/MultizoneMoistAirCO2EquippedSwimmingFacility.mos\",", "AixLib.ThermalZones.ReducedOrder.Examples.MultizoneMoistAirCO2EquippedSwimmingFacility.statistics.log"); +Modelica.Utilities.Streams.print(" \"model\" : \"AixLib.ThermalZones.ReducedOrder.Examples.MultizoneMoistAirCO2EquippedSwimmingFacility\",", "AixLib.ThermalZones.ReducedOrder.Examples.MultizoneMoistAirCO2EquippedSwimmingFacility.statistics.log"); +Modelica.Utilities.Streams.print(" \"check\" : {", "AixLib.ThermalZones.ReducedOrder.Examples.MultizoneMoistAirCO2EquippedSwimmingFacility.statistics.log"); +Modelica.Utilities.Streams.print(" \"command\" : \"checkModel(\\\"AixLib.ThermalZones.ReducedOrder.Examples.MultizoneMoistAirCO2EquippedSwimmingFacility\\\");\",", "AixLib.ThermalZones.ReducedOrder.Examples.MultizoneMoistAirCO2EquippedSwimmingFacility.statistics.log"); +Modelica.Utilities.Streams.print(" \"result\" : " + String(rCheck), "AixLib.ThermalZones.ReducedOrder.Examples.MultizoneMoistAirCO2EquippedSwimmingFacility.statistics.log"); +Modelica.Utilities.Streams.print(" },", "AixLib.ThermalZones.ReducedOrder.Examples.MultizoneMoistAirCO2EquippedSwimmingFacility.statistics.log"); + + +rScript=RunScript("modelica://AixLib/Resources/Scripts/Dymola/ThermalZones/ReducedOrder/Examples/MultizoneMoistAirCO2EquippedSwimmingFacility.mos"); +simulateModel("AixLib.ThermalZones.ReducedOrder.Examples.MultizoneMoistAirCO2EquippedSwimmingFacility", tolerance=1e-6, stopTime=3.1536e+007, numberOfIntervals=0, outputInterval=3600, method="CVode", resultFile="AixLib.ThermalZones.ReducedOrder.Examples.MultizoneMoistAirCO2EquippedSwimmingFacility"); +Translation of AixLib.ThermalZones.ReducedOrder.Examples.MultizoneMoistAirCO2EquippedSwimmingFacility +The DAE has 13468 scalar unknowns and 13468 scalar equations. +Redundant consistent initial conditions. +Removed the following equations which are redundant and consistent: + if (multizone.zone[1].airFlowMoistureToROM.AirLay.dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.FixedInitial) then + if (multizone.zone[1].airFlowMoistureToROM.AirLay.dynBal.initialize_p) then + multizone.zone[1].airFlowMoistureToROM.AirLay.dynBal.medium.p = multizone.zone[1].airFlowMoistureToROM.AirLay.dynBal.p_start; + end if; + else + if (multizone.zone[1].airFlowMoistureToROM.AirLay.dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then + if (multizone.zone[1].airFlowMoistureToROM.AirLay.dynBal.initialize_p) then + der(multizone.zone[1].airFlowMoistureToROM.AirLay.dynBal.medium.p) = 0; + end if; + end if; + end if; + if (multizone.zone[1].airFlowMoistureToROM.sou.vol.dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.FixedInitial) then + if (multizone.zone[1].airFlowMoistureToROM.sou.vol.dynBal.initialize_p) then + multizone.zone[1].airFlowMoistureToROM.sou.vol.dynBal.medium.p = multizone.zone[1].airFlowMoistureToROM.sou.vol.dynBal.p_start; + end if; + else + if (multizone.zone[1].airFlowMoistureToROM.sou.vol.dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then + if (multizone.zone[1].airFlowMoistureToROM.sou.vol.dynBal.initialize_p) then + der(multizone.zone[1].airFlowMoistureToROM.sou.vol.dynBal.medium.p) = 0; + end if; + end if; + end if; + +The redundancies involve +initial equations: + multizone.zone[1].ROM.volMoiAir.dynBal.medium.p = 101325.0; + multizone.zone[1].airFlowMoistureToROM.AirLay.dynBal.medium.p = 101325.0; + multizone.zone[1].airFlowMoistureToROM.sou.vol.dynBal.medium.p = 101325.0; + +active start values: + multizone.zone[1].ROM.ports[1].p = 101325; + + +Statistics + +Original Model + Number of components: 2234 + Variables: 22367 + Constants: 540 (540 scalars) + Parameters: 8721 (10838 scalars) + Unknowns: 13104 (13615 scalars) + Differentiated variables: 94 scalars + Equations: 9467 + Nontrivial: 8430 +Translated Model + Constants: 13099 scalars + Parameter depending: 215 scalars + Continuous time states: 86 scalars + Time-varying variables: 3976 scalars + Alias variables: 7703 scalars + Number of mixed real/discrete systems of equations: 0 + Sizes of linear systems of equations: {4, 26, 13, 13, 4, 4, 26, 13, 13, 46, 4, 4, 46, 4, 4, 45, 4, 4, 4, 45, 4, 46, 4, 4} + Sizes after manipulation of the linear systems: {0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0} + Sizes of nonlinear systems of equations: {56, 6, 6, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1} + Sizes after manipulation of the nonlinear systems: {6, 1, 1, 0, 0, 1, 0, 1, 0, 1, 1, 1, 0, 1, 0, 1, 0, 1, 0, 1, 0, 1, 0, 1, 0, 1, 0, 1, 0, 1, 0, 1, 0, 1, 0, 1, 0, 1, 0, 1, 0, 1} + Number of numerical Jacobians: 0 + Initialization problem + Sizes of linear systems of equations: {57, 57, 56, 56, 57} + Sizes after manipulation of the linear systems: {0, 0, 0, 0, 0} + Sizes of nonlinear systems of equations: {1, 1, 67, 1, 1} + Sizes after manipulation of the nonlinear systems: {0, 0, 9, 1, 1} + Number of numerical Jacobians: 0 + +Settings +Evaluate = true +Selected continuous time states +Statically selected continuous time states +multizone.zone[1].airFlowMoistureToROM.AirLay.dynBal.mC[1] +multizone.zone[1].airFlowMoistureToROM.AirLay.dynBal.medium.Xi[1] +multizone.zone[1].airFlowMoistureToROM.AirLay.dynBal.U +multizone.zone[1].airFlowMoistureToROM.sou.filter.s[1] +multizone.zone[1].airFlowMoistureToROM.sou.filter.s[2] +multizone.zone[1].airFlowMoistureToROM.sou.vol.dynBal.m +multizone.zone[1].airFlowMoistureToROM.sou.vol.dynBal.mC[1] +multizone.zone[1].airFlowMoistureToROM.sou.vol.dynBal.medium.Xi[1] +multizone.zone[1].airFlowMoistureToROM.sou.vol.dynBal.U +multizone.zone[1].heaterCooler.pITempHeat.PI.I.y +multizone.zone[1].indoorSwimmingPool[1].cirPump.filter.s[1] +multizone.zone[1].indoorSwimmingPool[1].cirPump.filter.s[2] +multizone.zone[1].indoorSwimmingPool[1].cirPump.vol.dynBal.U +multizone.zone[1].indoorSwimmingPool[1].PI.I.y +multizone.zone[1].indoorSwimmingPool[1].poolSto.dynBal.U +multizone.zone[1].indoorSwimmingPool[1].poolWat.dynBal.U +multizone.zone[1].indoorSwimmingPool[2].cirPump.filter.s[1] +multizone.zone[1].indoorSwimmingPool[2].cirPump.filter.s[2] +multizone.zone[1].indoorSwimmingPool[2].cirPump.vol.dynBal.U +multizone.zone[1].indoorSwimmingPool[2].PI.I.y +multizone.zone[1].indoorSwimmingPool[2].poolSto.dynBal.U +multizone.zone[1].indoorSwimmingPool[2].poolWat.dynBal.U +multizone.zone[1].ROM.extWallRC.thermCapExt[1].T +multizone.zone[1].ROM.floorRC.thermCapExt[1].T +multizone.zone[1].ROM.intWallRC.thermCapInt[1].T +multizone.zone[1].ROM.roofRC.thermCapExt[1].T +multizone.zone[1].ROM.volMoiAir.dynBal.mC[1] +multizone.zone[1].ROM.volMoiAir.dynBal.medium.Xi[1] +multizone.zone[1].ROM.volMoiAir.dynBal.U +multizone.zone[1].ventCont.dEMA.ExpAVG.x[1] +multizone.zone[1].ventCont.dEMA.ExpAVG1.x[1] +multizone.zone[2].heaterCooler.pITempHeat.PI.I.y +multizone.zone[2].ROM.extWallRC.thermCapExt[1].T +multizone.zone[2].ROM.floorRC.thermCapExt[1].T +multizone.zone[2].ROM.intWallRC.thermCapInt[1].T +multizone.zone[2].ROM.roofRC.thermCapExt[1].T +multizone.zone[2].ROM.volMoiAir.dynBal.m +multizone.zone[2].ROM.volMoiAir.dynBal.mC[1] +multizone.zone[2].ROM.volMoiAir.dynBal.medium.Xi[1] +multizone.zone[2].ROM.volMoiAir.dynBal.U +multizone.zone[2].ventCont.dEMA.ExpAVG.x[1] +multizone.zone[2].ventCont.dEMA.ExpAVG1.x[1] +multizone.zone[3].heaterCooler.pITempHeat.PI.I.y +multizone.zone[3].ROM.extWallRC.thermCapExt[1].T +multizone.zone[3].ROM.floorRC.thermCapExt[1].T +multizone.zone[3].ROM.intWallRC.thermCapInt[1].T +multizone.zone[3].ROM.roofRC.thermCapExt[1].T +multizone.zone[3].ROM.volMoiAir.dynBal.m +multizone.zone[3].ROM.volMoiAir.dynBal.mC[1] +multizone.zone[3].ROM.volMoiAir.dynBal.medium.Xi[1] +multizone.zone[3].ROM.volMoiAir.dynBal.U +multizone.zone[3].ventCont.dEMA.ExpAVG.x[1] +multizone.zone[3].ventCont.dEMA.ExpAVG1.x[1] +multizone.zone[4].heaterCooler.pITempHeat.PI.I.y +multizone.zone[4].ROM.extWallRC.thermCapExt[1].T +multizone.zone[4].ROM.floorRC.thermCapExt[1].T +multizone.zone[4].ROM.intWallRC.thermCapInt[1].T +multizone.zone[4].ROM.roofRC.thermCapExt[1].T +multizone.zone[4].ROM.volMoiAir.dynBal.m +multizone.zone[4].ROM.volMoiAir.dynBal.mC[1] +multizone.zone[4].ROM.volMoiAir.dynBal.medium.Xi[1] +multizone.zone[4].ROM.volMoiAir.dynBal.U +multizone.zone[4].ventCont.dEMA.ExpAVG.x[1] +multizone.zone[4].ventCont.dEMA.ExpAVG1.x[1] +multizone.zone[5].heaterCooler.pITempHeat.PI.I.y +multizone.zone[5].ROM.extWallRC.thermCapExt[1].T +multizone.zone[5].ROM.floorRC.thermCapExt[1].T +multizone.zone[5].ROM.intWallRC.thermCapInt[1].T +multizone.zone[5].ROM.roofRC.thermCapExt[1].T +multizone.zone[5].ROM.volMoiAir.dynBal.m +multizone.zone[5].ROM.volMoiAir.dynBal.mC[1] +multizone.zone[5].ROM.volMoiAir.dynBal.medium.Xi[1] +multizone.zone[5].ROM.volMoiAir.dynBal.U +multizone.zone[5].ventCont.dEMA.ExpAVG.x[1] +multizone.zone[5].ventCont.dEMA.ExpAVG1.x[1] +multizone.zone[6].heaterCooler.pITempHeat.PI.I.y +multizone.zone[6].ROM.extWallRC.thermCapExt[1].T +multizone.zone[6].ROM.floorRC.thermCapExt[1].T +multizone.zone[6].ROM.intWallRC.thermCapInt[1].T +multizone.zone[6].ROM.roofRC.thermCapExt[1].T +multizone.zone[6].ROM.volMoiAir.dynBal.m +multizone.zone[6].ROM.volMoiAir.dynBal.mC[1] +multizone.zone[6].ROM.volMoiAir.dynBal.medium.Xi[1] +multizone.zone[6].ROM.volMoiAir.dynBal.U +multizone.zone[6].ventCont.dEMA.ExpAVG.x[1] +multizone.zone[6].ventCont.dEMA.ExpAVG1.x[1] +Finished +Finished + = true + +Declaring variable: Boolean rScript ; + +savelog("AixLib.ThermalZones.ReducedOrder.Examples.MultizoneMoistAirCO2EquippedSwimmingFacility.translation.log"); = true + + +rCheck = checkModel("AixLib.ThermalZones.HighOrder.Examples.ASHREA140.CompareDynamicAndStaticSolarFrac_Case270"); +Check of AixLib.ThermalZones.HighOrder.Examples.ASHREA140.CompareDynamicAndStaticSolarFrac_Case270 +The model has the same number of unknowns and equations: 2803 +The model has the same number of unknowns and equations +for the given numerical settings of parameters: 2803 +Check of AixLib.ThermalZones.HighOrder.Examples.ASHREA140.CompareDynamicAndStaticSolarFrac_Case270 successful. +Declaring variable: Boolean rCheck ; + +Modelica.Utilities.Streams.print(" { \"file\" : \"AixLib/Resources/Scripts/Dymola/ThermalZones/HighOrder/Examples/ASHREA140/CompareDynamicAndStaticSolarFrac_Case270.mos\",", "AixLib.ThermalZones.HighOrder.Examples.ASHREA140.CompareDynamicAndStaticSolarFrac_Case270.statistics.log"); +Modelica.Utilities.Streams.print(" \"model\" : \"AixLib.ThermalZones.HighOrder.Examples.ASHREA140.CompareDynamicAndStaticSolarFrac_Case270\",", "AixLib.ThermalZones.HighOrder.Examples.ASHREA140.CompareDynamicAndStaticSolarFrac_Case270.statistics.log"); +Modelica.Utilities.Streams.print(" \"check\" : {", "AixLib.ThermalZones.HighOrder.Examples.ASHREA140.CompareDynamicAndStaticSolarFrac_Case270.statistics.log"); +Modelica.Utilities.Streams.print(" \"command\" : \"checkModel(\\\"AixLib.ThermalZones.HighOrder.Examples.ASHREA140.CompareDynamicAndStaticSolarFrac_Case270\\\");\",", "AixLib.ThermalZones.HighOrder.Examples.ASHREA140.CompareDynamicAndStaticSolarFrac_Case270.statistics.log"); +Modelica.Utilities.Streams.print(" \"result\" : " + String(rCheck), "AixLib.ThermalZones.HighOrder.Examples.ASHREA140.CompareDynamicAndStaticSolarFrac_Case270.statistics.log"); +Modelica.Utilities.Streams.print(" },", "AixLib.ThermalZones.HighOrder.Examples.ASHREA140.CompareDynamicAndStaticSolarFrac_Case270.statistics.log"); + + +rScript=RunScript("modelica://AixLib/Resources/Scripts/Dymola/ThermalZones/HighOrder/Examples/ASHREA140/CompareDynamicAndStaticSolarFrac_Case270.mos"); +simulateModel("AixLib.ThermalZones.HighOrder.Examples.ASHREA140.CompareDynamicAndStaticSolarFrac_Case270", startTime=0, stopTime=86400, outputInterval=3600, tolerance=1e-6, method="dassl", resultFile="AixLib.ThermalZones.HighOrder.Examples.ASHREA140.CompareDynamicAndStaticSolarFrac_Case270"); +Translation of AixLib.ThermalZones.HighOrder.Examples.ASHREA140.CompareDynamicAndStaticSolarFrac_Case270 +The DAE has 2803 scalar unknowns and 2803 scalar equations. + +Statistics + +Original Model + Number of components: 649 + Variables: 5512 + Constants: 52 (287 scalars) + Parameters: 2703 (3593 scalars) + Unknowns: 2757 (2803 scalars) + Differentiated variables: 47 scalars + Equations: 2206 + Nontrivial: 1843 +Translated Model + Constants: 1151 scalars + Free parameters: 1302 scalars + Parameter depending: 1670 scalars + Outputs: 5 scalars + Continuous time states: 47 scalars + Time-varying variables: 742 scalars + Alias variables: 1818 scalars + Number of mixed real/discrete systems of equations: 0 + Sizes of linear systems of equations: {4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 3, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 3, 4, 4, 4, 4, 4, 4, 4} + Sizes after manipulation of the linear systems: {0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0} + Sizes of nonlinear systems of equations: {55, 55} + Sizes after manipulation of the nonlinear systems: {13, 13} + Number of numerical Jacobians: 0 + +Selected continuous time states +Statically selected continuous time states +idealHeaterCooler.pITempCool.PI.I.y +idealHeaterCooler.pITempHeat.PI.I.y +idealHeaterCooler_dyn.pITempCool.PI.I.y +idealHeaterCooler_dyn.pITempHeat.PI.I.y +integrator2.y +integratorCool.y +integratorHeat.y +Room.airload.dynBal.m +Room.airload.dynBal.medium.Xi[1] +Room.airload.dynBal.U +Room.ceiling.Wall.simpleNLayer.cap[1].T +Room.ceiling.Wall.simpleNLayer.cap[2].T +Room.ceiling.Wall.simpleNLayer.cap[3].T +Room.floor.Wall.simpleNLayer.cap[1].T +Room.floor.Wall.simpleNLayer.cap[2].T +Room.wallEast.Wall.simpleNLayer.cap[1].T +Room.wallEast.Wall.simpleNLayer.cap[2].T +Room.wallEast.Wall.simpleNLayer.cap[3].T +Room.wallNorth.Wall.simpleNLayer.cap[1].T +Room.wallNorth.Wall.simpleNLayer.cap[2].T +Room.wallNorth.Wall.simpleNLayer.cap[3].T +Room.wallSouth.Wall.simpleNLayer.cap[1].T +Room.wallSouth.Wall.simpleNLayer.cap[2].T +Room.wallSouth.Wall.simpleNLayer.cap[3].T +Room.wallWest.Wall.simpleNLayer.cap[1].T +Room.wallWest.Wall.simpleNLayer.cap[2].T +Room.wallWest.Wall.simpleNLayer.cap[3].T +Room_dyn.airload.dynBal.m +Room_dyn.airload.dynBal.medium.Xi[1] +Room_dyn.airload.dynBal.U +Room_dyn.ceiling.Wall.simpleNLayer.cap[1].T +Room_dyn.ceiling.Wall.simpleNLayer.cap[2].T +Room_dyn.ceiling.Wall.simpleNLayer.cap[3].T +Room_dyn.floor.Wall.simpleNLayer.cap[1].T +Room_dyn.floor.Wall.simpleNLayer.cap[2].T +Room_dyn.wallEast.Wall.simpleNLayer.cap[1].T +Room_dyn.wallEast.Wall.simpleNLayer.cap[2].T +Room_dyn.wallEast.Wall.simpleNLayer.cap[3].T +Room_dyn.wallNorth.Wall.simpleNLayer.cap[1].T +Room_dyn.wallNorth.Wall.simpleNLayer.cap[2].T +Room_dyn.wallNorth.Wall.simpleNLayer.cap[3].T +Room_dyn.wallSouth.Wall.simpleNLayer.cap[1].T +Room_dyn.wallSouth.Wall.simpleNLayer.cap[2].T +Room_dyn.wallSouth.Wall.simpleNLayer.cap[3].T +Room_dyn.wallWest.Wall.simpleNLayer.cap[1].T +Room_dyn.wallWest.Wall.simpleNLayer.cap[2].T +Room_dyn.wallWest.Wall.simpleNLayer.cap[3].T +Finished +Finished + = true + +Declaring variable: Boolean rScript ; + +savelog("AixLib.ThermalZones.HighOrder.Examples.ASHREA140.CompareDynamicAndStaticSolarFrac_Case270.translation.log"); = true + + +rCheck = checkModel("AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case900"); +Check of AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case900 +The model has the same number of unknowns and equations: 1585 +The model has the same number of unknowns and equations +for the given numerical settings of parameters: 1585 +Check of AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case900 successful. +Declaring variable: Boolean rCheck ; + +Modelica.Utilities.Streams.print(" { \"file\" : \"AixLib/Resources/Scripts/Dymola/ThermalZones/HighOrder/Validation/ASHRAE140/Case900.mos\",", "AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case900.statistics.log"); +Modelica.Utilities.Streams.print(" \"model\" : \"AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case900\",", "AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case900.statistics.log"); +Modelica.Utilities.Streams.print(" \"check\" : {", "AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case900.statistics.log"); +Modelica.Utilities.Streams.print(" \"command\" : \"checkModel(\\\"AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case900\\\");\",", "AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case900.statistics.log"); +Modelica.Utilities.Streams.print(" \"result\" : " + String(rCheck), "AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case900.statistics.log"); +Modelica.Utilities.Streams.print(" },", "AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case900.statistics.log"); + + +rScript=RunScript("modelica://AixLib/Resources/Scripts/Dymola/ThermalZones/HighOrder/Validation/ASHRAE140/Case900.mos"); +simulateModel("AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case900", startTime=0, stopTime=31539600, outputInterval=1800, tolerance=1e-6, method="dassl", resultFile="AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case900"); +Translation of AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case900 +The DAE has 1585 scalar unknowns and 1585 scalar equations. + +Statistics + +Original Model + Number of components: 352 + Variables: 3082 + Constants: 41 (276 scalars) + Parameters: 1493 (2159 scalars) + Unknowns: 1548 (1585 scalars) + Differentiated variables: 25 scalars + Equations: 1257 + Nontrivial: 1045 +Translated Model + Constants: 780 scalars + Free parameters: 876 scalars + Parameter depending: 909 scalars + Outputs: 5 scalars + Continuous time states: 25 scalars + Time-varying variables: 474 scalars + Alias variables: 981 scalars + Number of mixed real/discrete systems of equations: 0 + Sizes of linear systems of equations: {4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 3, 4, 4, 4, 4} + Sizes after manipulation of the linear systems: {0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0} + Sizes of nonlinear systems of equations: {55} + Sizes after manipulation of the nonlinear systems: {13} + Number of numerical Jacobians: 0 + +Selected continuous time states +Statically selected continuous time states +idealHeaterCooler.pITempCool.PI.I.y +idealHeaterCooler.pITempHeat.PI.I.y +integrator2.y +integratorCool.y +integratorHeat.y +Room.airload.dynBal.m +Room.airload.dynBal.medium.Xi[1] +Room.airload.dynBal.U +Room.ceiling.Wall.simpleNLayer.cap[1].T +Room.ceiling.Wall.simpleNLayer.cap[2].T +Room.ceiling.Wall.simpleNLayer.cap[3].T +Room.floor.Wall.simpleNLayer.cap[1].T +Room.floor.Wall.simpleNLayer.cap[2].T +Room.wallEast.Wall.simpleNLayer.cap[1].T +Room.wallEast.Wall.simpleNLayer.cap[2].T +Room.wallEast.Wall.simpleNLayer.cap[3].T +Room.wallNorth.Wall.simpleNLayer.cap[1].T +Room.wallNorth.Wall.simpleNLayer.cap[2].T +Room.wallNorth.Wall.simpleNLayer.cap[3].T +Room.wallSouth.Wall.simpleNLayer.cap[1].T +Room.wallSouth.Wall.simpleNLayer.cap[2].T +Room.wallSouth.Wall.simpleNLayer.cap[3].T +Room.wallWest.Wall.simpleNLayer.cap[1].T +Room.wallWest.Wall.simpleNLayer.cap[2].T +Room.wallWest.Wall.simpleNLayer.cap[3].T +Finished +Finished + = true + +Declaring variable: Boolean rScript ; + +savelog("AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case900.translation.log"); = true + + +rCheck = checkModel("AixLib.ThermalZones.ReducedOrder.Examples.MultizonePartlyCooled"); +Check of AixLib.ThermalZones.ReducedOrder.Examples.MultizonePartlyCooled +The model has the same number of unknowns and equations: 9997 +The model has the same number of unknowns and equations +for the given numerical settings of parameters: 9997 +Check of AixLib.ThermalZones.ReducedOrder.Examples.MultizonePartlyCooled successful. +Declaring variable: Boolean rCheck ; + +Modelica.Utilities.Streams.print(" { \"file\" : \"AixLib/Resources/Scripts/Dymola/ThermalZones/ReducedOrder/Examples/MultizonePartlyCooled.mos\",", "AixLib.ThermalZones.ReducedOrder.Examples.MultizonePartlyCooled.statistics.log"); +Modelica.Utilities.Streams.print(" \"model\" : \"AixLib.ThermalZones.ReducedOrder.Examples.MultizonePartlyCooled\",", "AixLib.ThermalZones.ReducedOrder.Examples.MultizonePartlyCooled.statistics.log"); +Modelica.Utilities.Streams.print(" \"check\" : {", "AixLib.ThermalZones.ReducedOrder.Examples.MultizonePartlyCooled.statistics.log"); +Modelica.Utilities.Streams.print(" \"command\" : \"checkModel(\\\"AixLib.ThermalZones.ReducedOrder.Examples.MultizonePartlyCooled\\\");\",", "AixLib.ThermalZones.ReducedOrder.Examples.MultizonePartlyCooled.statistics.log"); +Modelica.Utilities.Streams.print(" \"result\" : " + String(rCheck), "AixLib.ThermalZones.ReducedOrder.Examples.MultizonePartlyCooled.statistics.log"); +Modelica.Utilities.Streams.print(" },", "AixLib.ThermalZones.ReducedOrder.Examples.MultizonePartlyCooled.statistics.log"); + + +rScript=RunScript("modelica://AixLib/Resources/Scripts/Dymola/ThermalZones/ReducedOrder/Examples/MultizonePartlyCooled.mos"); +simulateModel("AixLib.ThermalZones.ReducedOrder.Examples.MultizonePartlyCooled", tolerance=1e-6, startTime=14688000, stopTime=15552000, numberOfIntervals=0, outputInterval=3600, method="CVode", resultFile="AixLib.ThermalZones.ReducedOrder.Examples.MultizonePartlyCooled"); +Translation of AixLib.ThermalZones.ReducedOrder.Examples.MultizonePartlyCooled +The DAE has 9997 scalar unknowns and 9997 scalar equations. + +Statistics + +Original Model + Number of components: 1510 + Variables: 14667 + Constants: 315 (315 scalars) + Parameters: 4865 (5851 scalars) + Unknowns: 9487 (9997 scalars) + Differentiated variables: 39 scalars + Equations: 6500 + Nontrivial: 5993 +Translated Model + Constants: 2794 scalars + Free parameters: 1505 scalars + Parameter depending: 2674 scalars + Outputs: 23 scalars + Continuous time states: 39 scalars + Time-varying variables: 2979 scalars + Alias variables: 6211 scalars + Number of mixed real/discrete systems of equations: 0 + Sizes of linear systems of equations: {2, 29, 4, 2, 29, 4, 2, 29, 4, 2, 29, 4, 2, 29, 4} + Sizes after manipulation of the linear systems: {0, 4, 0, 0, 4, 0, 0, 4, 0, 0, 4, 0, 0, 4, 0} + Sizes of nonlinear systems of equations: {1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1} + Sizes after manipulation of the nonlinear systems: {0, 1, 0, 1, 0, 1, 0, 1, 0, 1, 0, 1, 0, 1, 0, 1, 0, 1, 0, 1, 0, 1, 0, 1, 0, 1, 0, 1, 0, 1} + Number of numerical Jacobians: 0 + Initialization problem + Sizes of linear systems of equations: {32, 32, 32, 32, 32} + Sizes after manipulation of the linear systems: {5, 5, 5, 5, 5} + +Selected continuous time states +Statically selected continuous time states +multizone.zone[1].heaterCooler.pITempCool.PI.I.y +multizone.zone[1].heaterCooler.pITempHeat.PI.I.y +multizone.zone[1].ROM.extWallRC.thermCapExt[1].T +multizone.zone[1].ROM.intWallRC.thermCapInt[1].T +multizone.zone[1].ROM.volAir.dynBal.m +multizone.zone[1].ROM.volAir.dynBal.U +multizone.zone[1].ventCont.dEMA.ExpAVG.x[1] +multizone.zone[1].ventCont.dEMA.ExpAVG1.x[1] +multizone.zone[2].heaterCooler.pITempCool.PI.I.y +multizone.zone[2].heaterCooler.pITempHeat.PI.I.y +multizone.zone[2].ROM.extWallRC.thermCapExt[1].T +multizone.zone[2].ROM.intWallRC.thermCapInt[1].T +multizone.zone[2].ROM.volAir.dynBal.m +multizone.zone[2].ROM.volAir.dynBal.U +multizone.zone[2].ventCont.dEMA.ExpAVG.x[1] +multizone.zone[2].ventCont.dEMA.ExpAVG1.x[1] +multizone.zone[3].heaterCooler.pITempHeat.PI.I.y +multizone.zone[3].ROM.extWallRC.thermCapExt[1].T +multizone.zone[3].ROM.intWallRC.thermCapInt[1].T +multizone.zone[3].ROM.volAir.dynBal.m +multizone.zone[3].ROM.volAir.dynBal.U +multizone.zone[3].ventCont.dEMA.ExpAVG.x[1] +multizone.zone[3].ventCont.dEMA.ExpAVG1.x[1] +multizone.zone[4].heaterCooler.pITempCool.PI.I.y +multizone.zone[4].heaterCooler.pITempHeat.PI.I.y +multizone.zone[4].ROM.extWallRC.thermCapExt[1].T +multizone.zone[4].ROM.intWallRC.thermCapInt[1].T +multizone.zone[4].ROM.volAir.dynBal.m +multizone.zone[4].ROM.volAir.dynBal.U +multizone.zone[4].ventCont.dEMA.ExpAVG.x[1] +multizone.zone[4].ventCont.dEMA.ExpAVG1.x[1] +multizone.zone[5].heaterCooler.pITempCool.PI.I.y +multizone.zone[5].heaterCooler.pITempHeat.PI.I.y +multizone.zone[5].ROM.extWallRC.thermCapExt[1].T +multizone.zone[5].ROM.intWallRC.thermCapInt[1].T +multizone.zone[5].ROM.volAir.dynBal.m +multizone.zone[5].ROM.volAir.dynBal.U +multizone.zone[5].ventCont.dEMA.ExpAVG.x[1] +multizone.zone[5].ventCont.dEMA.ExpAVG1.x[1] +Finished +Finished + = true + +Declaring variable: Boolean rScript ; + +savelog("AixLib.ThermalZones.ReducedOrder.Examples.MultizonePartlyCooled.translation.log"); = true + + +rCheck = checkModel("AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case650FF"); +Check of AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case650FF +The model has the same number of unknowns and equations: 1434 +The model has the same number of unknowns and equations +for the given numerical settings of parameters: 1434 +Check of AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case650FF successful. +Declaring variable: Boolean rCheck ; + +Modelica.Utilities.Streams.print(" { \"file\" : \"AixLib/Resources/Scripts/Dymola/ThermalZones/HighOrder/Validation/ASHRAE140/Case650FF.mos\",", "AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case650FF.statistics.log"); +Modelica.Utilities.Streams.print(" \"model\" : \"AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case650FF\",", "AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case650FF.statistics.log"); +Modelica.Utilities.Streams.print(" \"check\" : {", "AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case650FF.statistics.log"); +Modelica.Utilities.Streams.print(" \"command\" : \"checkModel(\\\"AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case650FF\\\");\",", "AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case650FF.statistics.log"); +Modelica.Utilities.Streams.print(" \"result\" : " + String(rCheck), "AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case650FF.statistics.log"); +Modelica.Utilities.Streams.print(" },", "AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case650FF.statistics.log"); + + +rScript=RunScript("modelica://AixLib/Resources/Scripts/Dymola/ThermalZones/HighOrder/Validation/ASHRAE140/Case650FF.mos"); +simulateModel("AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case650FF", startTime=0, stopTime=31539600, outputInterval=1800, tolerance=1e-6, method="dassl", resultFile="AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case650FF"); +Translation of AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case650FF +The DAE has 1434 scalar unknowns and 1434 scalar equations. + +Statistics + +Original Model + Number of components: 303 + Variables: 2724 + Constants: 39 (274 scalars) + Parameters: 1288 (1982 scalars) + Unknowns: 1397 (1434 scalars) + Differentiated variables: 21 scalars + Equations: 1107 + Nontrivial: 906 +Translated Model + Constants: 722 scalars + Free parameters: 749 scalars + Parameter depending: 891 scalars + Outputs: 3 scalars + Continuous time states: 21 scalars + Time-varying variables: 438 scalars + Alias variables: 890 scalars + Number of mixed real/discrete systems of equations: 0 + Sizes of linear systems of equations: {4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 3, 4, 4, 4, 4} + Sizes after manipulation of the linear systems: {0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0} + Sizes of nonlinear systems of equations: {55} + Sizes after manipulation of the nonlinear systems: {13} + Number of numerical Jacobians: 0 + +Selected continuous time states +Statically selected continuous time states +integrator2.y +Room.airload.dynBal.m +Room.airload.dynBal.medium.Xi[1] +Room.airload.dynBal.U +Room.ceiling.Wall.simpleNLayer.cap[1].T +Room.ceiling.Wall.simpleNLayer.cap[2].T +Room.ceiling.Wall.simpleNLayer.cap[3].T +Room.floor.Wall.simpleNLayer.cap[1].T +Room.floor.Wall.simpleNLayer.cap[2].T +Room.wallEast.Wall.simpleNLayer.cap[1].T +Room.wallEast.Wall.simpleNLayer.cap[2].T +Room.wallEast.Wall.simpleNLayer.cap[3].T +Room.wallNorth.Wall.simpleNLayer.cap[1].T +Room.wallNorth.Wall.simpleNLayer.cap[2].T +Room.wallNorth.Wall.simpleNLayer.cap[3].T +Room.wallSouth.Wall.simpleNLayer.cap[1].T +Room.wallSouth.Wall.simpleNLayer.cap[2].T +Room.wallSouth.Wall.simpleNLayer.cap[3].T +Room.wallWest.Wall.simpleNLayer.cap[1].T +Room.wallWest.Wall.simpleNLayer.cap[2].T +Room.wallWest.Wall.simpleNLayer.cap[3].T +Finished +Finished + = true + +Declaring variable: Boolean rScript ; + +savelog("AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case650FF.translation.log"); = true + + +rCheck = checkModel("AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case640"); +Check of AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case640 +The model has the same number of unknowns and equations: 1586 +The model has the same number of unknowns and equations +for the given numerical settings of parameters: 1586 +Check of AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case640 successful. +Declaring variable: Boolean rCheck ; + +Modelica.Utilities.Streams.print(" { \"file\" : \"AixLib/Resources/Scripts/Dymola/ThermalZones/HighOrder/Validation/ASHRAE140/Case640.mos\",", "AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case640.statistics.log"); +Modelica.Utilities.Streams.print(" \"model\" : \"AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case640\",", "AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case640.statistics.log"); +Modelica.Utilities.Streams.print(" \"check\" : {", "AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case640.statistics.log"); +Modelica.Utilities.Streams.print(" \"command\" : \"checkModel(\\\"AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case640\\\");\",", "AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case640.statistics.log"); +Modelica.Utilities.Streams.print(" \"result\" : " + String(rCheck), "AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case640.statistics.log"); +Modelica.Utilities.Streams.print(" },", "AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case640.statistics.log"); + + +rScript=RunScript("modelica://AixLib/Resources/Scripts/Dymola/ThermalZones/HighOrder/Validation/ASHRAE140/Case640.mos"); +simulateModel("AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case640", startTime=0, stopTime=31539600, outputInterval=1800, tolerance=1e-6, method="dassl", resultFile="AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case640"); +Translation of AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case640 +The DAE has 1586 scalar unknowns and 1586 scalar equations. + +Statistics + +Original Model + Number of components: 353 + Variables: 3104 + Constants: 41 (276 scalars) + Parameters: 1514 (2202 scalars) + Unknowns: 1549 (1586 scalars) + Differentiated variables: 25 scalars + Equations: 1259 + Nontrivial: 1048 +Translated Model + Constants: 788 scalars + Free parameters: 893 scalars + Parameter depending: 926 scalars + Outputs: 5 scalars + Continuous time states: 25 scalars + Time-varying variables: 478 scalars + Alias variables: 979 scalars + Number of mixed real/discrete systems of equations: 0 + Sizes of linear systems of equations: {4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 3, 4, 4, 4, 4} + Sizes after manipulation of the linear systems: {0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0} + Sizes of nonlinear systems of equations: {55} + Sizes after manipulation of the nonlinear systems: {13} + Number of numerical Jacobians: 0 + +Selected continuous time states +Statically selected continuous time states +idealHeaterCooler.pITempCool.PI.I.y +idealHeaterCooler.pITempHeat.PI.I.y +integrator2.y +integratorCool.y +integratorHeat.y +Room.airload.dynBal.m +Room.airload.dynBal.medium.Xi[1] +Room.airload.dynBal.U +Room.ceiling.Wall.simpleNLayer.cap[1].T +Room.ceiling.Wall.simpleNLayer.cap[2].T +Room.ceiling.Wall.simpleNLayer.cap[3].T +Room.floor.Wall.simpleNLayer.cap[1].T +Room.floor.Wall.simpleNLayer.cap[2].T +Room.wallEast.Wall.simpleNLayer.cap[1].T +Room.wallEast.Wall.simpleNLayer.cap[2].T +Room.wallEast.Wall.simpleNLayer.cap[3].T +Room.wallNorth.Wall.simpleNLayer.cap[1].T +Room.wallNorth.Wall.simpleNLayer.cap[2].T +Room.wallNorth.Wall.simpleNLayer.cap[3].T +Room.wallSouth.Wall.simpleNLayer.cap[1].T +Room.wallSouth.Wall.simpleNLayer.cap[2].T +Room.wallSouth.Wall.simpleNLayer.cap[3].T +Room.wallWest.Wall.simpleNLayer.cap[1].T +Room.wallWest.Wall.simpleNLayer.cap[2].T +Room.wallWest.Wall.simpleNLayer.cap[3].T +Finished +Finished + = true + +Declaring variable: Boolean rScript ; + +savelog("AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case640.translation.log"); = true + + +rCheck = checkModel("AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case940"); +Check of AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case940 +The model has the same number of unknowns and equations: 1586 +The model has the same number of unknowns and equations +for the given numerical settings of parameters: 1586 +Check of AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case940 successful. +Declaring variable: Boolean rCheck ; + +Modelica.Utilities.Streams.print(" { \"file\" : \"AixLib/Resources/Scripts/Dymola/ThermalZones/HighOrder/Validation/ASHRAE140/Case940.mos\",", "AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case940.statistics.log"); +Modelica.Utilities.Streams.print(" \"model\" : \"AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case940\",", "AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case940.statistics.log"); +Modelica.Utilities.Streams.print(" \"check\" : {", "AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case940.statistics.log"); +Modelica.Utilities.Streams.print(" \"command\" : \"checkModel(\\\"AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case940\\\");\",", "AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case940.statistics.log"); +Modelica.Utilities.Streams.print(" \"result\" : " + String(rCheck), "AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case940.statistics.log"); +Modelica.Utilities.Streams.print(" },", "AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case940.statistics.log"); + + +rScript=RunScript("modelica://AixLib/Resources/Scripts/Dymola/ThermalZones/HighOrder/Validation/ASHRAE140/Case940.mos"); +simulateModel("AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case940", startTime=0, stopTime=31539600, outputInterval=1800, tolerance=1e-6, method="dassl", resultFile="AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case940"); +Translation of AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case940 +The DAE has 1586 scalar unknowns and 1586 scalar equations. + +Statistics + +Original Model + Number of components: 353 + Variables: 3104 + Constants: 41 (276 scalars) + Parameters: 1514 (2202 scalars) + Unknowns: 1549 (1586 scalars) + Differentiated variables: 25 scalars + Equations: 1259 + Nontrivial: 1048 +Translated Model + Constants: 788 scalars + Free parameters: 893 scalars + Parameter depending: 926 scalars + Outputs: 5 scalars + Continuous time states: 25 scalars + Time-varying variables: 478 scalars + Alias variables: 979 scalars + Number of mixed real/discrete systems of equations: 0 + Sizes of linear systems of equations: {4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 3, 4, 4, 4, 4} + Sizes after manipulation of the linear systems: {0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0} + Sizes of nonlinear systems of equations: {55} + Sizes after manipulation of the nonlinear systems: {13} + Number of numerical Jacobians: 0 + +Selected continuous time states +Statically selected continuous time states +idealHeaterCooler.pITempCool.PI.I.y +idealHeaterCooler.pITempHeat.PI.I.y +integrator2.y +integratorCool.y +integratorHeat.y +Room.airload.dynBal.m +Room.airload.dynBal.medium.Xi[1] +Room.airload.dynBal.U +Room.ceiling.Wall.simpleNLayer.cap[1].T +Room.ceiling.Wall.simpleNLayer.cap[2].T +Room.ceiling.Wall.simpleNLayer.cap[3].T +Room.floor.Wall.simpleNLayer.cap[1].T +Room.floor.Wall.simpleNLayer.cap[2].T +Room.wallEast.Wall.simpleNLayer.cap[1].T +Room.wallEast.Wall.simpleNLayer.cap[2].T +Room.wallEast.Wall.simpleNLayer.cap[3].T +Room.wallNorth.Wall.simpleNLayer.cap[1].T +Room.wallNorth.Wall.simpleNLayer.cap[2].T +Room.wallNorth.Wall.simpleNLayer.cap[3].T +Room.wallSouth.Wall.simpleNLayer.cap[1].T +Room.wallSouth.Wall.simpleNLayer.cap[2].T +Room.wallSouth.Wall.simpleNLayer.cap[3].T +Room.wallWest.Wall.simpleNLayer.cap[1].T +Room.wallWest.Wall.simpleNLayer.cap[2].T +Room.wallWest.Wall.simpleNLayer.cap[3].T +Finished +Finished + = true + +Declaring variable: Boolean rScript ; + +savelog("AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case940.translation.log"); = true + + +rCheck = checkModel("AixLib.ThermalZones.ReducedOrder.Examples.ThermalZoneAirExchange"); +Check of AixLib.ThermalZones.ReducedOrder.Examples.ThermalZoneAirExchange +The model has the same number of unknowns and equations: 2010 +The model could not be deduced to be symbolically well-posed. +The model has + 1849+29*thermalZone.zoneParam.nOrientations+thermalZone.ROM.volAir.dynBal.nPorts +thermalZone.humanSenHeaDependent.productHeatOutput.nu+thermalZone.machinesSenHea.productHeatOutput.nu +thermalZone.lights.productHeatOutput.nu+thermalZone.ventCont.optimalTemp.nin+ thermalZone.ventCont.optimalTemp.nout+thermalZone.ventCont.dEMA.nout+ thermalZone.ventCont.dEMA.ExpAVG.n+thermalZone.ventCont.dEMA.ExpAVG1.n+max([ size(internalGains.columns, 1); size(internalGains.offset, 1)]) +scalar unknowns and + 1901+(if weaDat.pAtmSou == AixLib.BoundaryConditions.Types.DataSource.Parameter then 1 else 0)+(if weaDat.TDewPoiSou == AixLib.BoundaryConditions.Types.DataSource. Parameter then 1 else 0)+(if weaDat.TDryBulSou == AixLib.BoundaryConditions.Types.DataSource. Parameter then 1 else 0)+(if weaDat.TBlaSkySou == AixLib.BoundaryConditions.Types.DataSource. Parameter then 1 else 0)+(if weaDat.relHumSou == AixLib.BoundaryConditions.Types.DataSource. Parameter then 1 else 0)+(if weaDat.opaSkyCovSou == AixLib.BoundaryConditions.Types.DataSource. Parameter then 1 else 0)+(if weaDat.ceiHeiSou == AixLib.BoundaryConditions.Types.DataSource. Parameter then 1 else 0)+(if weaDat.totSkyCovSou == AixLib.BoundaryConditions.Types.DataSource. Parameter then 1 else 0)+(if weaDat.winSpeSou == AixLib.BoundaryConditions.Types.DataSource. Parameter then 1 else 0)+(if weaDat.winDirSou == AixLib.BoundaryConditions.Types.DataSource. Parameter then 1 else 0)+(if weaDat.HInfHorSou == AixLib.BoundaryConditions.Types.DataSource. Parameter then 1 else 0)+(if weaDat.HSou == AixLib.BoundaryConditions.Types.RadiationDataSource. Input_HDirNor_HDifHor then 2 else 1)+(if weaDat.HSou == AixLib.BoundaryConditions.Types.RadiationDataSource. Input_HDirNor_HGloHor then 2 else 1)+(if weaDat.HSou == AixLib.BoundaryConditions.Types.RadiationDataSource. Input_HGloHor_HDifHor then 2 else 1)+max([size(internalGains.columns, 1); size (internalGains.offset, 1)])+19*thermalZone.zoneParam.nOrientations+(if not thermalZone.eqAirTempWall.TGroundFromInput then 1 else 0)+thermalZone.ventCont.optimalTemp.nout +thermalZone.ventCont.dEMA.ExpAVG.n+thermalZone.ventCont.dEMA.ExpAVG1.n+(if not thermalZone.ROM.volAir.dynBal.use_mWat_flow then 1 else 0)+3* thermalZone.ROM.volAir.dynBal.nPorts +scalar equations. +However, exploiting the given numerical settings of parameters gives the same number of unknowns and equations: + 2010 +Check of AixLib.ThermalZones.ReducedOrder.Examples.ThermalZoneAirExchange successful. +Declaring variable: Boolean rCheck ; + +Modelica.Utilities.Streams.print(" { \"file\" : \"AixLib/Resources/Scripts/Dymola/ThermalZones/ReducedOrder/Examples/ThermalZoneAirExchange.mos\",", "AixLib.ThermalZones.ReducedOrder.Examples.ThermalZoneAirExchange.statistics.log"); +Modelica.Utilities.Streams.print(" \"model\" : \"AixLib.ThermalZones.ReducedOrder.Examples.ThermalZoneAirExchange\",", "AixLib.ThermalZones.ReducedOrder.Examples.ThermalZoneAirExchange.statistics.log"); +Modelica.Utilities.Streams.print(" \"check\" : {", "AixLib.ThermalZones.ReducedOrder.Examples.ThermalZoneAirExchange.statistics.log"); +Modelica.Utilities.Streams.print(" \"command\" : \"checkModel(\\\"AixLib.ThermalZones.ReducedOrder.Examples.ThermalZoneAirExchange\\\");\",", "AixLib.ThermalZones.ReducedOrder.Examples.ThermalZoneAirExchange.statistics.log"); +Modelica.Utilities.Streams.print(" \"result\" : " + String(rCheck), "AixLib.ThermalZones.ReducedOrder.Examples.ThermalZoneAirExchange.statistics.log"); +Modelica.Utilities.Streams.print(" },", "AixLib.ThermalZones.ReducedOrder.Examples.ThermalZoneAirExchange.statistics.log"); + + +rScript=RunScript("modelica://AixLib/Resources/Scripts/Dymola/ThermalZones/ReducedOrder/Examples/ThermalZoneAirExchange.mos"); +simulateModel("AixLib.ThermalZones.ReducedOrder.Examples.ThermalZoneAirExchange", tolerance=1e-6, stopTime=3.1536e+007, numberOfIntervals=0, outputInterval=3600, method="CVode", resultFile="AixLib.ThermalZones.ReducedOrder.Examples.ThermalZoneAirExchange"); +Translation of AixLib.ThermalZones.ReducedOrder.Examples.ThermalZoneAirExchange +The DAE has 2010 scalar unknowns and 2010 scalar equations. + +Statistics + +Original Model + Number of components: 304 + Variables: 2766 + Constants: 74 (74 scalars) + Parameters: 789 (2603 scalars) + Unknowns: 1903 (2010 scalars) + Differentiated variables: 6 scalars + Equations: 1344 + Nontrivial: 1238 +Translated Model + Constants: 571 scalars + Free parameters: 1947 scalars + Parameter depending: 316 scalars + Outputs: 23 scalars + Continuous time states: 6 scalars + Time-varying variables: 622 scalars + Alias variables: 1231 scalars + Number of mixed real/discrete systems of equations: 0 + Sizes of linear systems of equations: {2, 29, 4} + Sizes after manipulation of the linear systems: {0, 4, 0} + Sizes of nonlinear systems of equations: {1, 1, 1, 1, 1, 1} + Sizes after manipulation of the nonlinear systems: {0, 1, 0, 1, 0, 1} + Number of numerical Jacobians: 0 + Initialization problem + Sizes of linear systems of equations: {32} + Sizes after manipulation of the linear systems: {5} + +Selected continuous time states +Statically selected continuous time states +thermalZone.ROM.extWallRC.thermCapExt[1].T +thermalZone.ROM.intWallRC.thermCapInt[1].T +thermalZone.ROM.volAir.dynBal.m +thermalZone.ROM.volAir.dynBal.U +thermalZone.ventCont.dEMA.ExpAVG.x[1] +thermalZone.ventCont.dEMA.ExpAVG1.x[1] +Finished +Finished + = true + + + + +Declaring variable: Boolean rScript ; + +savelog("AixLib.ThermalZones.ReducedOrder.Examples.ThermalZoneAirExchange.translation.log"); = true + + +rCheck = checkModel("AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case600FF"); +Check of AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case600FF +The model has the same number of unknowns and equations: 1431 +The model has the same number of unknowns and equations +for the given numerical settings of parameters: 1431 +Check of AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case600FF successful. +Declaring variable: Boolean rCheck ; + +Modelica.Utilities.Streams.print(" { \"file\" : \"AixLib/Resources/Scripts/Dymola/ThermalZones/HighOrder/Validation/ASHRAE140/Case600FF.mos\",", "AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case600FF.statistics.log"); +Modelica.Utilities.Streams.print(" \"model\" : \"AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case600FF\",", "AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case600FF.statistics.log"); +Modelica.Utilities.Streams.print(" \"check\" : {", "AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case600FF.statistics.log"); +Modelica.Utilities.Streams.print(" \"command\" : \"checkModel(\\\"AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case600FF\\\");\",", "AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case600FF.statistics.log"); +Modelica.Utilities.Streams.print(" \"result\" : " + String(rCheck), "AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case600FF.statistics.log"); +Modelica.Utilities.Streams.print(" },", "AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case600FF.statistics.log"); + + +rScript=RunScript("modelica://AixLib/Resources/Scripts/Dymola/ThermalZones/HighOrder/Validation/ASHRAE140/Case600FF.mos"); +simulateModel("AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case600FF", startTime=0, stopTime=31539600, outputInterval=1800, tolerance=1e-6, method="dassl", resultFile="AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case600FF"); +Translation of AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case600FF +The DAE has 1431 scalar unknowns and 1431 scalar equations. + +Statistics + +Original Model + Number of components: 300 + Variables: 2699 + Constants: 39 (274 scalars) + Parameters: 1266 (1927 scalars) + Unknowns: 1394 (1431 scalars) + Differentiated variables: 21 scalars + Equations: 1103 + Nontrivial: 901 +Translated Model + Constants: 714 scalars + Free parameters: 720 scalars + Parameter depending: 873 scalars + Outputs: 3 scalars + Continuous time states: 21 scalars + Time-varying variables: 434 scalars + Alias variables: 891 scalars + Number of mixed real/discrete systems of equations: 0 + Sizes of linear systems of equations: {4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 3, 4, 4, 4, 4} + Sizes after manipulation of the linear systems: {0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0} + Sizes of nonlinear systems of equations: {55} + Sizes after manipulation of the nonlinear systems: {13} + Number of numerical Jacobians: 0 + +Selected continuous time states +Statically selected continuous time states +integrator2.y +Room.airload.dynBal.m +Room.airload.dynBal.medium.Xi[1] +Room.airload.dynBal.U +Room.ceiling.Wall.simpleNLayer.cap[1].T +Room.ceiling.Wall.simpleNLayer.cap[2].T +Room.ceiling.Wall.simpleNLayer.cap[3].T +Room.floor.Wall.simpleNLayer.cap[1].T +Room.floor.Wall.simpleNLayer.cap[2].T +Room.wallEast.Wall.simpleNLayer.cap[1].T +Room.wallEast.Wall.simpleNLayer.cap[2].T +Room.wallEast.Wall.simpleNLayer.cap[3].T +Room.wallNorth.Wall.simpleNLayer.cap[1].T +Room.wallNorth.Wall.simpleNLayer.cap[2].T +Room.wallNorth.Wall.simpleNLayer.cap[3].T +Room.wallSouth.Wall.simpleNLayer.cap[1].T +Room.wallSouth.Wall.simpleNLayer.cap[2].T +Room.wallSouth.Wall.simpleNLayer.cap[3].T +Room.wallWest.Wall.simpleNLayer.cap[1].T +Room.wallWest.Wall.simpleNLayer.cap[2].T +Room.wallWest.Wall.simpleNLayer.cap[3].T +Finished +Finished + = true + +Declaring variable: Boolean rScript ; + +savelog("AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case600FF.translation.log"); = true + + +rCheck = checkModel("AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case420"); +Check of AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case420 +The model has the same number of unknowns and equations: 1568 +The model has the same number of unknowns and equations +for the given numerical settings of parameters: 1568 +Check of AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case420 successful. +Declaring variable: Boolean rCheck ; + +Modelica.Utilities.Streams.print(" { \"file\" : \"AixLib/Resources/Scripts/Dymola/ThermalZones/HighOrder/Validation/ASHRAE140/Case420.mos\",", "AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case420.statistics.log"); +Modelica.Utilities.Streams.print(" \"model\" : \"AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case420\",", "AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case420.statistics.log"); +Modelica.Utilities.Streams.print(" \"check\" : {", "AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case420.statistics.log"); +Modelica.Utilities.Streams.print(" \"command\" : \"checkModel(\\\"AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case420\\\");\",", "AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case420.statistics.log"); +Modelica.Utilities.Streams.print(" \"result\" : " + String(rCheck), "AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case420.statistics.log"); +Modelica.Utilities.Streams.print(" },", "AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case420.statistics.log"); + + +rScript=RunScript("modelica://AixLib/Resources/Scripts/Dymola/ThermalZones/HighOrder/Validation/ASHRAE140/Case420.mos"); +simulateModel("AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case420", startTime=0, stopTime=31539600, outputInterval=1800, tolerance=1e-6, method="dassl", resultFile="AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case420"); +Translation of AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case420 +The DAE has 1568 scalar unknowns and 1568 scalar equations. + +Statistics + +Original Model + Number of components: 349 + Variables: 3047 + Constants: 41 (276 scalars) + Parameters: 1474 (2065 scalars) + Unknowns: 1532 (1568 scalars) + Differentiated variables: 25 scalars + Equations: 1252 + Nontrivial: 1041 +Translated Model + Constants: 771 scalars + Free parameters: 794 scalars + Parameter depending: 906 scalars + Outputs: 5 scalars + Continuous time states: 25 scalars + Time-varying variables: 461 scalars + Alias variables: 977 scalars + Number of mixed real/discrete systems of equations: 0 + Sizes of linear systems of equations: {4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 3, 4, 4, 4, 4} + Sizes after manipulation of the linear systems: {0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0} + Sizes of nonlinear systems of equations: {55} + Sizes after manipulation of the nonlinear systems: {13} + Number of numerical Jacobians: 0 + +Selected continuous time states +Statically selected continuous time states +idealHeaterCooler.pITempCool.PI.I.y +idealHeaterCooler.pITempHeat.PI.I.y +integrator2.y +integratorCool.y +integratorHeat.y +Room.airload.dynBal.m +Room.airload.dynBal.medium.Xi[1] +Room.airload.dynBal.U +Room.ceiling.Wall.simpleNLayer.cap[1].T +Room.ceiling.Wall.simpleNLayer.cap[2].T +Room.ceiling.Wall.simpleNLayer.cap[3].T +Room.floor.Wall.simpleNLayer.cap[1].T +Room.floor.Wall.simpleNLayer.cap[2].T +Room.wallEast.Wall.simpleNLayer.cap[1].T +Room.wallEast.Wall.simpleNLayer.cap[2].T +Room.wallEast.Wall.simpleNLayer.cap[3].T +Room.wallNorth.Wall.simpleNLayer.cap[1].T +Room.wallNorth.Wall.simpleNLayer.cap[2].T +Room.wallNorth.Wall.simpleNLayer.cap[3].T +Room.wallSouth.Wall.simpleNLayer.cap[1].T +Room.wallSouth.Wall.simpleNLayer.cap[2].T +Room.wallSouth.Wall.simpleNLayer.cap[3].T +Room.wallWest.Wall.simpleNLayer.cap[1].T +Room.wallWest.Wall.simpleNLayer.cap[2].T +Room.wallWest.Wall.simpleNLayer.cap[3].T +Finished +Finished + = true + +Declaring variable: Boolean rScript ; + +savelog("AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case420.translation.log"); = true + + +rCheck = checkModel("AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case210"); +Check of AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case210 +The model has the same number of unknowns and equations: 1568 +The model has the same number of unknowns and equations +for the given numerical settings of parameters: 1568 +Check of AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case210 successful. +Declaring variable: Boolean rCheck ; + +Modelica.Utilities.Streams.print(" { \"file\" : \"AixLib/Resources/Scripts/Dymola/ThermalZones/HighOrder/Validation/ASHRAE140/Case210.mos\",", "AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case210.statistics.log"); +Modelica.Utilities.Streams.print(" \"model\" : \"AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case210\",", "AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case210.statistics.log"); +Modelica.Utilities.Streams.print(" \"check\" : {", "AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case210.statistics.log"); +Modelica.Utilities.Streams.print(" \"command\" : \"checkModel(\\\"AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case210\\\");\",", "AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case210.statistics.log"); +Modelica.Utilities.Streams.print(" \"result\" : " + String(rCheck), "AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case210.statistics.log"); +Modelica.Utilities.Streams.print(" },", "AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case210.statistics.log"); + + +rScript=RunScript("modelica://AixLib/Resources/Scripts/Dymola/ThermalZones/HighOrder/Validation/ASHRAE140/Case210.mos"); +simulateModel("AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case210", startTime=0, stopTime=31539600, outputInterval=1800, tolerance=1e-6, method="dassl", resultFile="AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case210"); +Translation of AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case210 +The DAE has 1568 scalar unknowns and 1568 scalar equations. + +Statistics + +Original Model + Number of components: 349 + Variables: 3047 + Constants: 41 (276 scalars) + Parameters: 1474 (2065 scalars) + Unknowns: 1532 (1568 scalars) + Differentiated variables: 25 scalars + Equations: 1252 + Nontrivial: 1041 +Translated Model + Constants: 771 scalars + Free parameters: 794 scalars + Parameter depending: 906 scalars + Outputs: 5 scalars + Continuous time states: 25 scalars + Time-varying variables: 461 scalars + Alias variables: 977 scalars + Number of mixed real/discrete systems of equations: 0 + Sizes of linear systems of equations: {4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 3, 4, 4, 4, 4} + Sizes after manipulation of the linear systems: {0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0} + Sizes of nonlinear systems of equations: {55} + Sizes after manipulation of the nonlinear systems: {13} + Number of numerical Jacobians: 0 + +Selected continuous time states +Statically selected continuous time states +idealHeaterCooler.pITempCool.PI.I.y +idealHeaterCooler.pITempHeat.PI.I.y +integrator2.y +integratorCool.y +integratorHeat.y +Room.airload.dynBal.m +Room.airload.dynBal.medium.Xi[1] +Room.airload.dynBal.U +Room.ceiling.Wall.simpleNLayer.cap[1].T +Room.ceiling.Wall.simpleNLayer.cap[2].T +Room.ceiling.Wall.simpleNLayer.cap[3].T +Room.floor.Wall.simpleNLayer.cap[1].T +Room.floor.Wall.simpleNLayer.cap[2].T +Room.wallEast.Wall.simpleNLayer.cap[1].T +Room.wallEast.Wall.simpleNLayer.cap[2].T +Room.wallEast.Wall.simpleNLayer.cap[3].T +Room.wallNorth.Wall.simpleNLayer.cap[1].T +Room.wallNorth.Wall.simpleNLayer.cap[2].T +Room.wallNorth.Wall.simpleNLayer.cap[3].T +Room.wallSouth.Wall.simpleNLayer.cap[1].T +Room.wallSouth.Wall.simpleNLayer.cap[2].T +Room.wallSouth.Wall.simpleNLayer.cap[3].T +Room.wallWest.Wall.simpleNLayer.cap[1].T +Room.wallWest.Wall.simpleNLayer.cap[2].T +Room.wallWest.Wall.simpleNLayer.cap[3].T +Finished +Finished + = true + +Declaring variable: Boolean rScript ; + +savelog("AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case210.translation.log"); = true + + +rCheck = checkModel("AixLib.ThermalZones.ReducedOrder.Examples.MultizoneMoistAirCO2Equipped"); +Warning: Can not resolve link "AixLib.ThermalZones.ReducedOrder.Multizone.MultizoneMoistAirEquipped" in AixLib.ThermalZones.ReducedOrder.Examples.MultizoneMoistAirCO2Equipped +Check of AixLib.ThermalZones.ReducedOrder.Examples.MultizoneMoistAirCO2Equipped +The model has the same number of unknowns and equations: 10433 +The model has the same number of unknowns and equations +for the given numerical settings of parameters: 10433 +Check of AixLib.ThermalZones.ReducedOrder.Examples.MultizoneMoistAirCO2Equipped successful. +Declaring variable: Boolean rCheck ; + +Modelica.Utilities.Streams.print(" { \"file\" : \"AixLib/Resources/Scripts/Dymola/ThermalZones/ReducedOrder/Examples/MultizoneMoistAirCO2Equipped.mos\",", "AixLib.ThermalZones.ReducedOrder.Examples.MultizoneMoistAirCO2Equipped.statistics.log"); +Modelica.Utilities.Streams.print(" \"model\" : \"AixLib.ThermalZones.ReducedOrder.Examples.MultizoneMoistAirCO2Equipped\",", "AixLib.ThermalZones.ReducedOrder.Examples.MultizoneMoistAirCO2Equipped.statistics.log"); +Modelica.Utilities.Streams.print(" \"check\" : {", "AixLib.ThermalZones.ReducedOrder.Examples.MultizoneMoistAirCO2Equipped.statistics.log"); +Modelica.Utilities.Streams.print(" \"command\" : \"checkModel(\\\"AixLib.ThermalZones.ReducedOrder.Examples.MultizoneMoistAirCO2Equipped\\\");\",", "AixLib.ThermalZones.ReducedOrder.Examples.MultizoneMoistAirCO2Equipped.statistics.log"); +Modelica.Utilities.Streams.print(" \"result\" : " + String(rCheck), "AixLib.ThermalZones.ReducedOrder.Examples.MultizoneMoistAirCO2Equipped.statistics.log"); +Modelica.Utilities.Streams.print(" },", "AixLib.ThermalZones.ReducedOrder.Examples.MultizoneMoistAirCO2Equipped.statistics.log"); + + +rScript=RunScript("modelica://AixLib/Resources/Scripts/Dymola/ThermalZones/ReducedOrder/Examples/MultizoneMoistAirCO2Equipped.mos"); +simulateModel("AixLib.ThermalZones.ReducedOrder.Examples.MultizoneMoistAirCO2Equipped", tolerance=1e-6, stopTime=864000, numberOfIntervals=0, outputInterval=3600, method="CVode", resultFile="AixLib.ThermalZones.ReducedOrder.Examples.MultizoneMoistAirCO2Equipped"); +Translation of AixLib.ThermalZones.ReducedOrder.Examples.MultizoneMoistAirCO2Equipped +The DAE has 10433 scalar unknowns and 10433 scalar equations. + +Statistics + +Original Model + Number of components: 1571 + Variables: 15954 + Constants: 419 (419 scalars) + Parameters: 5787 (7304 scalars) + Unknowns: 9746 (10478 scalars) + Differentiated variables: 45 scalars + Equations: 6734 + Nontrivial: 6189 +Translated Model + Constants: 3023 scalars + Free parameters: 1718 scalars + Parameter depending: 3798 scalars + Continuous time states: 45 scalars + Time-varying variables: 3274 scalars + Alias variables: 6388 scalars + Number of mixed real/discrete systems of equations: 0 + Sizes of linear systems of equations: {29, 4, 29, 4, 29, 4, 29, 4, 29, 4} + Sizes after manipulation of the linear systems: {4, 0, 4, 0, 4, 0, 4, 0, 4, 0} + Sizes of nonlinear systems of equations: {6, 6, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1} + Sizes after manipulation of the nonlinear systems: {1, 1, 0, 0, 1, 0, 1, 0, 1, 0, 1, 0, 1, 0, 1, 0, 1, 0, 1, 0, 1, 0, 1, 0, 1, 0, 1, 0, 1, 0, 1, 0, 1} + Number of numerical Jacobians: 0 + Initialization problem + Sizes of linear systems of equations: {32, 32, 32, 32, 32} + Sizes after manipulation of the linear systems: {5, 5, 5, 5, 5} + +Selected continuous time states +Statically selected continuous time states +multizone.zone[1].heaterCooler.pITempHeat.PI.I.y +multizone.zone[1].ROM.extWallRC.thermCapExt[1].T +multizone.zone[1].ROM.intWallRC.thermCapInt[1].T +multizone.zone[1].ROM.volMoiAir.dynBal.m +multizone.zone[1].ROM.volMoiAir.dynBal.mC[1] +multizone.zone[1].ROM.volMoiAir.dynBal.medium.Xi[1] +multizone.zone[1].ROM.volMoiAir.dynBal.U +multizone.zone[1].ventCont.dEMA.ExpAVG.x[1] +multizone.zone[1].ventCont.dEMA.ExpAVG1.x[1] +multizone.zone[2].heaterCooler.pITempHeat.PI.I.y +multizone.zone[2].ROM.extWallRC.thermCapExt[1].T +multizone.zone[2].ROM.intWallRC.thermCapInt[1].T +multizone.zone[2].ROM.volMoiAir.dynBal.m +multizone.zone[2].ROM.volMoiAir.dynBal.mC[1] +multizone.zone[2].ROM.volMoiAir.dynBal.medium.Xi[1] +multizone.zone[2].ROM.volMoiAir.dynBal.U +multizone.zone[2].ventCont.dEMA.ExpAVG.x[1] +multizone.zone[2].ventCont.dEMA.ExpAVG1.x[1] +multizone.zone[3].heaterCooler.pITempHeat.PI.I.y +multizone.zone[3].ROM.extWallRC.thermCapExt[1].T +multizone.zone[3].ROM.intWallRC.thermCapInt[1].T +multizone.zone[3].ROM.volMoiAir.dynBal.m +multizone.zone[3].ROM.volMoiAir.dynBal.mC[1] +multizone.zone[3].ROM.volMoiAir.dynBal.medium.Xi[1] +multizone.zone[3].ROM.volMoiAir.dynBal.U +multizone.zone[3].ventCont.dEMA.ExpAVG.x[1] +multizone.zone[3].ventCont.dEMA.ExpAVG1.x[1] +multizone.zone[4].heaterCooler.pITempHeat.PI.I.y +multizone.zone[4].ROM.extWallRC.thermCapExt[1].T +multizone.zone[4].ROM.intWallRC.thermCapInt[1].T +multizone.zone[4].ROM.volMoiAir.dynBal.m +multizone.zone[4].ROM.volMoiAir.dynBal.mC[1] +multizone.zone[4].ROM.volMoiAir.dynBal.medium.Xi[1] +multizone.zone[4].ROM.volMoiAir.dynBal.U +multizone.zone[4].ventCont.dEMA.ExpAVG.x[1] +multizone.zone[4].ventCont.dEMA.ExpAVG1.x[1] +multizone.zone[5].heaterCooler.pITempHeat.PI.I.y +multizone.zone[5].ROM.extWallRC.thermCapExt[1].T +multizone.zone[5].ROM.intWallRC.thermCapInt[1].T +multizone.zone[5].ROM.volMoiAir.dynBal.m +multizone.zone[5].ROM.volMoiAir.dynBal.mC[1] +multizone.zone[5].ROM.volMoiAir.dynBal.medium.Xi[1] +multizone.zone[5].ROM.volMoiAir.dynBal.U +multizone.zone[5].ventCont.dEMA.ExpAVG.x[1] +multizone.zone[5].ventCont.dEMA.ExpAVG1.x[1] +Finished +Finished + = true + +Declaring variable: Boolean rScript ; + +savelog("AixLib.ThermalZones.ReducedOrder.Examples.MultizoneMoistAirCO2Equipped.translation.log"); = true + + +rCheck = checkModel("AixLib.ThermalZones.ReducedOrder.Examples.Multizone"); +Check of AixLib.ThermalZones.ReducedOrder.Examples.Multizone +The model has the same number of unknowns and equations: 9729 +The model has the same number of unknowns and equations +for the given numerical settings of parameters: 9729 +Check of AixLib.ThermalZones.ReducedOrder.Examples.Multizone successful. +Declaring variable: Boolean rCheck ; + +Modelica.Utilities.Streams.print(" { \"file\" : \"AixLib/Resources/Scripts/Dymola/ThermalZones/ReducedOrder/Examples/Multizone.mos\",", "AixLib.ThermalZones.ReducedOrder.Examples.Multizone.statistics.log"); +Modelica.Utilities.Streams.print(" \"model\" : \"AixLib.ThermalZones.ReducedOrder.Examples.Multizone\",", "AixLib.ThermalZones.ReducedOrder.Examples.Multizone.statistics.log"); +Modelica.Utilities.Streams.print(" \"check\" : {", "AixLib.ThermalZones.ReducedOrder.Examples.Multizone.statistics.log"); +Modelica.Utilities.Streams.print(" \"command\" : \"checkModel(\\\"AixLib.ThermalZones.ReducedOrder.Examples.Multizone\\\");\",", "AixLib.ThermalZones.ReducedOrder.Examples.Multizone.statistics.log"); +Modelica.Utilities.Streams.print(" \"result\" : " + String(rCheck), "AixLib.ThermalZones.ReducedOrder.Examples.Multizone.statistics.log"); +Modelica.Utilities.Streams.print(" },", "AixLib.ThermalZones.ReducedOrder.Examples.Multizone.statistics.log"); + + +rScript=RunScript("modelica://AixLib/Resources/Scripts/Dymola/ThermalZones/ReducedOrder/Examples/Multizone.mos"); +simulateModel("AixLib.ThermalZones.ReducedOrder.Examples.Multizone", tolerance=1e-6, stopTime=864000, numberOfIntervals=0, outputInterval=3600, method="CVode", resultFile="AixLib.ThermalZones.ReducedOrder.Examples.Multizone"); +Translation of AixLib.ThermalZones.ReducedOrder.Examples.Multizone +The DAE has 9729 scalar unknowns and 9729 scalar equations. + +Statistics + +Original Model + Number of components: 1430 + Variables: 14167 + Constants: 311 (311 scalars) + Parameters: 4637 (5623 scalars) + Unknowns: 9219 (9729 scalars) + Differentiated variables: 35 scalars + Equations: 6252 + Nontrivial: 5761 +Translated Model + Constants: 2714 scalars + Free parameters: 1389 scalars + Parameter depending: 2610 scalars + Outputs: 23 scalars + Continuous time states: 35 scalars + Time-varying variables: 2907 scalars + Alias variables: 6043 scalars + Number of mixed real/discrete systems of equations: 0 + Sizes of linear systems of equations: {2, 29, 4, 2, 29, 4, 2, 29, 4, 2, 29, 4, 2, 29, 4} + Sizes after manipulation of the linear systems: {0, 4, 0, 0, 4, 0, 0, 4, 0, 0, 4, 0, 0, 4, 0} + Sizes of nonlinear systems of equations: {1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1} + Sizes after manipulation of the nonlinear systems: {0, 1, 0, 1, 0, 1, 0, 1, 0, 1, 0, 1, 0, 1, 0, 1, 0, 1, 0, 1, 0, 1, 0, 1, 0, 1, 0, 1, 0, 1} + Number of numerical Jacobians: 0 + Initialization problem + Sizes of linear systems of equations: {32, 32, 32, 32, 32} + Sizes after manipulation of the linear systems: {5, 5, 5, 5, 5} + +Selected continuous time states +Statically selected continuous time states +multizone.zone[1].heaterCooler.pITempHeat.PI.I.y +multizone.zone[1].ROM.extWallRC.thermCapExt[1].T +multizone.zone[1].ROM.intWallRC.thermCapInt[1].T +multizone.zone[1].ROM.volAir.dynBal.m +multizone.zone[1].ROM.volAir.dynBal.U +multizone.zone[1].ventCont.dEMA.ExpAVG.x[1] +multizone.zone[1].ventCont.dEMA.ExpAVG1.x[1] +multizone.zone[2].heaterCooler.pITempHeat.PI.I.y +multizone.zone[2].ROM.extWallRC.thermCapExt[1].T +multizone.zone[2].ROM.intWallRC.thermCapInt[1].T +multizone.zone[2].ROM.volAir.dynBal.m +multizone.zone[2].ROM.volAir.dynBal.U +multizone.zone[2].ventCont.dEMA.ExpAVG.x[1] +multizone.zone[2].ventCont.dEMA.ExpAVG1.x[1] +multizone.zone[3].heaterCooler.pITempHeat.PI.I.y +multizone.zone[3].ROM.extWallRC.thermCapExt[1].T +multizone.zone[3].ROM.intWallRC.thermCapInt[1].T +multizone.zone[3].ROM.volAir.dynBal.m +multizone.zone[3].ROM.volAir.dynBal.U +multizone.zone[3].ventCont.dEMA.ExpAVG.x[1] +multizone.zone[3].ventCont.dEMA.ExpAVG1.x[1] +multizone.zone[4].heaterCooler.pITempHeat.PI.I.y +multizone.zone[4].ROM.extWallRC.thermCapExt[1].T +multizone.zone[4].ROM.intWallRC.thermCapInt[1].T +multizone.zone[4].ROM.volAir.dynBal.m +multizone.zone[4].ROM.volAir.dynBal.U +multizone.zone[4].ventCont.dEMA.ExpAVG.x[1] +multizone.zone[4].ventCont.dEMA.ExpAVG1.x[1] +multizone.zone[5].heaterCooler.pITempHeat.PI.I.y +multizone.zone[5].ROM.extWallRC.thermCapExt[1].T +multizone.zone[5].ROM.intWallRC.thermCapInt[1].T +multizone.zone[5].ROM.volAir.dynBal.m +multizone.zone[5].ROM.volAir.dynBal.U +multizone.zone[5].ventCont.dEMA.ExpAVG.x[1] +multizone.zone[5].ventCont.dEMA.ExpAVG1.x[1] +Finished +Finished + = true + +Declaring variable: Boolean rScript ; + +savelog("AixLib.ThermalZones.ReducedOrder.Examples.Multizone.translation.log"); = true + + +rCheck = checkModel("AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case395"); +Check of AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case395 +The model has the same number of unknowns and equations: 1568 +The model has the same number of unknowns and equations +for the given numerical settings of parameters: 1568 +Check of AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case395 successful. +Declaring variable: Boolean rCheck ; + +Modelica.Utilities.Streams.print(" { \"file\" : \"AixLib/Resources/Scripts/Dymola/ThermalZones/HighOrder/Validation/ASHRAE140/Case395.mos\",", "AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case395.statistics.log"); +Modelica.Utilities.Streams.print(" \"model\" : \"AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case395\",", "AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case395.statistics.log"); +Modelica.Utilities.Streams.print(" \"check\" : {", "AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case395.statistics.log"); +Modelica.Utilities.Streams.print(" \"command\" : \"checkModel(\\\"AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case395\\\");\",", "AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case395.statistics.log"); +Modelica.Utilities.Streams.print(" \"result\" : " + String(rCheck), "AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case395.statistics.log"); +Modelica.Utilities.Streams.print(" },", "AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case395.statistics.log"); + + +rScript=RunScript("modelica://AixLib/Resources/Scripts/Dymola/ThermalZones/HighOrder/Validation/ASHRAE140/Case395.mos"); +simulateModel("AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case395", startTime=0, stopTime=31539600, outputInterval=1800, tolerance=1e-6, method="dassl", resultFile="AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case395"); +Translation of AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case395 +The DAE has 1568 scalar unknowns and 1568 scalar equations. + +Statistics + +Original Model + Number of components: 349 + Variables: 3047 + Constants: 41 (276 scalars) + Parameters: 1474 (2065 scalars) + Unknowns: 1532 (1568 scalars) + Differentiated variables: 25 scalars + Equations: 1252 + Nontrivial: 1041 +Translated Model + Constants: 771 scalars + Free parameters: 794 scalars + Parameter depending: 906 scalars + Outputs: 5 scalars + Continuous time states: 25 scalars + Time-varying variables: 461 scalars + Alias variables: 977 scalars + Number of mixed real/discrete systems of equations: 0 + Sizes of linear systems of equations: {4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 3, 4, 4, 4, 4} + Sizes after manipulation of the linear systems: {0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0} + Sizes of nonlinear systems of equations: {55} + Sizes after manipulation of the nonlinear systems: {13} + Number of numerical Jacobians: 0 + +Selected continuous time states +Statically selected continuous time states +idealHeaterCooler.pITempCool.PI.I.y +idealHeaterCooler.pITempHeat.PI.I.y +integrator2.y +integratorCool.y +integratorHeat.y +Room.airload.dynBal.m +Room.airload.dynBal.medium.Xi[1] +Room.airload.dynBal.U +Room.ceiling.Wall.simpleNLayer.cap[1].T +Room.ceiling.Wall.simpleNLayer.cap[2].T +Room.ceiling.Wall.simpleNLayer.cap[3].T +Room.floor.Wall.simpleNLayer.cap[1].T +Room.floor.Wall.simpleNLayer.cap[2].T +Room.wallEast.Wall.simpleNLayer.cap[1].T +Room.wallEast.Wall.simpleNLayer.cap[2].T +Room.wallEast.Wall.simpleNLayer.cap[3].T +Room.wallNorth.Wall.simpleNLayer.cap[1].T +Room.wallNorth.Wall.simpleNLayer.cap[2].T +Room.wallNorth.Wall.simpleNLayer.cap[3].T +Room.wallSouth.Wall.simpleNLayer.cap[1].T +Room.wallSouth.Wall.simpleNLayer.cap[2].T +Room.wallSouth.Wall.simpleNLayer.cap[3].T +Room.wallWest.Wall.simpleNLayer.cap[1].T +Room.wallWest.Wall.simpleNLayer.cap[2].T +Room.wallWest.Wall.simpleNLayer.cap[3].T +Finished +Finished + = true + +Declaring variable: Boolean rScript ; + +savelog("AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case395.translation.log"); = true + + +rCheck = checkModel("AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case320"); +Check of AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case320 +The model has the same number of unknowns and equations: 1585 +The model has the same number of unknowns and equations +for the given numerical settings of parameters: 1585 +Check of AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case320 successful. +Declaring variable: Boolean rCheck ; + +Modelica.Utilities.Streams.print(" { \"file\" : \"AixLib/Resources/Scripts/Dymola/ThermalZones/HighOrder/Validation/ASHRAE140/Case320.mos\",", "AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case320.statistics.log"); +Modelica.Utilities.Streams.print(" \"model\" : \"AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case320\",", "AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case320.statistics.log"); +Modelica.Utilities.Streams.print(" \"check\" : {", "AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case320.statistics.log"); +Modelica.Utilities.Streams.print(" \"command\" : \"checkModel(\\\"AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case320\\\");\",", "AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case320.statistics.log"); +Modelica.Utilities.Streams.print(" \"result\" : " + String(rCheck), "AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case320.statistics.log"); +Modelica.Utilities.Streams.print(" },", "AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case320.statistics.log"); + + +rScript=RunScript("modelica://AixLib/Resources/Scripts/Dymola/ThermalZones/HighOrder/Validation/ASHRAE140/Case320.mos"); +simulateModel("AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case320", startTime=0, stopTime=31539600, outputInterval=1800, tolerance=1e-6, method="dassl", resultFile="AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case320"); +Translation of AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case320 +The DAE has 1585 scalar unknowns and 1585 scalar equations. + +Statistics + +Original Model + Number of components: 352 + Variables: 3082 + Constants: 41 (276 scalars) + Parameters: 1493 (2159 scalars) + Unknowns: 1548 (1585 scalars) + Differentiated variables: 25 scalars + Equations: 1257 + Nontrivial: 1045 +Translated Model + Constants: 780 scalars + Free parameters: 876 scalars + Parameter depending: 909 scalars + Outputs: 5 scalars + Continuous time states: 25 scalars + Time-varying variables: 474 scalars + Alias variables: 981 scalars + Number of mixed real/discrete systems of equations: 0 + Sizes of linear systems of equations: {4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 3, 4, 4, 4, 4} + Sizes after manipulation of the linear systems: {0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0} + Sizes of nonlinear systems of equations: {55} + Sizes after manipulation of the nonlinear systems: {13} + Number of numerical Jacobians: 0 + +Selected continuous time states +Statically selected continuous time states +idealHeaterCooler.pITempCool.PI.I.y +idealHeaterCooler.pITempHeat.PI.I.y +integrator2.y +integratorCool.y +integratorHeat.y +Room.airload.dynBal.m +Room.airload.dynBal.medium.Xi[1] +Room.airload.dynBal.U +Room.ceiling.Wall.simpleNLayer.cap[1].T +Room.ceiling.Wall.simpleNLayer.cap[2].T +Room.ceiling.Wall.simpleNLayer.cap[3].T +Room.floor.Wall.simpleNLayer.cap[1].T +Room.floor.Wall.simpleNLayer.cap[2].T +Room.wallEast.Wall.simpleNLayer.cap[1].T +Room.wallEast.Wall.simpleNLayer.cap[2].T +Room.wallEast.Wall.simpleNLayer.cap[3].T +Room.wallNorth.Wall.simpleNLayer.cap[1].T +Room.wallNorth.Wall.simpleNLayer.cap[2].T +Room.wallNorth.Wall.simpleNLayer.cap[3].T +Room.wallSouth.Wall.simpleNLayer.cap[1].T +Room.wallSouth.Wall.simpleNLayer.cap[2].T +Room.wallSouth.Wall.simpleNLayer.cap[3].T +Room.wallWest.Wall.simpleNLayer.cap[1].T +Room.wallWest.Wall.simpleNLayer.cap[2].T +Room.wallWest.Wall.simpleNLayer.cap[3].T +Finished +Finished + = true + +Declaring variable: Boolean rScript ; + +savelog("AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case320.translation.log"); = true + + +rCheck = checkModel("AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case800"); +Check of AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case800 +The model has the same number of unknowns and equations: 1568 +The model has the same number of unknowns and equations +for the given numerical settings of parameters: 1568 +Check of AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case800 successful. +Declaring variable: Boolean rCheck ; + +Modelica.Utilities.Streams.print(" { \"file\" : \"AixLib/Resources/Scripts/Dymola/ThermalZones/HighOrder/Validation/ASHRAE140/Case800.mos\",", "AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case800.statistics.log"); +Modelica.Utilities.Streams.print(" \"model\" : \"AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case800\",", "AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case800.statistics.log"); +Modelica.Utilities.Streams.print(" \"check\" : {", "AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case800.statistics.log"); +Modelica.Utilities.Streams.print(" \"command\" : \"checkModel(\\\"AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case800\\\");\",", "AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case800.statistics.log"); +Modelica.Utilities.Streams.print(" \"result\" : " + String(rCheck), "AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case800.statistics.log"); +Modelica.Utilities.Streams.print(" },", "AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case800.statistics.log"); + + +rScript=RunScript("modelica://AixLib/Resources/Scripts/Dymola/ThermalZones/HighOrder/Validation/ASHRAE140/Case800.mos"); +simulateModel("AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case800", startTime=0, stopTime=31539600, outputInterval=1800, tolerance=1e-6, method="dassl", resultFile="AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case800"); +Translation of AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case800 +The DAE has 1568 scalar unknowns and 1568 scalar equations. + +Statistics + +Original Model + Number of components: 349 + Variables: 3047 + Constants: 41 (276 scalars) + Parameters: 1474 (2065 scalars) + Unknowns: 1532 (1568 scalars) + Differentiated variables: 25 scalars + Equations: 1252 + Nontrivial: 1041 +Translated Model + Constants: 771 scalars + Free parameters: 794 scalars + Parameter depending: 906 scalars + Outputs: 5 scalars + Continuous time states: 25 scalars + Time-varying variables: 461 scalars + Alias variables: 977 scalars + Number of mixed real/discrete systems of equations: 0 + Sizes of linear systems of equations: {4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 3, 4, 4, 4, 4} + Sizes after manipulation of the linear systems: {0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0} + Sizes of nonlinear systems of equations: {55} + Sizes after manipulation of the nonlinear systems: {13} + Number of numerical Jacobians: 0 + +Selected continuous time states +Statically selected continuous time states +idealHeaterCooler.pITempCool.PI.I.y +idealHeaterCooler.pITempHeat.PI.I.y +integrator2.y +integratorCool.y +integratorHeat.y +Room.airload.dynBal.m +Room.airload.dynBal.medium.Xi[1] +Room.airload.dynBal.U +Room.ceiling.Wall.simpleNLayer.cap[1].T +Room.ceiling.Wall.simpleNLayer.cap[2].T +Room.ceiling.Wall.simpleNLayer.cap[3].T +Room.floor.Wall.simpleNLayer.cap[1].T +Room.floor.Wall.simpleNLayer.cap[2].T +Room.wallEast.Wall.simpleNLayer.cap[1].T +Room.wallEast.Wall.simpleNLayer.cap[2].T +Room.wallEast.Wall.simpleNLayer.cap[3].T +Room.wallNorth.Wall.simpleNLayer.cap[1].T +Room.wallNorth.Wall.simpleNLayer.cap[2].T +Room.wallNorth.Wall.simpleNLayer.cap[3].T +Room.wallSouth.Wall.simpleNLayer.cap[1].T +Room.wallSouth.Wall.simpleNLayer.cap[2].T +Room.wallSouth.Wall.simpleNLayer.cap[3].T +Room.wallWest.Wall.simpleNLayer.cap[1].T +Room.wallWest.Wall.simpleNLayer.cap[2].T +Room.wallWest.Wall.simpleNLayer.cap[3].T +Finished +Finished + = true + +Declaring variable: Boolean rScript ; + +savelog("AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case800.translation.log"); = true + + +rCheck = checkModel("AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case650"); +Check of AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case650 +The model has the same number of unknowns and equations: 1522 +The model has the same number of unknowns and equations +for the given numerical settings of parameters: 1522 +Check of AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case650 successful. +Declaring variable: Boolean rCheck ; + +Modelica.Utilities.Streams.print(" { \"file\" : \"AixLib/Resources/Scripts/Dymola/ThermalZones/HighOrder/Validation/ASHRAE140/Case650.mos\",", "AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case650.statistics.log"); +Modelica.Utilities.Streams.print(" \"model\" : \"AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case650\",", "AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case650.statistics.log"); +Modelica.Utilities.Streams.print(" \"check\" : {", "AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case650.statistics.log"); +Modelica.Utilities.Streams.print(" \"command\" : \"checkModel(\\\"AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case650\\\");\",", "AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case650.statistics.log"); +Modelica.Utilities.Streams.print(" \"result\" : " + String(rCheck), "AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case650.statistics.log"); +Modelica.Utilities.Streams.print(" },", "AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case650.statistics.log"); + + +rScript=RunScript("modelica://AixLib/Resources/Scripts/Dymola/ThermalZones/HighOrder/Validation/ASHRAE140/Case650.mos"); +simulateModel("AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case650", startTime=0, stopTime=31539600, outputInterval=1800, tolerance=1e-6, method="dassl", resultFile="AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case650"); +Translation of AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case650 +The DAE has 1522 scalar unknowns and 1522 scalar equations. + +Statistics + +Original Model + Number of components: 334 + Variables: 3002 + Constants: 40 (275 scalars) + Parameters: 1477 (2187 scalars) + Unknowns: 1485 (1522 scalars) + Differentiated variables: 24 scalars + Equations: 1198 + Nontrivial: 992 +Translated Model + Constants: 777 scalars + Free parameters: 881 scalars + Parameter depending: 926 scalars + Outputs: 5 scalars + Continuous time states: 24 scalars + Time-varying variables: 464 scalars + Alias variables: 936 scalars + Number of mixed real/discrete systems of equations: 0 + Sizes of linear systems of equations: {4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 3, 4, 4, 4, 4} + Sizes after manipulation of the linear systems: {0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0} + Sizes of nonlinear systems of equations: {55} + Sizes after manipulation of the nonlinear systems: {13} + Number of numerical Jacobians: 0 + +Selected continuous time states +Statically selected continuous time states +idealHeaterCooler.pITempCool.PI.I.y +integrator2.y +integratorCool.y +integratorHeat.y +Room.airload.dynBal.m +Room.airload.dynBal.medium.Xi[1] +Room.airload.dynBal.U +Room.ceiling.Wall.simpleNLayer.cap[1].T +Room.ceiling.Wall.simpleNLayer.cap[2].T +Room.ceiling.Wall.simpleNLayer.cap[3].T +Room.floor.Wall.simpleNLayer.cap[1].T +Room.floor.Wall.simpleNLayer.cap[2].T +Room.wallEast.Wall.simpleNLayer.cap[1].T +Room.wallEast.Wall.simpleNLayer.cap[2].T +Room.wallEast.Wall.simpleNLayer.cap[3].T +Room.wallNorth.Wall.simpleNLayer.cap[1].T +Room.wallNorth.Wall.simpleNLayer.cap[2].T +Room.wallNorth.Wall.simpleNLayer.cap[3].T +Room.wallSouth.Wall.simpleNLayer.cap[1].T +Room.wallSouth.Wall.simpleNLayer.cap[2].T +Room.wallSouth.Wall.simpleNLayer.cap[3].T +Room.wallWest.Wall.simpleNLayer.cap[1].T +Room.wallWest.Wall.simpleNLayer.cap[2].T +Room.wallWest.Wall.simpleNLayer.cap[3].T +Finished +Finished + = true + +Declaring variable: Boolean rScript ; + +savelog("AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case650.translation.log"); = true + + +rCheck = checkModel("AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case810"); +Check of AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case810 +The model has the same number of unknowns and equations: 1585 +The model has the same number of unknowns and equations +for the given numerical settings of parameters: 1585 +Check of AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case810 successful. +Declaring variable: Boolean rCheck ; + +Modelica.Utilities.Streams.print(" { \"file\" : \"AixLib/Resources/Scripts/Dymola/ThermalZones/HighOrder/Validation/ASHRAE140/Case810.mos\",", "AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case810.statistics.log"); +Modelica.Utilities.Streams.print(" \"model\" : \"AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case810\",", "AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case810.statistics.log"); +Modelica.Utilities.Streams.print(" \"check\" : {", "AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case810.statistics.log"); +Modelica.Utilities.Streams.print(" \"command\" : \"checkModel(\\\"AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case810\\\");\",", "AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case810.statistics.log"); +Modelica.Utilities.Streams.print(" \"result\" : " + String(rCheck), "AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case810.statistics.log"); +Modelica.Utilities.Streams.print(" },", "AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case810.statistics.log"); + + +rScript=RunScript("modelica://AixLib/Resources/Scripts/Dymola/ThermalZones/HighOrder/Validation/ASHRAE140/Case810.mos"); +simulateModel("AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case810", startTime=0, stopTime=31539600, outputInterval=1800, tolerance=1e-6, method="dassl", resultFile="AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case810"); +Translation of AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case810 +The DAE has 1585 scalar unknowns and 1585 scalar equations. + +Statistics + +Original Model + Number of components: 352 + Variables: 3082 + Constants: 41 (276 scalars) + Parameters: 1493 (2159 scalars) + Unknowns: 1548 (1585 scalars) + Differentiated variables: 25 scalars + Equations: 1257 + Nontrivial: 1045 +Translated Model + Constants: 780 scalars + Free parameters: 876 scalars + Parameter depending: 909 scalars + Outputs: 5 scalars + Continuous time states: 25 scalars + Time-varying variables: 474 scalars + Alias variables: 981 scalars + Number of mixed real/discrete systems of equations: 0 + Sizes of linear systems of equations: {4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 3, 4, 4, 4, 4} + Sizes after manipulation of the linear systems: {0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0} + Sizes of nonlinear systems of equations: {55} + Sizes after manipulation of the nonlinear systems: {13} + Number of numerical Jacobians: 0 + +Selected continuous time states +Statically selected continuous time states +idealHeaterCooler.pITempCool.PI.I.y +idealHeaterCooler.pITempHeat.PI.I.y +integrator2.y +integratorCool.y +integratorHeat.y +Room.airload.dynBal.m +Room.airload.dynBal.medium.Xi[1] +Room.airload.dynBal.U +Room.ceiling.Wall.simpleNLayer.cap[1].T +Room.ceiling.Wall.simpleNLayer.cap[2].T +Room.ceiling.Wall.simpleNLayer.cap[3].T +Room.floor.Wall.simpleNLayer.cap[1].T +Room.floor.Wall.simpleNLayer.cap[2].T +Room.wallEast.Wall.simpleNLayer.cap[1].T +Room.wallEast.Wall.simpleNLayer.cap[2].T +Room.wallEast.Wall.simpleNLayer.cap[3].T +Room.wallNorth.Wall.simpleNLayer.cap[1].T +Room.wallNorth.Wall.simpleNLayer.cap[2].T +Room.wallNorth.Wall.simpleNLayer.cap[3].T +Room.wallSouth.Wall.simpleNLayer.cap[1].T +Room.wallSouth.Wall.simpleNLayer.cap[2].T +Room.wallSouth.Wall.simpleNLayer.cap[3].T +Room.wallWest.Wall.simpleNLayer.cap[1].T +Room.wallWest.Wall.simpleNLayer.cap[2].T +Room.wallWest.Wall.simpleNLayer.cap[3].T +Finished +Finished + = true + +Declaring variable: Boolean rScript ; + +savelog("AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case810.translation.log"); = true + + +rCheck = checkModel("AixLib.ThermalZones.ReducedOrder.Examples.ThermalZone"); +Check of AixLib.ThermalZones.ReducedOrder.Examples.ThermalZone +The model has the same number of unknowns and equations: 1929 +The model could not be deduced to be symbolically well-posed. +The model has + 1777+29*thermalZone.zoneParam.nOrientations+thermalZone.ROM.volAir.dynBal.nPorts +thermalZone.humanSenHeaDependent.productHeatOutput.nu+thermalZone.machinesSenHea.productHeatOutput.nu +thermalZone.lights.productHeatOutput.nu+max([size(internalGains.columns, 1); size(internalGains.offset, 1)]) +scalar unknowns and + 1825+(if weaDat.pAtmSou == AixLib.BoundaryConditions.Types.DataSource.Parameter then 1 else 0)+(if weaDat.TDewPoiSou == AixLib.BoundaryConditions.Types.DataSource. Parameter then 1 else 0)+(if weaDat.TDryBulSou == AixLib.BoundaryConditions.Types.DataSource. Parameter then 1 else 0)+(if weaDat.TBlaSkySou == AixLib.BoundaryConditions.Types.DataSource. Parameter then 1 else 0)+(if weaDat.relHumSou == AixLib.BoundaryConditions.Types.DataSource. Parameter then 1 else 0)+(if weaDat.opaSkyCovSou == AixLib.BoundaryConditions.Types.DataSource. Parameter then 1 else 0)+(if weaDat.ceiHeiSou == AixLib.BoundaryConditions.Types.DataSource. Parameter then 1 else 0)+(if weaDat.totSkyCovSou == AixLib.BoundaryConditions.Types.DataSource. Parameter then 1 else 0)+(if weaDat.winSpeSou == AixLib.BoundaryConditions.Types.DataSource. Parameter then 1 else 0)+(if weaDat.winDirSou == AixLib.BoundaryConditions.Types.DataSource. Parameter then 1 else 0)+(if weaDat.HInfHorSou == AixLib.BoundaryConditions.Types.DataSource. Parameter then 1 else 0)+(if weaDat.HSou == AixLib.BoundaryConditions.Types.RadiationDataSource. Input_HDirNor_HDifHor then 2 else 1)+(if weaDat.HSou == AixLib.BoundaryConditions.Types.RadiationDataSource. Input_HDirNor_HGloHor then 2 else 1)+(if weaDat.HSou == AixLib.BoundaryConditions.Types.RadiationDataSource. Input_HGloHor_HDifHor then 2 else 1)+max([size(internalGains.columns, 1); size (internalGains.offset, 1)])+19*thermalZone.zoneParam.nOrientations+(if not thermalZone.eqAirTempWall.TGroundFromInput then 1 else 0)+(if not thermalZone.ROM.volAir.dynBal.use_mWat_flow then 1 else 0)+3*thermalZone.ROM.volAir.dynBal.nPorts +scalar equations. +However, exploiting the given numerical settings of parameters gives the same number of unknowns and equations: + 1929 +Check of AixLib.ThermalZones.ReducedOrder.Examples.ThermalZone successful. +Declaring variable: Boolean rCheck ; + +Modelica.Utilities.Streams.print(" { \"file\" : \"AixLib/Resources/Scripts/Dymola/ThermalZones/ReducedOrder/Examples/ThermalZone.mos\",", "AixLib.ThermalZones.ReducedOrder.Examples.ThermalZone.statistics.log"); +Modelica.Utilities.Streams.print(" \"model\" : \"AixLib.ThermalZones.ReducedOrder.Examples.ThermalZone\",", "AixLib.ThermalZones.ReducedOrder.Examples.ThermalZone.statistics.log"); +Modelica.Utilities.Streams.print(" \"check\" : {", "AixLib.ThermalZones.ReducedOrder.Examples.ThermalZone.statistics.log"); +Modelica.Utilities.Streams.print(" \"command\" : \"checkModel(\\\"AixLib.ThermalZones.ReducedOrder.Examples.ThermalZone\\\");\",", "AixLib.ThermalZones.ReducedOrder.Examples.ThermalZone.statistics.log"); +Modelica.Utilities.Streams.print(" \"result\" : " + String(rCheck), "AixLib.ThermalZones.ReducedOrder.Examples.ThermalZone.statistics.log"); +Modelica.Utilities.Streams.print(" },", "AixLib.ThermalZones.ReducedOrder.Examples.ThermalZone.statistics.log"); + + +rScript=RunScript("modelica://AixLib/Resources/Scripts/Dymola/ThermalZones/ReducedOrder/Examples/ThermalZone.mos"); +simulateModel("AixLib.ThermalZones.ReducedOrder.Examples.ThermalZone", tolerance=1e-6, stopTime=3.1536e+007, numberOfIntervals=0, outputInterval=3600, method="CVode", resultFile="AixLib.ThermalZones.ReducedOrder.Examples.ThermalZone"); +Translation of AixLib.ThermalZones.ReducedOrder.Examples.ThermalZone +The DAE has 1929 scalar unknowns and 1929 scalar equations. + +Statistics + +Original Model + Number of components: 291 + Variables: 2646 + Constants: 73 (73 scalars) + Parameters: 748 (2557 scalars) + Unknowns: 1825 (1929 scalars) + Differentiated variables: 4 scalars + Equations: 1304 + Nontrivial: 1201 +Translated Model + Constants: 553 scalars + Free parameters: 1936 scalars + Parameter depending: 293 scalars + Continuous time states: 4 scalars + Time-varying variables: 600 scalars + Alias variables: 1177 scalars + Number of mixed real/discrete systems of equations: 0 + Sizes of linear systems of equations: {2, 29, 4} + Sizes after manipulation of the linear systems: {0, 4, 0} + Sizes of nonlinear systems of equations: {1, 1, 1, 1, 1, 1} + Sizes after manipulation of the nonlinear systems: {0, 1, 0, 1, 0, 1} + Number of numerical Jacobians: 0 + Initialization problem + Sizes of linear systems of equations: {32} + Sizes after manipulation of the linear systems: {5} + +Selected continuous time states +Statically selected continuous time states +thermalZone.ROM.extWallRC.thermCapExt[1].T +thermalZone.ROM.intWallRC.thermCapInt[1].T +thermalZone.ROM.volAir.dynBal.m +thermalZone.ROM.volAir.dynBal.U +Finished +Finished + = true + + +Declaring variable: Boolean rScript ; + +savelog("AixLib.ThermalZones.ReducedOrder.Examples.ThermalZone.translation.log"); = true + + +rCheck = checkModel("AixLib.ThermalZones.HighOrder.Validation.EmpiricalValidation.TwinHouseN2"); +Check of AixLib.ThermalZones.HighOrder.Validation.EmpiricalValidation.TwinHouseN2 +The model has the same number of unknowns and equations: 2111 +The model has the same number of unknowns and equations +for the given numerical settings of parameters: 2111 +Check of AixLib.ThermalZones.HighOrder.Validation.EmpiricalValidation.TwinHouseN2 successful. +Declaring variable: Boolean rCheck ; + +Modelica.Utilities.Streams.print(" { \"file\" : \"AixLib/Resources/Scripts/Dymola/ThermalZones/HighOrder/Validation/EmpiricalValidation/TwinHouseN2.mos\",", "AixLib.ThermalZones.HighOrder.Validation.EmpiricalValidation.TwinHouseN2.statistics.log"); +Modelica.Utilities.Streams.print(" \"model\" : \"AixLib.ThermalZones.HighOrder.Validation.EmpiricalValidation.TwinHouseN2\",", "AixLib.ThermalZones.HighOrder.Validation.EmpiricalValidation.TwinHouseN2.statistics.log"); +Modelica.Utilities.Streams.print(" \"check\" : {", "AixLib.ThermalZones.HighOrder.Validation.EmpiricalValidation.TwinHouseN2.statistics.log"); +Modelica.Utilities.Streams.print(" \"command\" : \"checkModel(\\\"AixLib.ThermalZones.HighOrder.Validation.EmpiricalValidation.TwinHouseN2\\\");\",", "AixLib.ThermalZones.HighOrder.Validation.EmpiricalValidation.TwinHouseN2.statistics.log"); +Modelica.Utilities.Streams.print(" \"result\" : " + String(rCheck), "AixLib.ThermalZones.HighOrder.Validation.EmpiricalValidation.TwinHouseN2.statistics.log"); +Modelica.Utilities.Streams.print(" },", "AixLib.ThermalZones.HighOrder.Validation.EmpiricalValidation.TwinHouseN2.statistics.log"); + + +rScript=RunScript("modelica://AixLib/Resources/Scripts/Dymola/ThermalZones/HighOrder/Validation/EmpiricalValidation/TwinHouseN2.mos"); +simulateModel("AixLib.ThermalZones.HighOrder.Validation.EmpiricalValidation.TwinHouseN2", startTime=0, stopTime=3546000, outputInterval=1800, tolerance=1e-6, method="dassl", resultFile="AixLib.ThermalZones.HighOrder.Validation.EmpiricalValidation.TwinHouseN2"); +Translation of AixLib.ThermalZones.HighOrder.Validation.EmpiricalValidation.TwinHouseN2 +The DAE has 2111 scalar unknowns and 2111 scalar equations. +The translated model contains large nonlinear systems of equations. The simulation may run faster in DAE mode. Enable DAE mode by setting the flag Advanced.Define.DAEsolver and use one of the solvers Dassl, Radau IIa, Esdirk*, or Sdirk34hw. + +Statistics + +Original Model + Number of components: 445 + Variables: 3672 + Constants: 10 (10 scalars) + Parameters: 1604 (2228 scalars) + Unknowns: 2058 (2111 scalars) + Differentiated variables: 39 scalars + Equations: 1503 + Nontrivial: 1250 +Translated Model + Constants: 624 scalars + Free parameters: 609 scalars + Parameter depending: 1160 scalars + Outputs: 12 scalars + Continuous time states: 39 scalars + Time-varying variables: 559 scalars + Alias variables: 1397 scalars + Number of mixed real/discrete systems of equations: 0 + Sizes of linear systems of equations: {4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4} + Sizes after manipulation of the linear systems: {0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0} + Sizes of nonlinear systems of equations: {119, 1, 1} + Sizes after manipulation of the nonlinear systems: {33, 0, 1} + Number of numerical Jacobians: 0 + +Selected continuous time states +Statically selected continuous time states +roomTwinHouseN2.airload.dynBal.m +roomTwinHouseN2.airload.dynBal.medium.Xi[1] +roomTwinHouseN2.airload.dynBal.U +roomTwinHouseN2.ceiling.Wall.simpleNLayer.cap[1].T +roomTwinHouseN2.ceiling.Wall.simpleNLayer.cap[2].T +roomTwinHouseN2.ceiling.Wall.simpleNLayer.cap[3].T +roomTwinHouseN2.ceiling.Wall.simpleNLayer.cap[4].T +roomTwinHouseN2.ceiling.Wall.simpleNLayer.cap[5].T +roomTwinHouseN2.floor.Wall.simpleNLayer.cap[1].T +roomTwinHouseN2.floor.Wall.simpleNLayer.cap[2].T +roomTwinHouseN2.floor.Wall.simpleNLayer.cap[3].T +roomTwinHouseN2.floor.Wall.simpleNLayer.cap[4].T +roomTwinHouseN2.floor.Wall.simpleNLayer.cap[5].T +roomTwinHouseN2.IW.Wall.simpleNLayer.cap[1].T +roomTwinHouseN2.IW.Wall.simpleNLayer.cap[2].T +roomTwinHouseN2.IW.Wall.simpleNLayer.cap[3].T +roomTwinHouseN2.IW1.Wall.simpleNLayer.cap[1].T +roomTwinHouseN2.IW1.Wall.simpleNLayer.cap[2].T +roomTwinHouseN2.IW1.Wall.simpleNLayer.cap[3].T +roomTwinHouseN2.wallEast.Wall.simpleNLayer.cap[1].T +roomTwinHouseN2.wallEast.Wall.simpleNLayer.cap[2].T +roomTwinHouseN2.wallEast.Wall.simpleNLayer.cap[3].T +roomTwinHouseN2.wallEast.Wall.simpleNLayer.cap[4].T +roomTwinHouseN2.wallEast.Wall.simpleNLayer.cap[5].T +roomTwinHouseN2.wallNorth.Wall.simpleNLayer.cap[1].T +roomTwinHouseN2.wallNorth.Wall.simpleNLayer.cap[2].T +roomTwinHouseN2.wallNorth.Wall.simpleNLayer.cap[3].T +roomTwinHouseN2.wallNorth.Wall.simpleNLayer.cap[4].T +roomTwinHouseN2.wallNorth.Wall.simpleNLayer.cap[5].T +roomTwinHouseN2.wallSouth.Wall.simpleNLayer.cap[1].T +roomTwinHouseN2.wallSouth.Wall.simpleNLayer.cap[2].T +roomTwinHouseN2.wallSouth.Wall.simpleNLayer.cap[3].T +roomTwinHouseN2.wallSouth.Wall.simpleNLayer.cap[4].T +roomTwinHouseN2.wallSouth.Wall.simpleNLayer.cap[5].T +roomTwinHouseN2.wallWest.Wall.simpleNLayer.cap[1].T +roomTwinHouseN2.wallWest.Wall.simpleNLayer.cap[2].T +roomTwinHouseN2.wallWest.Wall.simpleNLayer.cap[3].T +roomTwinHouseN2.wallWest.Wall.simpleNLayer.cap[4].T +roomTwinHouseN2.wallWest.Wall.simpleNLayer.cap[5].T +Finished +Finished + = true + +Declaring variable: Boolean rScript ; + +savelog("AixLib.ThermalZones.HighOrder.Validation.EmpiricalValidation.TwinHouseN2.translation.log"); = true + + +rCheck = checkModel("AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case900FF"); +Check of AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case900FF +The model has the same number of unknowns and equations: 1431 +The model has the same number of unknowns and equations +for the given numerical settings of parameters: 1431 +Check of AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case900FF successful. +Declaring variable: Boolean rCheck ; + +Modelica.Utilities.Streams.print(" { \"file\" : \"AixLib/Resources/Scripts/Dymola/ThermalZones/HighOrder/Validation/ASHRAE140/Case900FF.mos\",", "AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case900FF.statistics.log"); +Modelica.Utilities.Streams.print(" \"model\" : \"AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case900FF\",", "AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case900FF.statistics.log"); +Modelica.Utilities.Streams.print(" \"check\" : {", "AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case900FF.statistics.log"); +Modelica.Utilities.Streams.print(" \"command\" : \"checkModel(\\\"AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case900FF\\\");\",", "AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case900FF.statistics.log"); +Modelica.Utilities.Streams.print(" \"result\" : " + String(rCheck), "AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case900FF.statistics.log"); +Modelica.Utilities.Streams.print(" },", "AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case900FF.statistics.log"); + + +rScript=RunScript("modelica://AixLib/Resources/Scripts/Dymola/ThermalZones/HighOrder/Validation/ASHRAE140/Case900FF.mos"); +simulateModel("AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case900FF", startTime=0, stopTime=31539600, outputInterval=1800, tolerance=1e-6, method="dassl", resultFile="AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case900FF"); +Translation of AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case900FF +The DAE has 1431 scalar unknowns and 1431 scalar equations. + +Statistics + +Original Model + Number of components: 300 + Variables: 2699 + Constants: 39 (274 scalars) + Parameters: 1266 (1927 scalars) + Unknowns: 1394 (1431 scalars) + Differentiated variables: 21 scalars + Equations: 1103 + Nontrivial: 901 +Translated Model + Constants: 714 scalars + Free parameters: 720 scalars + Parameter depending: 873 scalars + Outputs: 3 scalars + Continuous time states: 21 scalars + Time-varying variables: 434 scalars + Alias variables: 891 scalars + Number of mixed real/discrete systems of equations: 0 + Sizes of linear systems of equations: {4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 4, 3, 4, 4, 4, 4} + Sizes after manipulation of the linear systems: {0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0} + Sizes of nonlinear systems of equations: {55} + Sizes after manipulation of the nonlinear systems: {13} + Number of numerical Jacobians: 0 + +Selected continuous time states +Statically selected continuous time states +integrator2.y +Room.airload.dynBal.m +Room.airload.dynBal.medium.Xi[1] +Room.airload.dynBal.U +Room.ceiling.Wall.simpleNLayer.cap[1].T +Room.ceiling.Wall.simpleNLayer.cap[2].T +Room.ceiling.Wall.simpleNLayer.cap[3].T +Room.floor.Wall.simpleNLayer.cap[1].T +Room.floor.Wall.simpleNLayer.cap[2].T +Room.wallEast.Wall.simpleNLayer.cap[1].T +Room.wallEast.Wall.simpleNLayer.cap[2].T +Room.wallEast.Wall.simpleNLayer.cap[3].T +Room.wallNorth.Wall.simpleNLayer.cap[1].T +Room.wallNorth.Wall.simpleNLayer.cap[2].T +Room.wallNorth.Wall.simpleNLayer.cap[3].T +Room.wallSouth.Wall.simpleNLayer.cap[1].T +Room.wallSouth.Wall.simpleNLayer.cap[2].T +Room.wallSouth.Wall.simpleNLayer.cap[3].T +Room.wallWest.Wall.simpleNLayer.cap[1].T +Room.wallWest.Wall.simpleNLayer.cap[2].T +Room.wallWest.Wall.simpleNLayer.cap[3].T +Finished +Finished + = true + +Declaring variable: Boolean rScript ; + +savelog("AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case900FF.translation.log"); \ No newline at end of file diff --git a/docs/correct_HTML_issue1147_GenericBoiler/regression/ThermalZones/unitTests-dymola.log b/docs/correct_HTML_issue1147_GenericBoiler/regression/ThermalZones/unitTests-dymola.log new file mode 100644 index 0000000000..95e99c55ce --- /dev/null +++ b/docs/correct_HTML_issue1147_GenericBoiler/regression/ThermalZones/unitTests-dymola.log @@ -0,0 +1,12 @@ +Regression tests are only run for the following package: + AixLib.ThermalZones +*** Error: Model 'AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case300' failed: TimeoutExpired: Command '['dymola', 'run_AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case300.mos', '/nowindow']' timed out after 300 seconds +*** Error: Model 'AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case620' failed: TimeoutExpired: Command '['dymola', 'run_AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case620.mos', '/nowindow']' timed out after 300 seconds +*** Error: Simulation failed for 'dymola run_AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case300.mos /nowindow'. +*** Error: Simulation failed for 'dymola run_AixLib.ThermalZones.HighOrder.Validation.ASHRAE140.Case620.mos /nowindow'. +Comparison files output by funnel are stored in the directory 'funnel_comp' of size 3.1 MB. +Run 'python -c "import buildingspy.development.regressiontest as t; t.Tester(tool=\"dymola\").report()"' +to access a summary of the comparison results. + +Script that runs unit tests had 0 warnings and 4 errors. +