Running: ./testmodel.py --libraries=/home/hudson/saved_omc/libraries/.openmodelica/libraries --ompython_omhome=/usr ThermoSysPro_ThermoSysPro.Examples.SimpleExamples.TestNTUWaterHeating2.conf.json
loadFile("/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermoSysPro 4.0.0-master/package.mo", uses=false)
Using package ThermoSysPro with version 4.0 (/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermoSysPro 4.0.0-master/package.mo)
Running command: translateModel(ThermoSysPro.Examples.SimpleExamples.TestNTUWaterHeating2,tolerance=1e-06,outputFormat="empty",numberOfIntervals=5000,variableFilter="",fileNamePrefix="ThermoSysPro_ThermoSysPro.Examples.SimpleExamples.TestNTUWaterHeating2")
translateModel(ThermoSysPro.Examples.SimpleExamples.TestNTUWaterHeating2,tolerance=1e-06,outputFormat="empty",numberOfIntervals=5000,variableFilter="",fileNamePrefix="ThermoSysPro_ThermoSysPro.Examples.SimpleExamples.TestNTUWaterHeating2")
Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermoSysPro 4.0.0-master/package.mo): time 0.8305/0.8305, allocations: 150.9 MB / 167.2 MB, free: 14.48 MB / 142.1 MB
Notification: Performance of FrontEnd - loaded program: time 0.0003656/0.0003656, allocations: 20.39 kB / 237.8 MB, free: 1.77 MB / 190.1 MB
Notification: Performance of FrontEnd - Absyn->SCode: time 0.05756/0.05794, allocations: 31.34 MB / 269.1 MB, free: 7.016 MB / 222.1 MB
Notification: Automatically loaded package Complex 4.0.0 due to uses annotation from Modelica.
Notification: Automatically loaded package ModelicaServices 4.0.0 due to uses annotation from Modelica.
Notification: Automatically loaded package Modelica 4.0.0 due to usage.
Notification: Performance of NFInst.instantiate(ThermoSysPro.Examples.SimpleExamples.TestNTUWaterHeating2): time 1.664/1.722, allocations: 302.3 MB / 0.5581 GB, free: 5.691 MB / 446.1 MB
Notification: Performance of NFInst.instExpressions: time 0.04496/1.767, allocations: 38.09 MB / 0.5953 GB, free: 15.45 MB / 494.1 MB
Notification: Performance of NFInst.updateImplicitVariability: time 0.001265/1.768, allocations: 12 kB / 0.5953 GB, free: 15.44 MB / 494.1 MB
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermoSysPro 4.0.0-master/WaterSteam/BoundaryConditions/SourcePQ.mo:29:3-30:52:writable] Warning: Connector C is not balanced: The number of potential variables (4) is not equal to the number of flow variables (0).
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermoSysPro 4.0.0-master/WaterSteam/BoundaryConditions/Sink.mo:17:3-19:16:writable] Warning: Connector C is not balanced: The number of potential variables (4) is not equal to the number of flow variables (0).
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermoSysPro 4.0.0-master/WaterSteam/BoundaryConditions/SourceP.mo:30:3-31:45:writable] Warning: Connector C is not balanced: The number of potential variables (4) is not equal to the number of flow variables (0).
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermoSysPro 4.0.0-master/WaterSteam/PressureLosses/SingularPressureLoss.mo:25:3-27:16:writable] Warning: Connector C1 is not balanced: The number of potential variables (4) is not equal to the number of flow variables (0).
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermoSysPro 4.0.0-master/WaterSteam/PressureLosses/SingularPressureLoss.mo:28:3-29:52:writable] Warning: Connector C2 is not balanced: The number of potential variables (4) is not equal to the number of flow variables (0).
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermoSysPro 4.0.0-master/WaterSteam/PressureLosses/SingularPressureLoss.mo:25:3-27:16:writable] Warning: Connector C1 is not balanced: The number of potential variables (4) is not equal to the number of flow variables (0).
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermoSysPro 4.0.0-master/WaterSteam/PressureLosses/SingularPressureLoss.mo:28:3-29:52:writable] Warning: Connector C2 is not balanced: The number of potential variables (4) is not equal to the number of flow variables (0).
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermoSysPro 4.0.0-master/WaterSteam/BoundaryConditions/Sink.mo:17:3-19:16:writable] Warning: Connector C is not balanced: The number of potential variables (4) is not equal to the number of flow variables (0).
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermoSysPro 4.0.0-master/WaterSteam/PressureLosses/SingularPressureLoss.mo:25:3-27:16:writable] Warning: Connector C1 is not balanced: The number of potential variables (4) is not equal to the number of flow variables (0).
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermoSysPro 4.0.0-master/WaterSteam/PressureLosses/SingularPressureLoss.mo:28:3-29:52:writable] Warning: Connector C2 is not balanced: The number of potential variables (4) is not equal to the number of flow variables (0).
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermoSysPro 4.0.0-master/WaterSteam/PressureLosses/SingularPressureLoss.mo:25:3-27:16:writable] Warning: Connector C1 is not balanced: The number of potential variables (4) is not equal to the number of flow variables (0).
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermoSysPro 4.0.0-master/WaterSteam/PressureLosses/SingularPressureLoss.mo:28:3-29:52:writable] Warning: Connector C2 is not balanced: The number of potential variables (4) is not equal to the number of flow variables (0).
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermoSysPro 4.0.0-master/WaterSteam/HeatExchangers/NTUWaterHeating.mo:65:3-67:38:writable] Warning: Connector Ee is not balanced: The number of potential variables (4) is not equal to the number of flow variables (0).
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermoSysPro 4.0.0-master/WaterSteam/HeatExchangers/NTUWaterHeating.mo:68:3-70:36:writable] Warning: Connector Se is not balanced: The number of potential variables (4) is not equal to the number of flow variables (0).
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermoSysPro 4.0.0-master/WaterSteam/HeatExchangers/NTUWaterHeating.mo:71:3-73:37:writable] Warning: Connector Ep is not balanced: The number of potential variables (4) is not equal to the number of flow variables (0).
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermoSysPro 4.0.0-master/WaterSteam/HeatExchangers/NTUWaterHeating.mo:74:3-76:38:writable] Warning: Connector Sp is not balanced: The number of potential variables (4) is not equal to the number of flow variables (0).
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermoSysPro 4.0.0-master/WaterSteam/HeatExchangers/NTUWaterHeating.mo:77:3-79:36:writable] Warning: Connector Ev is not balanced: The number of potential variables (4) is not equal to the number of flow variables (0).
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermoSysPro 4.0.0-master/WaterSteam/PressureLosses/SingularPressureLoss.mo:25:3-27:16:writable] Warning: Connector C1 is not balanced: The number of potential variables (4) is not equal to the number of flow variables (0).
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermoSysPro 4.0.0-master/WaterSteam/PressureLosses/SingularPressureLoss.mo:28:3-29:52:writable] Warning: Connector C2 is not balanced: The number of potential variables (4) is not equal to the number of flow variables (0).
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermoSysPro 4.0.0-master/WaterSteam/BoundaryConditions/SourcePQ.mo:29:3-30:52:writable] Warning: Connector C is not balanced: The number of potential variables (4) is not equal to the number of flow variables (0).
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermoSysPro 4.0.0-master/WaterSteam/HeatExchangers/NTUWaterHeating.mo:65:3-67:38:writable] Warning: Connector Ee is not balanced: The number of potential variables (4) is not equal to the number of flow variables (0).
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermoSysPro 4.0.0-master/WaterSteam/HeatExchangers/NTUWaterHeating.mo:68:3-70:36:writable] Warning: Connector Se is not balanced: The number of potential variables (4) is not equal to the number of flow variables (0).
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermoSysPro 4.0.0-master/WaterSteam/HeatExchangers/NTUWaterHeating.mo:71:3-73:37:writable] Warning: Connector Ep is not balanced: The number of potential variables (4) is not equal to the number of flow variables (0).
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermoSysPro 4.0.0-master/WaterSteam/HeatExchangers/NTUWaterHeating.mo:74:3-76:38:writable] Warning: Connector Sp is not balanced: The number of potential variables (4) is not equal to the number of flow variables (0).
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermoSysPro 4.0.0-master/WaterSteam/HeatExchangers/NTUWaterHeating.mo:77:3-79:36:writable] Warning: Connector Ev is not balanced: The number of potential variables (4) is not equal to the number of flow variables (0).
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermoSysPro 4.0.0-master/WaterSteam/BoundaryConditions/SourceP.mo:30:3-31:45:writable] Warning: Connector C is not balanced: The number of potential variables (4) is not equal to the number of flow variables (0).
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermoSysPro 4.0.0-master/WaterSteam/PressureLosses/SingularPressureLoss.mo:25:3-27:16:writable] Warning: Connector C1 is not balanced: The number of potential variables (4) is not equal to the number of flow variables (0).
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermoSysPro 4.0.0-master/WaterSteam/PressureLosses/SingularPressureLoss.mo:28:3-29:52:writable] Warning: Connector C2 is not balanced: The number of potential variables (4) is not equal to the number of flow variables (0).
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermoSysPro 4.0.0-master/WaterSteam/PressureLosses/SingularPressureLoss.mo:25:3-27:16:writable] Warning: Connector C1 is not balanced: The number of potential variables (4) is not equal to the number of flow variables (0).
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermoSysPro 4.0.0-master/WaterSteam/PressureLosses/SingularPressureLoss.mo:28:3-29:52:writable] Warning: Connector C2 is not balanced: The number of potential variables (4) is not equal to the number of flow variables (0).
Notification: Performance of NFTyping.typeComponents: time 0.001158/1.77, allocations: 485.5 kB / 0.5957 GB, free: 14.96 MB / 494.1 MB
Notification: Performance of NFTyping.typeBindings: time 0.002241/1.772, allocations: 1.06 MB / 0.5968 GB, free: 13.9 MB / 494.1 MB
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermoSysPro 4.0.0-master/Properties/WaterSteam/IF97_packages.mo:783:9-783:27:writable] Warning: cv was used before it was defined (given a value). Additional such uses may exist for the variable, but some messages were suppressed.
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermoSysPro 4.0.0-master/Properties/WaterSteam/IF97_packages.mo:850:9-850:27:writable] Warning: cv was used before it was defined (given a value). Additional such uses may exist for the variable, but some messages were suppressed.
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermoSysPro 4.0.0-master/Properties/WaterSteam/IF97_packages.mo:1088:9-1088:27:writable] Warning: cv was used before it was defined (given a value). Additional such uses may exist for the variable, but some messages were suppressed.
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermoSysPro 4.0.0-master/Properties/WaterSteamSimple/prop4_Ph.mo:69:3-69:60:writable] Warning: dh1satp was used before it was defined (given a value). Additional such uses may exist for the variable, but some messages were suppressed.
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermoSysPro 4.0.0-master/Properties/WaterSteamSimple/prop4_Ph.mo:69:3-69:60:writable] Warning: dh2satp was used before it was defined (given a value). Additional such uses may exist for the variable, but some messages were suppressed.
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermoSysPro 4.0.0-master/Properties/WaterSteamSimple/prop4_Ph_der.mo:167:3-170:49:writable] Warning: du1satp_der was used before it was defined (given a value). Additional such uses may exist for the variable, but some messages were suppressed.
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermoSysPro 4.0.0-master/Properties/WaterSteamSimple/prop4_Ph_der.mo:167:3-170:49:writable] Warning: du2satp_der was used before it was defined (given a value). Additional such uses may exist for the variable, but some messages were suppressed.
Notification: Performance of NFTyping.typeClassSections: time 0.02515/1.797, allocations: 10.62 MB / 0.6071 GB, free: 3.258 MB / 494.1 MB
Notification: Performance of NFFlatten.flatten: time 0.003469/1.801, allocations: 3.02 MB / 0.6101 GB, free: 228 kB / 494.1 MB
Notification: Performance of NFFlatten.resolveConnections: time 0.0009822/1.801, allocations: 0.8626 MB / 0.6109 GB, free: 15.34 MB / 0.4981 GB
Notification: Performance of NFEvalConstants.evaluate: time 0.001376/1.803, allocations: 1.14 MB / 0.6121 GB, free: 14.19 MB / 0.4981 GB
Notification: Performance of NFSimplifyModel.simplify: time 0.0009447/1.804, allocations: 0.9329 MB / 0.613 GB, free: 13.25 MB / 0.4981 GB
Notification: Performance of NFPackage.collectConstants: time 0.0001954/1.804, allocations: 148 kB / 0.6131 GB, free: 13.11 MB / 0.4981 GB
Notification: Performance of NFFlatten.collectFunctions: time 0.02771/1.832, allocations: 16.04 MB / 0.6288 GB, free: 13.05 MB / 0.5137 GB
Notification: Performance of NFScalarize.scalarize: time 0.0004508/1.832, allocations: 362.4 kB / 0.6291 GB, free: 12.7 MB / 0.5137 GB
Notification: Performance of NFVerifyModel.verify: time 0.001425/1.834, allocations: 1.076 MB / 0.6302 GB, free: 11.62 MB / 0.5137 GB
Notification: Performance of NFConvertDAE.convert: time 0.02048/1.854, allocations: 9.974 MB / 0.6399 GB, free: 1.613 MB / 0.5137 GB
Notification: Performance of FrontEnd - DAE generated: time 6.743e-06/1.854, allocations: 0 / 0.6399 GB, free: 1.613 MB / 0.5137 GB
Notification: Performance of FrontEnd: time 1.734e-06/1.854, allocations: 0 / 0.6399 GB, free: 1.613 MB / 0.5137 GB
Notification: Performance of Transformations before backend: time 8.642e-05/1.854, allocations: 0 / 0.6399 GB, free: 1.613 MB / 0.5137 GB
Notification: Model statistics after passing the front-end and creating the data structures used by the back-end:
 * Number of equations: 686
 * Number of variables: 686
Notification: Performance of Generate backend data structure: time 0.007649/1.862, allocations: 3.12 MB / 0.6429 GB, free: 14.42 MB / 0.5294 GB
Notification: Performance of prepare preOptimizeDAE: time 5.187e-05/1.862, allocations: 8.031 kB / 0.643 GB, free: 14.41 MB / 0.5294 GB
Notification: Performance of preOpt normalInlineFunction (simulation): time 0.0004302/1.862, allocations: 230.3 kB / 0.6432 GB, free: 14.19 MB / 0.5294 GB
Notification: Performance of preOpt evaluateParameters (simulation): time 0.0009598/1.863, allocations: 0.6665 MB / 0.6438 GB, free: 13.48 MB / 0.5294 GB
Notification: Performance of preOpt simplifyIfEquations (simulation): time 0.0003236/1.864, allocations: 328.2 kB / 0.6441 GB, free: 13.11 MB / 0.5294 GB
Notification: Performance of preOpt expandDerOperator (simulation): time 0.0001623/1.864, allocations: 124 kB / 0.6443 GB, free: 12.98 MB / 0.5294 GB
Notification: Performance of preOpt clockPartitioning (simulation): time 0.003235/1.867, allocations: 2.313 MB / 0.6465 GB, free: 10.53 MB / 0.5294 GB
Notification: Performance of preOpt findStateOrder (simulation): time 3.062e-05/1.867, allocations: 3.938 kB / 0.6465 GB, free: 10.53 MB / 0.5294 GB
Notification: Performance of preOpt replaceEdgeChange (simulation): time 0.0001009/1.867, allocations: 56 kB / 0.6466 GB, free: 10.47 MB / 0.5294 GB
Notification: Performance of preOpt inlineArrayEqn (simulation): time 0.0001065/1.867, allocations: 131.8 kB / 0.6467 GB, free: 10.34 MB / 0.5294 GB
Notification: Performance of preOpt removeEqualRHS (simulation): time 0.002422/1.87, allocations: 1.713 MB / 0.6484 GB, free: 8.621 MB / 0.5294 GB
Warning: The model contains alias variables with redundant start and/or conflicting nominal values. It is recommended to resolve the conflicts, because otherwise the system could be hard to solve. To print the conflicting alias sets and the chosen candidates please use -d=aliasConflicts.
Notification: Performance of preOpt removeSimpleEquations (simulation): time 0.008845/1.879, allocations: 10.01 MB / 0.6581 GB, free: 13.79 MB / 0.545 GB
Notification: Performance of preOpt comSubExp (simulation): time 0.002016/1.881, allocations: 1.504 MB / 0.6596 GB, free: 12.27 MB / 0.545 GB
Notification: Performance of preOpt resolveLoops (simulation): time 0.001484/1.882, allocations: 1.275 MB / 0.6609 GB, free: 11 MB / 0.545 GB
Notification: Performance of preOpt evalFunc (simulation): time 0.3807/2.263, allocations: 81.02 MB / 0.74 GB, free: 196.2 MB / 0.5919 GB
Notification: Performance of preOpt encapsulateWhenConditions (simulation): time 3.809e-05/2.263, allocations: 43.88 kB / 0.74 GB, free: 196.2 MB / 0.5919 GB
Notification: Performance of pre-optimization done (n=452): time 4.619e-06/2.263, allocations: 0 / 0.74 GB, free: 196.2 MB / 0.5919 GB
Notification: Performance of matching and sorting (n=452): time 0.02298/2.286, allocations: 8.504 MB / 0.7483 GB, free: 194.3 MB / 0.5919 GB
Notification: Performance of inlineWhenForInitialization (initialization): time 2.445e-05/2.286, allocations: 60.22 kB / 0.7484 GB, free: 194.2 MB / 0.5919 GB
Notification: Performance of selectInitializationVariablesDAE (initialization): time 0.0006779/2.287, allocations: 0.6476 MB / 0.749 GB, free: 194 MB / 0.5919 GB
Notification: Performance of collectPreVariables (initialization): time 8.148e-05/2.287, allocations: 41.02 kB / 0.7491 GB, free: 194 MB / 0.5919 GB
Notification: Performance of collectInitialEqns (initialization): time 0.0002331/2.287, allocations: 475.5 kB / 0.7495 GB, free: 193.7 MB / 0.5919 GB
Notification: Performance of collectInitialBindings (initialization): time 0.0007575/2.288, allocations: 1.5 MB / 0.751 GB, free: 192.8 MB / 0.5919 GB
Notification: Performance of simplifyInitialFunctions (initialization): time 0.0004107/2.288, allocations: 367 kB / 0.7513 GB, free: 192.7 MB / 0.5919 GB
Notification: Performance of setup shared object (initialization): time 7.836e-05/2.288, allocations: 353 kB / 0.7517 GB, free: 192.4 MB / 0.5919 GB
Notification: Performance of preBalanceInitialSystem (initialization): time 0.001117/2.289, allocations: 0.9213 MB / 0.7526 GB, free: 192.3 MB / 0.5919 GB
Notification: Performance of partitionIndependentBlocks (initialization): time 0.001268/2.291, allocations: 1.304 MB / 0.7538 GB, free: 191.8 MB / 0.5919 GB
Notification: Performance of analyzeInitialSystem (initialization): time 0.002626/2.293, allocations: 2.559 MB / 0.7563 GB, free: 191.2 MB / 0.5919 GB
Notification: Performance of solveInitialSystemEqSystem (initialization): time 8.015e-06/2.293, allocations: 3.844 kB / 0.7563 GB, free: 191.2 MB / 0.5919 GB
Notification: Performance of matching and sorting (n=484) (initialization): time 0.004516/2.298, allocations: 3.635 MB / 0.7599 GB, free: 189.9 MB / 0.5919 GB
Notification: Performance of prepare postOptimizeDAE: time 2.194e-05/2.298, allocations: 7.562 kB / 0.7599 GB, free: 189.9 MB / 0.5919 GB
Notification: Performance of postOpt simplifyComplexFunction (initialization): time 2.497e-05/2.298, allocations: 10.38 kB / 0.7599 GB, free: 189.9 MB / 0.5919 GB
Notification: Performance of postOpt tearingSystem (initialization): time 0.007669/2.306, allocations: 5.879 MB / 0.7656 GB, free: 184.3 MB / 0.5919 GB
Notification: Performance of postOpt solveSimpleEquations (initialization): time 0.0001705/2.306, allocations: 49.86 kB / 0.7657 GB, free: 184.3 MB / 0.5919 GB
Notification: Performance of postOpt calculateStrongComponentJacobians (initialization): time 0.004997/2.311, allocations: 5.522 MB / 0.7711 GB, free: 178.6 MB / 0.5919 GB
Notification: Performance of postOpt simplifyAllExpressions (initialization): time 0.0008702/2.312, allocations: 269.8 kB / 0.7713 GB, free: 178.4 MB / 0.5919 GB
Notification: Performance of postOpt collapseArrayExpressions (initialization): time 9.181e-05/2.312, allocations: 51.98 kB / 0.7714 GB, free: 178.4 MB / 0.5919 GB
Notification: Model statistics after passing the back-end for initialization:
 * Number of independent subsystems: 35
 * Number of states: 0 ()
 * Number of discrete variables: 30 (singularPressureLoss7.C2.b,singularPressureLoss7.C1.a,singularPressureLoss6.C2.b,singularPressureLoss6.C1.a,sourceP1.C.b,nTUWaterHeating1.Ev.a,nTUWaterHeating1.Sp.b,nTUWaterHeating1.Ep.a,nTUWaterHeating1.Se.b,nTUWaterHeating1.Ee.a,Source_condenseur1.C.b,singularPressureLoss1.C2.b,singularPressureLoss1.C1.a,nTUWaterHeating.Ev.a,nTUWaterHeating.Sp.b,nTUWaterHeating.Ep.a,nTUWaterHeating.Se.b,nTUWaterHeating.Ee.a,singularPressureLoss5.C2.b,singularPressureLoss5.C1.a,singularPressureLoss4.C2.b,singularPressureLoss4.C1.a,Puit_condenseur1.C.a,singularPressureLoss3.C2.b,singularPressureLoss3.C1.a,singularPressureLoss2.C2.b,singularPressureLoss2.C1.a,sourceP.C.b,Puit_condenseur.C.a,Source_condenseur.C.b)
 * Number of discrete states: 0 ()
 * Number of clocked states: 0 ()
 * Top-level inputs: 0
Notification: Strong component statistics for initialization (55):
 * Single equations (assignments): 36
 * Array equations: 0
 * Algorithm blocks: 0
 * Record equations: 14
 * When equations: 0
 * If-equations: 0
 * Equation systems (not torn): 0
 * Torn equation systems: 5
 * Mixed (continuous/discrete) equation systems: 0
Notification: Torn system details for strict tearing set:
 * Linear torn systems (#iteration vars, #inner vars, density): 0 systems
 * Non-linear torn systems (#iteration vars, #inner vars): 5 systems
   {(1,3), (1,3), (1,3), (1,3), (21,38)}
Notification: Performance of prepare postOptimizeDAE: time 0.0005983/2.312, allocations: 332.5 kB / 0.7717 GB, free: 178.1 MB / 0.5919 GB
Notification: Performance of postOpt lateInlineFunction (simulation): time 0.0001751/2.313, allocations: 176.7 kB / 0.7719 GB, free: 177.9 MB / 0.5919 GB
Notification: Performance of postOpt wrapFunctionCalls (simulation): time 0.00531/2.318, allocations: 5.44 MB / 0.7772 GB, free: 172.4 MB / 0.5919 GB
Notification: Performance of postOpt simplifysemiLinear (simulation): time 1.181e-05/2.318, allocations: 14.72 kB / 0.7772 GB, free: 172.4 MB / 0.5919 GB
Notification: Performance of postOpt simplifyComplexFunction (simulation): time 1.112e-05/2.318, allocations: 0.5625 kB / 0.7772 GB, free: 172.4 MB / 0.5919 GB
Notification: Performance of postOpt removeConstants (simulation): time 0.0005388/2.319, allocations: 490.2 kB / 0.7777 GB, free: 172 MB / 0.5919 GB
Notification: Performance of postOpt simplifyTimeIndepFuncCalls (simulation): time 0.0001201/2.319, allocations: 39.05 kB / 0.7777 GB, free: 171.9 MB / 0.5919 GB
Notification: Performance of postOpt simplifyAllExpressions (simulation): time 0.0005655/2.319, allocations: 35.97 kB / 0.7777 GB, free: 171.9 MB / 0.5919 GB
Notification: Performance of postOpt findZeroCrossings (simulation): time 0.0001661/2.319, allocations: 68.91 kB / 0.7778 GB, free: 171.8 MB / 0.5919 GB
[/var/lib/jenkins1/ws/OpenModelicaLibraryTestingWork/OpenModelica/OMCompiler/Compiler/BackEnd/DAEMode.mo:528:7-530:90:writable] Error: Internal error DAEMode.traverserStrongComponents failed on equation:
1/1 (10): ThermoSysPro.Properties.WaterSteam.Common.ThermoProperties_ph(nTUWaterHeating.promeF.T, nTUWaterHeating.rho, nTUWaterHeating.promeF.u, nTUWaterHeating.promeF.s, nTUWaterHeating.promeF.cp, nTUWaterHeating.promeF.ddhp, nTUWaterHeating.promeF.ddph, nTUWaterHeating.promeF.duph, nTUWaterHeating.promeF.duhp, nTUWaterHeating.promeF.x) = $cse15

Variables:
1: singularPressureLoss3.deltaP:VARIABLE(unit = "Pa" )  "Singular pressure loss" type: Real
2: nTUWaterHeating.lsatC.cv:VARIABLE(unit = "J/(kg.K)" )  "Specific heat capacity at constant volume" type: Real
3: nTUWaterHeating.lsatC.P:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 )  "Pressure" type: Real
4: nTUWaterHeating.lsatC.pt:VARIABLE()  "Derivative of pressure wrt. temperature" type: Real
5: nTUWaterHeating.lsatC.cp:VARIABLE(unit = "J/(kg.K)" )  "Specific heat capacity at constant pressure" type: Real
6: nTUWaterHeating.vsatC.rho:VARIABLE(min = 0.0 unit = "kg/m3" )  "Density" type: Real
7: nTUWaterHeating.vsatC.pt:VARIABLE()  "Derivative of pressure wrt. temperature" type: Real
8: nTUWaterHeating.vsatC.cv:VARIABLE(unit = "J/(kg.K)" )  "Specific heat capacity at constant volume" type: Real
9: nTUWaterHeating.TsatC:VARIABLE(min = 0.0 start = 400.0 unit = "K" nominal = 300.0 )  "Saturation temperature" type: Real
10: nTUWaterHeating.HsatvC:VARIABLE(min = 0.0 start = 2.5e6 unit = "J/kg" )  "Saturation specific enthalpy of the vapor at the pressure of the vapor inlet" type: Real
[/var/lib/jenkins1/ws/OpenModelicaLibraryTestingWork/OpenModelica/OMCompiler/Compiler/BackEnd/DAEMode.mo:528:7-530:90:writable] Error: Internal error DAEMode.traverserStrongComponents failed on equation:
1/1 (1): 0.0 = if singularPressureLoss7.Q > 0.0 then singularPressureLoss7.h - nTUWaterHeating.h else singularPressureLoss7.h - nTUWaterHeating1.h
2/2 (10): nTUWaterHeating1.flashepC = ThermoSysPro.Properties.WaterSteam.IF97.Water_Ph(nTUWaterHeating1.P, singularPressureLoss7.h, nTUWaterHeating1.mode_flash)
3/12 (1): nTUWaterHeating1.Wflash = if nTUWaterHeating1.flashepC.x > 0.0 then singularPressureLoss7.Q * (singularPressureLoss7.h - nTUWaterHeating1.HsateC) else 0.0
4/13 (14): (ThermoSysPro.Properties.WaterSteam.Common.PropThermoSat(nTUWaterHeating1.lsatC.P, nTUWaterHeating1.TsatC, nTUWaterHeating1.lsatC.rho, nTUWaterHeating1.HsateC, nTUWaterHeating1.lsatC.cp, nTUWaterHeating1.lsatC.pt, nTUWaterHeating1.lsatC.cv), ThermoSysPro.Properties.WaterSteam.Common.PropThermoSat(nTUWaterHeating1.vsatC.P, nTUWaterHeating1.vsatC.T, nTUWaterHeating1.vsatC.rho, nTUWaterHeating1.HsatvC, nTUWaterHeating1.vsatC.cp, nTUWaterHeating1.vsatC.pt, nTUWaterHeating1.vsatC.cv)) = ThermoSysPro.Properties.WaterSteam.IF97.Water_sat_P(nTUWaterHeating1.P)
5/27 (1): nTUWaterHeating1.Wcond = Source_condenseur.Q0 * nTUWaterHeating1.promcF.cp * $cse10 * (nTUWaterHeating1.TsatC - nTUWaterHeating1.TeiF)
6/28 (1): $cse10 = ThermoSysPro.Correlations.Thermal.WBHeatExchangerEfficiency(singularPressureLoss6.Q, Source_condenseur.Q0, 1e20, nTUWaterHeating1.promcF.cp, nTUWaterHeating1.KCond, nTUWaterHeating1.SCondDes - 1e-9, 0.5)
7/29 (1): $cse4 = ThermoSysPro.Functions.ThermoSquare(singularPressureLoss6.Q, singularPressureLoss6.eps)
8/30 (1): singularPressureLoss6.deltaP = singularPressureLoss6.K * $cse4 / singularPressureLoss6.rho
9/31 (10): $cse3 = ThermoSysPro.Properties.Fluid.Ph(singularPressureLoss6.Pm, singularPressureLoss6.h, singularPressureLoss6.mode, singularPressureLoss6.fluid)
10/41 (10): ThermoSysPro.Properties.WaterSteam.Common.ThermoProperties_ph(singularPressureLoss6.T, singularPressureLoss6.rho, singularPressureLoss6.pro.u, singularPressureLoss6.pro.s, singularPressureLoss6.pro.cp, singularPressureLoss6.pro.ddhp, singularPressureLoss6.pro.ddph, singularPressureLoss6.pro.duph, singularPressureLoss6.pro.duhp, singularPressureLoss6.pro.x) = $cse3
11/51 (1): nTUWaterHeating1.Wcond = if noEvent(singularPressureLoss6.h < nTUWaterHeating1.HsatvC) then singularPressureLoss6.Q * (singularPressureLoss6.h - nTUWaterHeating1.HsateC) + nTUWaterHeating1.Wflash else singularPressureLoss6.Q * (nTUWaterHeating1.HsatvC - nTUWaterHeating1.HsateC) + nTUWaterHeating1.Wflash
12/52 (1): 0.0 = if singularPressureLoss6.Q > 0.0 then singularPressureLoss6.h - sourceP1.h0 else singularPressureLoss6.h - nTUWaterHeating1.h
13/53 (1): 0.0 = if singularPressureLoss5.Q > 0.0 then singularPressureLoss5.h - nTUWaterHeating1.h else singularPressureLoss5.h - Puit_condenseur1.h0
14/54 (10): nTUWaterHeating1.prompC = ThermoSysPro.Properties.WaterSteam.IF97.Water_Ph(nTUWaterHeating1.P, 0.5 * (nTUWaterHeating1.Hep + singularPressureLoss5.h), nTUWaterHeating1.mode_spC)
15/64 (1): $cse8 = min(singularPressureLoss5.Q * nTUWaterHeating1.prompC.cp, Source_condenseur.Q0 * nTUWaterHeating1.prompF.cp)
16/65 (10): $cse6 = ThermoSysPro.Properties.WaterSteam.IF97.Water_Ph(singularPressureLoss2.C2.P, nTUWaterHeating1.HeiF, nTUWaterHeating1.mode_eeF)
17/75 (10): ThermoSysPro.Properties.WaterSteam.Common.ThermoProperties_ph(nTUWaterHeating1.TeiF, nTUWaterHeating1.proecF.d, nTUWaterHeating1.proecF.u, nTUWaterHeating1.proecF.s, nTUWaterHeating1.proecF.cp, nTUWaterHeating1.proecF.ddhp, nTUWaterHeating1.proecF.ddph, nTUWaterHeating1.proecF.duph, nTUWaterHeating1.proecF.duhp, nTUWaterHeating1.proecF.x) = $cse6
18/85 (10): nTUWaterHeating1.promcF = ThermoSysPro.Properties.WaterSteam.IF97.Water_Ph(0.5 * (singularPressureLoss2.C2.P + nTUWaterHeating1.Se.P), 0.5 * (nTUWaterHeating1.HeiF + nTUWaterHeating1.HDesF), nTUWaterHeating1.mode_mF)
19/95 (10): nTUWaterHeating1.prompF = ThermoSysPro.Properties.WaterSteam.IF97.Water_Ph(singularPressureLoss2.C2.P, 0.5 * (singularPressureLoss2.h + nTUWaterHeating1.HeiF), nTUWaterHeating1.mode_eeF)
20/105 (1): nTUWaterHeating1.Wcond = Source_condenseur.Q0 * (nTUWaterHeating1.HDesF - nTUWaterHeating1.HeiF)
21/106 (1): nTUWaterHeating1.Wpurge = Source_condenseur.Q0 * (nTUWaterHeating1.HeiF - singularPressureLoss2.h)
22/107 (1): nTUWaterHeating1.Wpurge = singularPressureLoss5.Q * (nTUWaterHeating1.Hep - singularPressureLoss5.h)
23/108 (10): nTUWaterHeating1.prosp = ThermoSysPro.Properties.WaterSteam.IF97.Water_Ph(nTUWaterHeating1.P, nTUWaterHeating1.Hep, nTUWaterHeating1.mode_spC)
24/118 (1): nTUWaterHeating1.Wpurge = $cse8 * $cse9 * (nTUWaterHeating1.prosp.T - nTUWaterHeating1.proeeF.T)
25/119 (1): 0.0 = if nTUWaterHeating1.flashepC.x > 0.0 then nTUWaterHeating1.Hep - nTUWaterHeating1.HsateC else singularPressureLoss5.Q * nTUWaterHeating1.Hep - (nTUWaterHeating1.HsateC * singularPressureLoss6.Q + singularPressureLoss7.h * singularPressureLoss7.Q)
26/120 (1): $cse9 = ThermoSysPro.Correlations.Thermal.WBHeatExchangerEfficiency(singularPressureLoss5.Q, Source_condenseur.Q0, nTUWaterHeating1.prompC.cp, nTUWaterHeating1.prompF.cp, nTUWaterHeating1.KPurge, 1458.0, 0.0)
27/121 (1): singularPressureLoss5.Q = singularPressureLoss6.Q + singularPressureLoss7.Q
28/122 (1): $cse16 = min(singularPressureLoss7.Q * nTUWaterHeating.prompC.cp, Source_condenseur.Q0 * nTUWaterHeating.prompF.cp)
29/123 (1): nTUWaterHeating.Wpurge = $cse16 * $cse17 * (nTUWaterHeating.prosp.T - nTUWaterHeating.proeeF.T)
30/124 (10): $cse7 = ThermoSysPro.Properties.WaterSteam.IF97.Water_Ph(0.5 * (singularPressureLoss2.C2.P + nTUWaterHeating1.Se.P), 0.5 * (singularPressureLoss2.h + nTUWaterHeating1.HDesF), nTUWaterHeating1.mode_eeF)
31/134 (10): nTUWaterHeating1.proeeF = ThermoSysPro.Properties.WaterSteam.IF97.Water_Ph(singularPressureLoss2.C2.P, singularPressureLoss2.h, nTUWaterHeating1.mode_eeF)
32/144 (10): $cse26 = ThermoSysPro.Properties.Fluid.Ph(singularPressureLoss2.Pm, singularPressureLoss2.h, singularPressureLoss2.mode, singularPressureLoss2.fluid)
33/154 (1): singularPressureLoss2.deltaP = singularPressureLoss2.K * $cse27 / singularPressureLoss2.rho
34/155 (1): Source_condenseur.P0 - singularPressureLoss2.C2.P = singularPressureLoss2.deltaP
35/156 (1): singularPressureLoss2.Pm = 0.5 * (Source_condenseur.P0 + singularPressureLoss2.C2.P)
36/157 (1): singularPressureLoss2.C2.P - nTUWaterHeating1.Se.P = nTUWaterHeating1.lambdaE * $cse11 / nTUWaterHeating1.rho
37/158 (10): ThermoSysPro.Properties.WaterSteam.Common.ThermoProperties_ph(nTUWaterHeating1.promeF.T, nTUWaterHeating1.rho, nTUWaterHeating1.promeF.u, nTUWaterHeating1.promeF.s, nTUWaterHeating1.promeF.cp, nTUWaterHeating1.promeF.ddhp, nTUWaterHeating1.promeF.ddph, nTUWaterHeating1.promeF.duph, nTUWaterHeating1.promeF.duhp, nTUWaterHeating1.promeF.x) = $cse7
38/168 (10): ThermoSysPro.Properties.WaterSteam.Common.ThermoProperties_ph(singularPressureLoss2.T, singularPressureLoss2.rho, singularPressureLoss2.pro.u, singularPressureLoss2.pro.s, singularPressureLoss2.pro.cp, singularPressureLoss2.pro.ddhp, singularPressureLoss2.pro.ddph, singularPressureLoss2.pro.duph, singularPressureLoss2.pro.duhp, singularPressureLoss2.pro.x) = $cse26
39/178 (1): 0.0 = if Source_condenseur.Q0 > 0.0 then singularPressureLoss2.h - Source_condenseur.h0 else singularPressureLoss2.h - singularPressureLoss2.C2.h_vol
40/179 (1): 0.0 = if noEvent(Source_condenseur.Q0 > 0.0) then singularPressureLoss2.h - singularPressureLoss2.C2.h_vol else nTUWaterHeating1.HDesF - nTUWaterHeating1.Se.h_vol
41/180 (1): 0.0 = if noEvent(Source_condenseur.Q0 > 0.0) then nTUWaterHeating1.HDesF - nTUWaterHeating1.Se.h_vol else nTUWaterHeating.HDesF - nTUWaterHeating.Se.h_vol
42/181 (10): nTUWaterHeating.prompF = ThermoSysPro.Properties.WaterSteam.IF97.Water_Ph(nTUWaterHeating1.Se.P, 0.5 * (nTUWaterHeating1.HDesF + nTUWaterHeating.HeiF), nTUWaterHeating.mode_eeF)
43/191 (1): $cse17 = ThermoSysPro.Correlations.Thermal.WBHeatExchangerEfficiency(singularPressureLoss7.Q, Source_condenseur.Q0, nTUWaterHeating.prompC.cp, nTUWaterHeating.prompF.cp, nTUWaterHeating.KPurge, 656.0, 0.0)
44/192 (10): $cse15 = ThermoSysPro.Properties.WaterSteam.IF97.Water_Ph(0.5 * (nTUWaterHeating1.Se.P + nTUWaterHeating.Se.P), 0.5 * (nTUWaterHeating1.HDesF + nTUWaterHeating.HDesF), nTUWaterHeating.mode_eeF)
45/202 (10): nTUWaterHeating.promcF = ThermoSysPro.Properties.WaterSteam.IF97.Water_Ph(0.5 * (nTUWaterHeating1.Se.P + nTUWaterHeating.Se.P), 0.5 * (nTUWaterHeating.HeiF + nTUWaterHeating.HDesF), nTUWaterHeating.mode_mF)
46/212 (1): $cse18 = ThermoSysPro.Correlations.Thermal.WBHeatExchangerEfficiency(singularPressureLoss3.Q, Source_condenseur.Q0, 1e20, nTUWaterHeating.promcF.cp, nTUWaterHeating.KCond, nTUWaterHeating.SCondDes - 1e-9, 0.5)
47/213 (1): nTUWaterHeating.Wcond = Source_condenseur.Q0 * nTUWaterHeating.promcF.cp * $cse18 * (nTUWaterHeating.TsatC - nTUWaterHeating.TeiF)
48/214 (1): nTUWaterHeating.Wcond = if noEvent(singularPressureLoss3.h < nTUWaterHeating.HsatvC) then singularPressureLoss3.Q * (singularPressureLoss3.h - nTUWaterHeating.HsateC) + nTUWaterHeating.Wflash else singularPressureLoss3.Q * (nTUWaterHeating.HsatvC - nTUWaterHeating.HsateC) + nTUWaterHeating.Wflash
49/215 (1): nTUWaterHeating.Wflash = if nTUWaterHeating.flashepC.x > 0.0 then Source_condenseur1.Q0 * (singularPressureLoss1.h - nTUWaterHeating.HsateC) else 0.0
50/216 (10): nTUWaterHeating.flashepC = ThermoSysPro.Properties.WaterSteam.IF97.Water_Ph(nTUWaterHeating.P, singularPressureLoss1.h, nTUWaterHeating.mode_flash)
51/226 (1): 0.0 = if nTUWaterHeating.flashepC.x > 0.0 then nTUWaterHeating.Hep - nTUWaterHeating.HsateC else singularPressureLoss7.Q * nTUWaterHeating.Hep - (nTUWaterHeating.HsateC * singularPressureLoss3.Q + singularPressureLoss1.h * Source_condenseur1.Q0)
52/227 (10): nTUWaterHeating.prompC = ThermoSysPro.Properties.WaterSteam.IF97.Water_Ph(nTUWaterHeating.P, 0.5 * (nTUWaterHeating.Hep + singularPressureLoss7.h), nTUWaterHeating.mode_spC)
53/237 (10): nTUWaterHeating.prosp = ThermoSysPro.Properties.WaterSteam.IF97.Water_Ph(nTUWaterHeating.P, nTUWaterHeating.Hep, nTUWaterHeating.mode_spC)
54/247 (1): nTUWaterHeating.Wpurge = singularPressureLoss7.Q * (nTUWaterHeating.Hep - singularPressureLoss7.h)
55/248 (1): nTUWaterHeating.Wpurge = Source_condenseur.Q0 * (nTUWaterHeating.HeiF - nTUWaterHeating1.HDesF)
56/249 (10): $cse14 = ThermoSysPro.Properties.WaterSteam.IF97.Water_Ph(nTUWaterHeating1.Se.P, nTUWaterHeating.HeiF, nTUWaterHeating.mode_eeF)
57/259 (10): ThermoSysPro.Properties.WaterSteam.Common.ThermoProperties_ph(nTUWaterHeating.TeiF, nTUWaterHeating.proecF.d, nTUWaterHeating.proecF.u, nTUWaterHeating.proecF.s, nTUWaterHeating.proecF.cp, nTUWaterHeating.proecF.ddhp, nTUWaterHeating.proecF.ddph, nTUWaterHeating.proecF.duph, nTUWaterHeating.proecF.duhp, nTUWaterHeating.proecF.x) = $cse14
58/269 (1): nTUWaterHeating.Wcond = Source_condenseur.Q0 * (nTUWaterHeating.HDesF - nTUWaterHeating.HeiF)
59/270 (1): 0.0 = if Source_condenseur.Q0 > 0.0 then nTUWaterHeating.HDesF - nTUWaterHeating.Se.h_vol else nTUWaterHeating.HDesF - Puit_condenseur.h0
60/271 (1): 0.0 = if Source_condenseur1.Q0 > 0.0 then singularPressureLoss1.h - Source_condenseur1.h0 else singularPressureLoss1.h - nTUWaterHeating.h
61/272 (1): 0.0 = if singularPressureLoss3.Q > 0.0 then singularPressureLoss3.h - sourceP.h0 else singularPressureLoss3.h - nTUWaterHeating.h
62/273 (10): $cse24 = ThermoSysPro.Properties.Fluid.Ph(singularPressureLoss3.Pm, singularPressureLoss3.h, singularPressureLoss3.mode, singularPressureLoss3.fluid)
63/283 (10): ThermoSysPro.Properties.WaterSteam.Common.ThermoProperties_ph(singularPressureLoss3.T, singularPressureLoss3.rho, singularPressureLoss3.pro.u, singularPressureLoss3.pro.s, singularPressureLoss3.pro.cp, singularPressureLoss3.pro.ddhp, singularPressureLoss3.pro.ddph, singularPressureLoss3.pro.duph, singularPressureLoss3.pro.duhp, singularPressureLoss3.pro.x) = $cse24
64/293 (1): singularPressureLoss3.Pm = 0.5 * (sourceP.P0 + nTUWaterHeating.P)
65/294 (14): (ThermoSysPro.Properties.WaterSteam.Common.PropThermoSat(nTUWaterHeating.lsatC.P, nTUWaterHeating.TsatC, nTUWaterHeating.lsatC.rho, nTUWaterHeating.HsateC, nTUWaterHeating.lsatC.cp, nTUWaterHeating.lsatC.pt, nTUWaterHeating.lsatC.cv), ThermoSysPro.Properties.WaterSteam.Common.PropThermoSat(nTUWaterHeating.vsatC.P, nTUWaterHeating.vsatC.T, nTUWaterHeating.vsatC.rho, nTUWaterHeating.HsatvC, nTUWaterHeating.vsatC.cp, nTUWaterHeating.vsatC.pt, nTUWaterHeating.vsatC.cv)) = ThermoSysPro.Properties.WaterSteam.IF97.Water_sat_P(nTUWaterHeating.P)
66/308 (1): sourceP.P0 - nTUWaterHeating.P = singularPressureLoss3.deltaP
67/309 (1): singularPressureLoss3.deltaP = singularPressureLoss3.K * $cse25 / singularPressureLoss3.rho
68/310 (1): nTUWaterHeating1.Se.P - nTUWaterHeating.Se.P = nTUWaterHeating.lambdaE * $cse19 / nTUWaterHeating.rho
69/311 (10): ThermoSysPro.Properties.WaterSteam.Common.ThermoProperties_ph(nTUWaterHeating.promeF.T, nTUWaterHeating.rho, nTUWaterHeating.promeF.u, nTUWaterHeating.promeF.s, nTUWaterHeating.promeF.cp, nTUWaterHeating.promeF.ddhp, nTUWaterHeating.promeF.ddph, nTUWaterHeating.promeF.duph, nTUWaterHeating.promeF.duhp, nTUWaterHeating.promeF.x) = $cse15
70/321 (10): nTUWaterHeating.proeeF = ThermoSysPro.Properties.WaterSteam.IF97.Water_Ph(nTUWaterHeating1.Se.P, nTUWaterHeating1.HDesF, nTUWaterHeating.mode_eeF)
71/331 (1): singularPressureLoss7.Q = singularPressureLoss3.Q + Source_condenseur1.Q0
72/332 (1): $cse25 = ThermoSysPro.Functions.ThermoSquare(singularPressureLoss3.Q, singularPressureLoss3.eps)
73/333 (1): sourceP1.P0 - nTUWaterHeating1.P = singularPressureLoss6.deltaP
74/334 (1): singularPressureLoss6.Pm = 0.5 * (sourceP1.P0 + nTUWaterHeating1.P)

Variables:
1: singularPressureLoss6.Pm:VARIABLE(min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 )  "Average fluid pressure" type: Real
2: singularPressureLoss6.deltaP:VARIABLE(unit = "Pa" )  "Singular pressure loss" type: Real
3: $cse25:VARIABLE(protected = true )  type: Real unreplaceable
4: singularPressureLoss3.Q:VARIABLE(start = 100.0 unit = "kg/s" )  "Mass flow rate" type: Real
5: nTUWaterHeating.proeeF.duph:VARIABLE(unit = "m3/kg" )  "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real
6: nTUWaterHeating.proeeF.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 )  "Density" type: Real
7: nTUWaterHeating.proeeF.x:VARIABLE(min = 0.0 max = 1.0 unit = "1" )  "Vapor mass fraction" type: Real
8: nTUWaterHeating.proeeF.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific heat capacity at constant presure" type: Real
9: nTUWaterHeating.proeeF.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 )  "Specific inner energy" type: Real
10: nTUWaterHeating.proeeF.ddph:VARIABLE(unit = "s2/m2" )  "Derivative of density wrt. pressure at constant specific enthalpy" type: Real
11: nTUWaterHeating.proeeF.duhp:VARIABLE(unit = "1" )  "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real
12: nTUWaterHeating.promeF.ddph:VARIABLE(unit = "s2/m2" )  "Derivative of density wrt. pressure at constant specific enthalpy" type: Real
13: nTUWaterHeating.promeF.duhp:VARIABLE(unit = "1" )  "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real
14: nTUWaterHeating.promeF.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific heat capacity at constant presure" type: Real
15: nTUWaterHeating.promeF.x:VARIABLE(min = 0.0 max = 1.0 unit = "1" )  "Vapor mass fraction" type: Real
16: nTUWaterHeating.promeF.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific entropy" type: Real
17: nTUWaterHeating.promeF.ddhp:VARIABLE(unit = "kg.s2/m5" )  "Derivative of density wrt. specific enthalpy at constant pressure" type: Real
18: nTUWaterHeating.promeF.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 )  "Specific inner energy" type: Real
19: nTUWaterHeating.promeF.T:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 320.0 )  "Temperature" type: Real
20: $cse15.ddph:VARIABLE(protected = true )  type: Real unreplaceable
21: nTUWaterHeating.promeF.duph:VARIABLE(unit = "m3/kg" )  "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real
22: nTUWaterHeating.rho:VARIABLE(min = 1e-9 max = 1e5 start = 1000.0 unit = "kg/m3" nominal = 998.0 )  "Average water density" type: Real
23: singularPressureLoss3.rho:VARIABLE(min = 1e-9 max = 1e5 start = 998.0 unit = "kg/m3" nominal = 998.0 )  "Fluid density" type: Real
24: singularPressureLoss3.deltaP:VARIABLE(unit = "Pa" )  "Singular pressure loss" type: Real
25: nTUWaterHeating.lsatC.cv:VARIABLE(unit = "J/(kg.K)" )  "Specific heat capacity at constant volume" type: Real
26: nTUWaterHeating.lsatC.P:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 )  "Pressure" type: Real
27: nTUWaterHeating.lsatC.pt:VARIABLE()  "Derivative of pressure wrt. temperature" type: Real
28: nTUWaterHeating.lsatC.cp:VARIABLE(unit = "J/(kg.K)" )  "Specific heat capacity at constant pressure" type: Real
29: nTUWaterHeating.vsatC.rho:VARIABLE(min = 0.0 unit = "kg/m3" )  "Density" type: Real
30: nTUWaterHeating.vsatC.pt:VARIABLE()  "Derivative of pressure wrt. temperature" type: Real
31: nTUWaterHeating.vsatC.cv:VARIABLE(unit = "J/(kg.K)" )  "Specific heat capacity at constant volume" type: Real
32: nTUWaterHeating.TsatC:VARIABLE(min = 0.0 start = 400.0 unit = "K" nominal = 300.0 )  "Saturation temperature" type: Real
33: nTUWaterHeating.HsatvC:VARIABLE(min = 0.0 start = 2.5e6 unit = "J/kg" )  "Saturation specific enthalpy of the vapor at the pressure of the vapor inlet" type: Real
34: nTUWaterHeating.HsateC:VARIABLE(min = 0.0 start = 3e5 unit = "J/kg" )  "Saturation specific enthalpy of the water at the pressure of the vapor inlet" type: Real
35: nTUWaterHeating.vsatC.T:VARIABLE(min = 0.0 start = 288.15 unit = "K" nominal = 300.0 )  "Temperature" type: Real
36: nTUWaterHeating.vsatC.P:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 )  "Pressure" type: Real
37: nTUWaterHeating.vsatC.cp:VARIABLE(unit = "J/(kg.K)" )  "Specific heat capacity at constant pressure" type: Real
38: nTUWaterHeating.lsatC.rho:VARIABLE(min = 0.0 unit = "kg/m3" )  "Density" type: Real
39: nTUWaterHeating.P:VARIABLE(min = 0.0 start = 2.7e6 unit = "Pa" nominal = 1e5 )  "Fluid pressure" type: Real
40: singularPressureLoss3.pro.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 )  "Specific inner energy" type: Real
41: singularPressureLoss3.pro.ddph:VARIABLE(unit = "s2/m2" )  "Derivative of density wrt. pressure at constant specific enthalpy" type: Real
42: singularPressureLoss3.pro.x:VARIABLE(min = 0.0 max = 1.0 unit = "1" )  "Vapor mass fraction" type: Real
43: singularPressureLoss3.T:VARIABLE(min = 200.0 max = 6000.0 start = 290.0 unit = "K" nominal = 300.0 )  "Fluid temperature" type: Real
44: $cse24.d:VARIABLE(protected = true )  type: Real unreplaceable
45: singularPressureLoss3.pro.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific entropy" type: Real
46: singularPressureLoss3.pro.duhp:VARIABLE(unit = "1" )  "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real
47: singularPressureLoss3.pro.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific heat capacity at constant presure" type: Real
48: singularPressureLoss3.pro.duph:VARIABLE(unit = "m3/kg" )  "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real
49: singularPressureLoss3.pro.ddhp:VARIABLE(unit = "kg.s2/m5" )  "Derivative of density wrt. specific enthalpy at constant pressure" type: Real
50: $cse24.ddph:VARIABLE(protected = true )  type: Real unreplaceable
51: $cse24.s:VARIABLE(protected = true )  type: Real unreplaceable
52: $cse24.u:VARIABLE(protected = true )  type: Real unreplaceable
53: $cse24.x:VARIABLE(protected = true )  type: Real unreplaceable
54: singularPressureLoss3.Pm:VARIABLE(min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 )  "Average fluid pressure" type: Real
55: $cse24.duhp:VARIABLE(protected = true )  type: Real unreplaceable
56: $cse24.T:VARIABLE(protected = true )  type: Real unreplaceable
57: $cse24.ddhp:VARIABLE(protected = true )  type: Real unreplaceable
58: $cse24.duph:VARIABLE(protected = true )  type: Real unreplaceable
59: $cse24.cp:VARIABLE(protected = true )  type: Real unreplaceable
60: singularPressureLoss3.h:VARIABLE(start = 2.6e6 unit = "J/kg" )  "Fluid specific enthalpy" type: Real
61: nTUWaterHeating.h:VARIABLE(start = 879000.0 unit = "J/kg" )  "Fluid specific enthalpy" type: Real
62: nTUWaterHeating.Se.h_vol:VARIABLE(flow=false start = 9.7e5 unit = "J/kg" )  "Fluid specific enthalpy in the control volume" type: Real
63: nTUWaterHeating.HDesF:VARIABLE(start = 973600.0 unit = "J/kg" )  "Fluid specific enthalpy after deheating" type: Real
64: nTUWaterHeating.proecF.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 )  "Specific inner energy" type: Real
65: nTUWaterHeating.proecF.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 )  "Density" type: Real
66: nTUWaterHeating.proecF.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific entropy" type: Real
67: nTUWaterHeating.proecF.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific heat capacity at constant presure" type: Real
68: nTUWaterHeating.proecF.ddph:VARIABLE(unit = "s2/m2" )  "Derivative of density wrt. pressure at constant specific enthalpy" type: Real
69: nTUWaterHeating.proecF.duph:VARIABLE(unit = "m3/kg" )  "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real
70: nTUWaterHeating.TeiF:VARIABLE(min = 200.0 max = 6000.0 start = 400.0 unit = "K" nominal = 300.0 )  "Fluid temperature after drain cooling" type: Real
71: nTUWaterHeating.proecF.x:VARIABLE(min = 0.0 max = 1.0 unit = "1" )  "Vapor mass fraction" type: Real
72: nTUWaterHeating.proecF.ddhp:VARIABLE(unit = "kg.s2/m5" )  "Derivative of density wrt. specific enthalpy at constant pressure" type: Real
73: nTUWaterHeating.proecF.duhp:VARIABLE(unit = "1" )  "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real
74: $cse14.ddhp:VARIABLE(protected = true )  type: Real unreplaceable
75: $cse14.duhp:VARIABLE(protected = true )  type: Real unreplaceable
76: $cse14.s:VARIABLE(protected = true )  type: Real unreplaceable
77: $cse14.cp:VARIABLE(protected = true )  type: Real unreplaceable
78: $cse14.u:VARIABLE(protected = true )  type: Real unreplaceable
79: $cse14.duph:VARIABLE(protected = true )  type: Real unreplaceable
80: $cse14.ddph:VARIABLE(protected = true )  type: Real unreplaceable
81: $cse14.T:VARIABLE(protected = true )  type: Real unreplaceable
82: $cse14.d:VARIABLE(protected = true )  type: Real unreplaceable
83: $cse14.x:VARIABLE(protected = true )  type: Real unreplaceable
84: nTUWaterHeating.HeiF:VARIABLE(start = 873550.0 unit = "J/kg" )  "Fluid specific enthalpy after drain cooling" type: Real
85: nTUWaterHeating.Wpurge:VARIABLE(start = 1.0 unit = "W" )  "Energy transfer during drain cooling" type: Real
86: nTUWaterHeating.prosp.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 )  "Specific inner energy" type: Real
87: nTUWaterHeating.prosp.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific entropy" type: Real
88: nTUWaterHeating.prosp.ddph:VARIABLE(unit = "s2/m2" )  "Derivative of density wrt. pressure at constant specific enthalpy" type: Real
89: nTUWaterHeating.prosp.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific heat capacity at constant presure" type: Real
90: nTUWaterHeating.prosp.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 )  "Density" type: Real
91: nTUWaterHeating.prosp.duph:VARIABLE(unit = "m3/kg" )  "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real
92: nTUWaterHeating.prosp.duhp:VARIABLE(unit = "1" )  "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real
93: nTUWaterHeating.prosp.T:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 320.0 )  "Temperature" type: Real
94: nTUWaterHeating.prosp.ddhp:VARIABLE(unit = "kg.s2/m5" )  "Derivative of density wrt. specific enthalpy at constant pressure" type: Real
95: nTUWaterHeating.prosp.x:VARIABLE(min = 0.0 max = 1.0 unit = "1" )  "Vapor mass fraction" type: Real
96: nTUWaterHeating.prompC.ddhp:VARIABLE(unit = "kg.s2/m5" )  "Derivative of density wrt. specific enthalpy at constant pressure" type: Real
97: nTUWaterHeating.prompC.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 )  "Density" type: Real
98: nTUWaterHeating.prompC.duph:VARIABLE(unit = "m3/kg" )  "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real
99: nTUWaterHeating.prompC.duhp:VARIABLE(unit = "1" )  "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real
100: nTUWaterHeating.prompC.ddph:VARIABLE(unit = "s2/m2" )  "Derivative of density wrt. pressure at constant specific enthalpy" type: Real
101: nTUWaterHeating.prompC.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 )  "Specific inner energy" type: Real
102: nTUWaterHeating.prompC.T:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 320.0 )  "Temperature" type: Real
103: nTUWaterHeating.prompC.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific heat capacity at constant presure" type: Real
104: nTUWaterHeating.prompC.x:VARIABLE(min = 0.0 max = 1.0 unit = "1" )  "Vapor mass fraction" type: Real
105: nTUWaterHeating.prompC.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific entropy" type: Real
106: nTUWaterHeating.Hep:VARIABLE(start = 873550.0 unit = "J/kg" )  "Mixing specific enthalpy of the drain and the condensate" type: Real
107: nTUWaterHeating.flashepC.T:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 320.0 )  "Temperature" type: Real
108: nTUWaterHeating.flashepC.duph:VARIABLE(unit = "m3/kg" )  "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real
109: nTUWaterHeating.flashepC.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific entropy" type: Real
110: nTUWaterHeating.flashepC.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 )  "Specific inner energy" type: Real
111: nTUWaterHeating.flashepC.ddph:VARIABLE(unit = "s2/m2" )  "Derivative of density wrt. pressure at constant specific enthalpy" type: Real
112: nTUWaterHeating.flashepC.duhp:VARIABLE(unit = "1" )  "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real
113: nTUWaterHeating.flashepC.ddhp:VARIABLE(unit = "kg.s2/m5" )  "Derivative of density wrt. specific enthalpy at constant pressure" type: Real
114: nTUWaterHeating.flashepC.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific heat capacity at constant presure" type: Real
115: nTUWaterHeating.flashepC.x:VARIABLE(min = 0.0 max = 1.0 unit = "1" )  "Vapor mass fraction" type: Real
116: nTUWaterHeating.flashepC.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 )  "Density" type: Real
117: singularPressureLoss1.h:VARIABLE(start = 1e5 unit = "J/kg" )  "Fluid specific enthalpy" type: Real
118: nTUWaterHeating.Wflash:VARIABLE(start = 1.0 unit = "W" )  "Energy transfer during partial vaporisation in the drain" type: Real
119: nTUWaterHeating.Wcond:VARIABLE(start = 1.0 unit = "W" )  "Energy transfer during condensation" type: Real
120: $cse18:VARIABLE(protected = true )  type: Real unreplaceable
121: nTUWaterHeating.promcF.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 )  "Density" type: Real
122: nTUWaterHeating.promcF.duph:VARIABLE(unit = "m3/kg" )  "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real
123: nTUWaterHeating.promcF.ddhp:VARIABLE(unit = "kg.s2/m5" )  "Derivative of density wrt. specific enthalpy at constant pressure" type: Real
124: nTUWaterHeating.promcF.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific heat capacity at constant presure" type: Real
125: nTUWaterHeating.promcF.ddph:VARIABLE(unit = "s2/m2" )  "Derivative of density wrt. pressure at constant specific enthalpy" type: Real
126: nTUWaterHeating.promcF.T:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 320.0 )  "Temperature" type: Real
127: nTUWaterHeating.promcF.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific entropy" type: Real
128: nTUWaterHeating.promcF.x:VARIABLE(min = 0.0 max = 1.0 unit = "1" )  "Vapor mass fraction" type: Real
129: nTUWaterHeating.promcF.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 )  "Specific inner energy" type: Real
130: nTUWaterHeating.promcF.duhp:VARIABLE(unit = "1" )  "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real
131: nTUWaterHeating.Se.P:VARIABLE(flow=false min = 0.0 start = 7.287e6 unit = "Pa" nominal = 1e5 )  "Fluid pressure in the control volume" type: Real
132: $cse15.d:VARIABLE(protected = true )  type: Real unreplaceable
133: $cse15.cp:VARIABLE(protected = true )  type: Real unreplaceable
134: $cse15.duhp:VARIABLE(protected = true )  type: Real unreplaceable
135: $cse15.x:VARIABLE(protected = true )  type: Real unreplaceable
136: $cse15.duph:VARIABLE(protected = true )  type: Real unreplaceable
137: $cse15.u:VARIABLE(protected = true )  type: Real unreplaceable
138: $cse15.s:VARIABLE(protected = true )  type: Real unreplaceable
139: $cse15.ddhp:VARIABLE(protected = true )  type: Real unreplaceable
140: $cse15.T:VARIABLE(protected = true )  type: Real unreplaceable
141: $cse17:VARIABLE(protected = true )  type: Real unreplaceable
142: nTUWaterHeating.prompF.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific entropy" type: Real
143: nTUWaterHeating.prompF.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific heat capacity at constant presure" type: Real
144: nTUWaterHeating.prompF.T:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 320.0 )  "Temperature" type: Real
145: nTUWaterHeating.prompF.duhp:VARIABLE(unit = "1" )  "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real
146: nTUWaterHeating.prompF.ddph:VARIABLE(unit = "s2/m2" )  "Derivative of density wrt. pressure at constant specific enthalpy" type: Real
147: nTUWaterHeating.prompF.ddhp:VARIABLE(unit = "kg.s2/m5" )  "Derivative of density wrt. specific enthalpy at constant pressure" type: Real
148: nTUWaterHeating.prompF.x:VARIABLE(min = 0.0 max = 1.0 unit = "1" )  "Vapor mass fraction" type: Real
149: nTUWaterHeating.prompF.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 )  "Density" type: Real
150: nTUWaterHeating.prompF.duph:VARIABLE(unit = "m3/kg" )  "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real
151: nTUWaterHeating.prompF.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 )  "Specific inner energy" type: Real
152: nTUWaterHeating1.HDesF:VARIABLE(start = 867000.0 unit = "J/kg" )  "Fluid specific enthalpy after deheating" type: Real
153: nTUWaterHeating1.Se.h_vol:VARIABLE(flow=false start = 867000.0 unit = "J/kg" )  "Fluid specific enthalpy in the control volume" type: Real
154: singularPressureLoss2.C2.h_vol:VARIABLE(flow=false start = 7.6e5 unit = "J/kg" )  "Fluid specific enthalpy in the control volume" type: Real
155: singularPressureLoss2.pro.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 )  "Specific inner energy" type: Real
156: singularPressureLoss2.pro.ddph:VARIABLE(unit = "s2/m2" )  "Derivative of density wrt. pressure at constant specific enthalpy" type: Real
157: singularPressureLoss2.pro.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific heat capacity at constant presure" type: Real
158: singularPressureLoss2.pro.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific entropy" type: Real
159: singularPressureLoss2.pro.x:VARIABLE(min = 0.0 max = 1.0 unit = "1" )  "Vapor mass fraction" type: Real
160: singularPressureLoss2.pro.ddhp:VARIABLE(unit = "kg.s2/m5" )  "Derivative of density wrt. specific enthalpy at constant pressure" type: Real
161: singularPressureLoss2.pro.duhp:VARIABLE(unit = "1" )  "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real
162: nTUWaterHeating1.promeF.ddph:VARIABLE(unit = "s2/m2" )  "Derivative of density wrt. pressure at constant specific enthalpy" type: Real
163: nTUWaterHeating1.promeF.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific entropy" type: Real
164: $cse7.duph:VARIABLE(protected = true )  type: Real unreplaceable
165: nTUWaterHeating1.promeF.duhp:VARIABLE(unit = "1" )  "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real
166: nTUWaterHeating1.promeF.ddhp:VARIABLE(unit = "kg.s2/m5" )  "Derivative of density wrt. specific enthalpy at constant pressure" type: Real
167: nTUWaterHeating1.promeF.x:VARIABLE(min = 0.0 max = 1.0 unit = "1" )  "Vapor mass fraction" type: Real
168: nTUWaterHeating1.promeF.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific heat capacity at constant presure" type: Real
169: nTUWaterHeating1.promeF.duph:VARIABLE(unit = "m3/kg" )  "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real
170: nTUWaterHeating1.promeF.T:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 320.0 )  "Temperature" type: Real
171: nTUWaterHeating1.promeF.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 )  "Specific inner energy" type: Real
172: nTUWaterHeating1.rho:VARIABLE(min = 1e-9 max = 1e5 start = 1000.0 unit = "kg/m3" nominal = 998.0 )  "Average water density" type: Real
173: singularPressureLoss2.Pm:VARIABLE(min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 )  "Average fluid pressure" type: Real
174: singularPressureLoss2.C2.P:VARIABLE(flow=false min = 0.0 start = 7.9e6 unit = "Pa" nominal = 1e5 )  "Fluid pressure in the control volume" type: Real
175: singularPressureLoss2.deltaP:VARIABLE(unit = "Pa" )  "Singular pressure loss" type: Real
176: singularPressureLoss2.rho:VARIABLE(min = 1e-9 max = 1e5 start = 998.0 unit = "kg/m3" nominal = 998.0 )  "Fluid density" type: Real
177: singularPressureLoss2.pro.duph:VARIABLE(unit = "m3/kg" )  "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real
178: singularPressureLoss2.T:VARIABLE(min = 200.0 max = 6000.0 start = 290.0 unit = "K" nominal = 300.0 )  "Fluid temperature" type: Real
179: $cse26.s:VARIABLE(protected = true )  type: Real unreplaceable
180: $cse26.ddph:VARIABLE(protected = true )  type: Real unreplaceable
181: $cse26.duph:VARIABLE(protected = true )  type: Real unreplaceable
182: $cse26.x:VARIABLE(protected = true )  type: Real unreplaceable
183: $cse26.ddhp:VARIABLE(protected = true )  type: Real unreplaceable
184: $cse26.d:VARIABLE(protected = true )  type: Real unreplaceable
185: $cse26.duhp:VARIABLE(protected = true )  type: Real unreplaceable
186: $cse26.T:VARIABLE(protected = true )  type: Real unreplaceable
187: $cse26.u:VARIABLE(protected = true )  type: Real unreplaceable
188: $cse26.cp:VARIABLE(protected = true )  type: Real unreplaceable
189: nTUWaterHeating1.proeeF.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 )  "Density" type: Real
190: nTUWaterHeating1.proeeF.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific heat capacity at constant presure" type: Real
191: nTUWaterHeating1.proeeF.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 )  "Specific inner energy" type: Real
192: nTUWaterHeating1.proeeF.x:VARIABLE(min = 0.0 max = 1.0 unit = "1" )  "Vapor mass fraction" type: Real
193: nTUWaterHeating1.proeeF.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific entropy" type: Real
194: nTUWaterHeating1.proeeF.duhp:VARIABLE(unit = "1" )  "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real
195: nTUWaterHeating1.proeeF.duph:VARIABLE(unit = "m3/kg" )  "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real
196: nTUWaterHeating1.proeeF.ddhp:VARIABLE(unit = "kg.s2/m5" )  "Derivative of density wrt. specific enthalpy at constant pressure" type: Real
197: nTUWaterHeating1.proeeF.T:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 320.0 )  "Temperature" type: Real
198: nTUWaterHeating1.proeeF.ddph:VARIABLE(unit = "s2/m2" )  "Derivative of density wrt. pressure at constant specific enthalpy" type: Real
199: singularPressureLoss2.h:VARIABLE(start = 1e5 unit = "J/kg" )  "Fluid specific enthalpy" type: Real
200: $cse7.d:VARIABLE(protected = true )  type: Real unreplaceable
201: $cse7.x:VARIABLE(protected = true )  type: Real unreplaceable
202: $cse7.ddph:VARIABLE(protected = true )  type: Real unreplaceable
203: $cse7.cp:VARIABLE(protected = true )  type: Real unreplaceable
204: $cse7.ddhp:VARIABLE(protected = true )  type: Real unreplaceable
205: $cse7.s:VARIABLE(protected = true )  type: Real unreplaceable
206: $cse7.duhp:VARIABLE(protected = true )  type: Real unreplaceable
207: $cse7.T:VARIABLE(protected = true )  type: Real unreplaceable
208: $cse7.u:VARIABLE(protected = true )  type: Real unreplaceable
209: nTUWaterHeating1.Se.P:VARIABLE(flow=false min = 0.0 start = 7.65e6 unit = "Pa" nominal = 1e5 )  "Fluid pressure in the control volume" type: Real
210: nTUWaterHeating.proeeF.ddhp:VARIABLE(unit = "kg.s2/m5" )  "Derivative of density wrt. specific enthalpy at constant pressure" type: Real
211: nTUWaterHeating.proeeF.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific entropy" type: Real
212: nTUWaterHeating.proeeF.T:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 320.0 )  "Temperature" type: Real
213: $cse16:VARIABLE(protected = true )  type: Real unreplaceable
214: singularPressureLoss7.Q:VARIABLE(start = 110.0 unit = "kg/s" )  "Mass flow rate" type: Real
215: $cse9:VARIABLE(protected = true )  type: Real unreplaceable
216: singularPressureLoss5.Q:VARIABLE(start = 100.0 unit = "kg/s" )  "Mass flow rate" type: Real
217: $cse8:VARIABLE(protected = true )  type: Real unreplaceable
218: nTUWaterHeating1.prosp.duph:VARIABLE(unit = "m3/kg" )  "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real
219: nTUWaterHeating1.prosp.duhp:VARIABLE(unit = "1" )  "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real
220: nTUWaterHeating1.prosp.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 )  "Specific inner energy" type: Real
221: nTUWaterHeating1.prosp.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific heat capacity at constant presure" type: Real
222: nTUWaterHeating1.prosp.x:VARIABLE(min = 0.0 max = 1.0 unit = "1" )  "Vapor mass fraction" type: Real
223: nTUWaterHeating1.prosp.T:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 320.0 )  "Temperature" type: Real
224: nTUWaterHeating1.prosp.ddph:VARIABLE(unit = "s2/m2" )  "Derivative of density wrt. pressure at constant specific enthalpy" type: Real
225: nTUWaterHeating1.prosp.ddhp:VARIABLE(unit = "kg.s2/m5" )  "Derivative of density wrt. specific enthalpy at constant pressure" type: Real
226: nTUWaterHeating1.prosp.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific entropy" type: Real
227: nTUWaterHeating1.prosp.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 )  "Density" type: Real
228: nTUWaterHeating1.Hep:VARIABLE(start = 865000.0 unit = "J/kg" )  "Mixing specific enthalpy of the drain and the condensate" type: Real
229: nTUWaterHeating1.Wpurge:VARIABLE(start = 1.0 unit = "W" )  "Energy transfer during drain cooling" type: Real
230: nTUWaterHeating1.Wcond:VARIABLE(start = 1.0 unit = "W" )  "Energy transfer during condensation" type: Real
231: nTUWaterHeating1.prompF.ddhp:VARIABLE(unit = "kg.s2/m5" )  "Derivative of density wrt. specific enthalpy at constant pressure" type: Real
232: nTUWaterHeating1.prompF.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific entropy" type: Real
233: nTUWaterHeating1.prompF.duph:VARIABLE(unit = "m3/kg" )  "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real
234: nTUWaterHeating1.prompF.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 )  "Density" type: Real
235: nTUWaterHeating1.prompF.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 )  "Specific inner energy" type: Real
236: nTUWaterHeating1.prompF.x:VARIABLE(min = 0.0 max = 1.0 unit = "1" )  "Vapor mass fraction" type: Real
237: nTUWaterHeating1.prompF.ddph:VARIABLE(unit = "s2/m2" )  "Derivative of density wrt. pressure at constant specific enthalpy" type: Real
238: nTUWaterHeating1.promcF.ddhp:VARIABLE(unit = "kg.s2/m5" )  "Derivative of density wrt. specific enthalpy at constant pressure" type: Real
239: nTUWaterHeating1.promcF.x:VARIABLE(min = 0.0 max = 1.0 unit = "1" )  "Vapor mass fraction" type: Real
240: nTUWaterHeating1.promcF.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 )  "Density" type: Real
241: nTUWaterHeating1.promcF.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 )  "Specific inner energy" type: Real
242: nTUWaterHeating1.promcF.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific entropy" type: Real
243: nTUWaterHeating1.promcF.duph:VARIABLE(unit = "m3/kg" )  "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real
244: nTUWaterHeating1.promcF.T:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 320.0 )  "Temperature" type: Real
245: nTUWaterHeating1.promcF.duhp:VARIABLE(unit = "1" )  "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real
246: nTUWaterHeating1.promcF.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific heat capacity at constant presure" type: Real
247: nTUWaterHeating1.promcF.ddph:VARIABLE(unit = "s2/m2" )  "Derivative of density wrt. pressure at constant specific enthalpy" type: Real
248: nTUWaterHeating1.proecF.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 )  "Specific inner energy" type: Real
249: nTUWaterHeating1.TeiF:VARIABLE(min = 200.0 max = 6000.0 start = 400.0 unit = "K" nominal = 300.0 )  "Fluid temperature after drain cooling" type: Real
250: nTUWaterHeating1.proecF.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific heat capacity at constant presure" type: Real
251: nTUWaterHeating1.proecF.ddhp:VARIABLE(unit = "kg.s2/m5" )  "Derivative of density wrt. specific enthalpy at constant pressure" type: Real
252: nTUWaterHeating1.proecF.ddph:VARIABLE(unit = "s2/m2" )  "Derivative of density wrt. pressure at constant specific enthalpy" type: Real
253: nTUWaterHeating1.proecF.x:VARIABLE(min = 0.0 max = 1.0 unit = "1" )  "Vapor mass fraction" type: Real
254: nTUWaterHeating1.proecF.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 )  "Density" type: Real
255: nTUWaterHeating1.proecF.duhp:VARIABLE(unit = "1" )  "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real
256: nTUWaterHeating1.proecF.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific entropy" type: Real
257: nTUWaterHeating1.proecF.duph:VARIABLE(unit = "m3/kg" )  "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real
258: $cse6.ddph:VARIABLE(protected = true )  type: Real unreplaceable
259: $cse6.d:VARIABLE(protected = true )  type: Real unreplaceable
260: $cse6.x:VARIABLE(protected = true )  type: Real unreplaceable
261: $cse6.duhp:VARIABLE(protected = true )  type: Real unreplaceable
262: $cse6.ddhp:VARIABLE(protected = true )  type: Real unreplaceable
263: $cse6.cp:VARIABLE(protected = true )  type: Real unreplaceable
264: $cse6.duph:VARIABLE(protected = true )  type: Real unreplaceable
265: $cse6.s:VARIABLE(protected = true )  type: Real unreplaceable
266: $cse6.u:VARIABLE(protected = true )  type: Real unreplaceable
267: $cse6.T:VARIABLE(protected = true )  type: Real unreplaceable
268: nTUWaterHeating1.HeiF:VARIABLE(start = 772000.0 unit = "J/kg" )  "Fluid specific enthalpy after drain cooling" type: Real
269: nTUWaterHeating1.prompF.T:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 320.0 )  "Temperature" type: Real
270: nTUWaterHeating1.prompF.duhp:VARIABLE(unit = "1" )  "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real
271: nTUWaterHeating1.prompF.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific heat capacity at constant presure" type: Real
272: nTUWaterHeating1.prompC.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 )  "Density" type: Real
273: nTUWaterHeating1.prompC.T:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 320.0 )  "Temperature" type: Real
274: nTUWaterHeating1.prompC.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific heat capacity at constant presure" type: Real
275: nTUWaterHeating1.prompC.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific entropy" type: Real
276: nTUWaterHeating1.prompC.duhp:VARIABLE(unit = "1" )  "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real
277: nTUWaterHeating1.prompC.x:VARIABLE(min = 0.0 max = 1.0 unit = "1" )  "Vapor mass fraction" type: Real
278: nTUWaterHeating1.prompC.ddph:VARIABLE(unit = "s2/m2" )  "Derivative of density wrt. pressure at constant specific enthalpy" type: Real
279: nTUWaterHeating1.prompC.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 )  "Specific inner energy" type: Real
280: nTUWaterHeating1.prompC.ddhp:VARIABLE(unit = "kg.s2/m5" )  "Derivative of density wrt. specific enthalpy at constant pressure" type: Real
281: nTUWaterHeating1.prompC.duph:VARIABLE(unit = "m3/kg" )  "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real
282: singularPressureLoss5.h:VARIABLE(start = 765298.0 unit = "J/kg" )  "Fluid specific enthalpy" type: Real
283: nTUWaterHeating1.h:VARIABLE(start = 765300.0 unit = "J/kg" )  "Fluid specific enthalpy" type: Real
284: nTUWaterHeating1.Wflash:VARIABLE(start = 1.0 unit = "W" )  "Energy transfer during partial vaporisation in the drain" type: Real
285: singularPressureLoss6.pro.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 )  "Specific inner energy" type: Real
286: singularPressureLoss6.pro.duhp:VARIABLE(unit = "1" )  "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real
287: singularPressureLoss6.pro.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific entropy" type: Real
288: singularPressureLoss6.pro.x:VARIABLE(min = 0.0 max = 1.0 unit = "1" )  "Vapor mass fraction" type: Real
289: singularPressureLoss6.T:VARIABLE(min = 200.0 max = 6000.0 start = 290.0 unit = "K" nominal = 300.0 )  "Fluid temperature" type: Real
290: singularPressureLoss6.pro.ddph:VARIABLE(unit = "s2/m2" )  "Derivative of density wrt. pressure at constant specific enthalpy" type: Real
291: singularPressureLoss6.pro.duph:VARIABLE(unit = "m3/kg" )  "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real
292: $cse3.s:VARIABLE(protected = true )  type: Real unreplaceable
293: $cse3.duhp:VARIABLE(protected = true )  type: Real unreplaceable
294: $cse3.x:VARIABLE(protected = true )  type: Real unreplaceable
295: $cse3.T:VARIABLE(protected = true )  type: Real unreplaceable
296: $cse3.d:VARIABLE(protected = true )  type: Real unreplaceable
297: $cse3.u:VARIABLE(protected = true )  type: Real unreplaceable
298: $cse3.ddhp:VARIABLE(protected = true )  type: Real unreplaceable
299: $cse3.duph:VARIABLE(protected = true )  type: Real unreplaceable
300: $cse3.ddph:VARIABLE(protected = true )  type: Real unreplaceable
301: singularPressureLoss6.h:VARIABLE(start = 2.4e6 unit = "J/kg" )  "Fluid specific enthalpy" type: Real
302: $cse3.cp:VARIABLE(protected = true )  type: Real unreplaceable
303: singularPressureLoss6.pro.ddhp:VARIABLE(unit = "kg.s2/m5" )  "Derivative of density wrt. specific enthalpy at constant pressure" type: Real
304: singularPressureLoss6.pro.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific heat capacity at constant presure" type: Real
305: singularPressureLoss6.rho:VARIABLE(min = 1e-9 max = 1e5 start = 998.0 unit = "kg/m3" nominal = 998.0 )  "Fluid density" type: Real
306: $cse4:VARIABLE(protected = true )  type: Real unreplaceable
307: singularPressureLoss6.Q:VARIABLE(start = 109.0 unit = "kg/s" )  "Mass flow rate" type: Real
308: $cse10:VARIABLE(protected = true )  type: Real unreplaceable
309: nTUWaterHeating1.lsatC.P:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 )  "Pressure" type: Real
310: nTUWaterHeating1.TsatC:VARIABLE(min = 0.0 start = 400.0 unit = "K" nominal = 300.0 )  "Saturation temperature" type: Real
311: nTUWaterHeating1.vsatC.pt:VARIABLE()  "Derivative of pressure wrt. temperature" type: Real
312: nTUWaterHeating1.lsatC.cp:VARIABLE(unit = "J/(kg.K)" )  "Specific heat capacity at constant pressure" type: Real
313: nTUWaterHeating1.vsatC.P:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 )  "Pressure" type: Real
314: nTUWaterHeating1.vsatC.rho:VARIABLE(min = 0.0 unit = "kg/m3" )  "Density" type: Real
315: nTUWaterHeating1.vsatC.cp:VARIABLE(unit = "J/(kg.K)" )  "Specific heat capacity at constant pressure" type: Real
316: nTUWaterHeating1.lsatC.pt:VARIABLE()  "Derivative of pressure wrt. temperature" type: Real
317: nTUWaterHeating1.lsatC.cv:VARIABLE(unit = "J/(kg.K)" )  "Specific heat capacity at constant volume" type: Real
318: nTUWaterHeating1.HsatvC:VARIABLE(min = 0.0 start = 2.5e6 unit = "J/kg" )  "Saturation specific enthalpy of the vapor at the pressure of the vapor inlet" type: Real
319: nTUWaterHeating1.vsatC.cv:VARIABLE(unit = "J/(kg.K)" )  "Specific heat capacity at constant volume" type: Real
320: nTUWaterHeating1.lsatC.rho:VARIABLE(min = 0.0 unit = "kg/m3" )  "Density" type: Real
321: nTUWaterHeating1.vsatC.T:VARIABLE(min = 0.0 start = 288.15 unit = "K" nominal = 300.0 )  "Temperature" type: Real
322: nTUWaterHeating1.P:VARIABLE(min = 0.0 start = 1.65e6 unit = "Pa" nominal = 1e5 )  "Fluid pressure" type: Real
323: nTUWaterHeating1.HsateC:VARIABLE(min = 0.0 start = 3e5 unit = "J/kg" )  "Saturation specific enthalpy of the water at the pressure of the vapor inlet" type: Real
324: nTUWaterHeating1.flashepC.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific heat capacity at constant presure" type: Real
325: nTUWaterHeating1.flashepC.T:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 320.0 )  "Temperature" type: Real
326: nTUWaterHeating1.flashepC.duph:VARIABLE(unit = "m3/kg" )  "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real
327: nTUWaterHeating1.flashepC.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 )  "Density" type: Real
328: nTUWaterHeating1.flashepC.duhp:VARIABLE(unit = "1" )  "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real
329: nTUWaterHeating1.flashepC.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 )  "Specific inner energy" type: Real
330: nTUWaterHeating1.flashepC.x:VARIABLE(min = 0.0 max = 1.0 unit = "1" )  "Vapor mass fraction" type: Real
331: nTUWaterHeating1.flashepC.ddph:VARIABLE(unit = "s2/m2" )  "Derivative of density wrt. pressure at constant specific enthalpy" type: Real
332: nTUWaterHeating1.flashepC.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific entropy" type: Real
333: nTUWaterHeating1.flashepC.ddhp:VARIABLE(unit = "kg.s2/m5" )  "Derivative of density wrt. specific enthalpy at constant pressure" type: Real
334: singularPressureLoss7.h:VARIABLE(start = 879000.0 unit = "J/kg" )  "Fluid specific enthalpy" type: Real
[/var/lib/jenkins1/ws/OpenModelicaLibraryTestingWork/OpenModelica/OMCompiler/Compiler/BackEnd/BackendDAEUtil.mo:9805:5-9806:77:writable] Error: Internal error BackendDAEUtil.traverseEqSystemStrongComponents failed with function:
omc_DAEMode_traverserStrongComponents
Notification: Performance of <failed> postOpt createDAEmodeBDAE (simulation): time 0.00879/2.328, allocations: 31.62 MB / 0.8087 GB, free: 137 MB / 0.5919 GB
Error: post-optimization module createDAEmodeBDAE (simulation) failed.
Error: Internal error SimCode DAEmode: The model ThermoSysPro.Examples.SimpleExamples.TestNTUWaterHeating2 could not be translated