Running: ./testmodel.py --libraries=/home/hudson/saved_omc/libraries/.openmodelica/libraries --ompython_omhome=/usr ThermoSysPro_ThermoSysPro.Examples.SimpleExamples.TestNTUWaterHeating1.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.TestNTUWaterHeating1,tolerance=1e-06,outputFormat="empty",numberOfIntervals=5000,variableFilter="",fileNamePrefix="ThermoSysPro_ThermoSysPro.Examples.SimpleExamples.TestNTUWaterHeating1")
translateModel(ThermoSysPro.Examples.SimpleExamples.TestNTUWaterHeating1,tolerance=1e-06,outputFormat="empty",numberOfIntervals=5000,variableFilter="",fileNamePrefix="ThermoSysPro_ThermoSysPro.Examples.SimpleExamples.TestNTUWaterHeating1")
Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermoSysPro 4.0.0-master/package.mo): time 0.8242/0.8242, allocations: 150.9 MB / 167.2 MB, free: 14.29 MB / 142.1 MB
Notification: Performance of FrontEnd - loaded program: time 0.0003413/0.0003413, allocations: 16.83 kB / 237.8 MB, free: 1.844 MB / 190.1 MB
Notification: Performance of FrontEnd - Absyn->SCode: time 0.05814/0.05849, allocations: 31.35 MB / 269.1 MB, free: 7 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.TestNTUWaterHeating1): time 1.655/1.714, allocations: 298.7 MB / 0.5546 GB, free: 9 MB / 446.1 MB
Notification: Performance of NFInst.instExpressions: time 0.04204/1.756, allocations: 37.19 MB / 0.5909 GB, free: 3.664 MB / 478.1 MB
Notification: Performance of NFInst.updateImplicitVariability: time 0.0006533/1.756, allocations: 8 kB / 0.5909 GB, free: 3.656 MB / 478.1 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).
Notification: Performance of NFTyping.typeComponents: time 0.000792/1.757, allocations: 307.9 kB / 0.5912 GB, free: 3.355 MB / 478.1 MB
Notification: Performance of NFTyping.typeBindings: time 0.0009734/1.758, allocations: 0.496 MB / 0.5917 GB, free: 2.855 MB / 478.1 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 0.02511/1.783, allocations: 10.28 MB / 0.6017 GB, free: 8.566 MB / 494.1 MB
Notification: Performance of NFFlatten.flatten: time 0.002161/1.785, allocations: 1.767 MB / 0.6034 GB, free: 6.789 MB / 494.1 MB
Notification: Performance of NFFlatten.resolveConnections: time 0.0005759/1.786, allocations: 0.5292 MB / 0.6039 GB, free: 6.25 MB / 494.1 MB
Notification: Performance of NFEvalConstants.evaluate: time 0.0007205/1.787, allocations: 0.6733 MB / 0.6046 GB, free: 5.574 MB / 494.1 MB
Notification: Performance of NFSimplifyModel.simplify: time 0.0004992/1.787, allocations: 0.5598 MB / 0.6051 GB, free: 5.012 MB / 494.1 MB
Notification: Performance of NFPackage.collectConstants: time 0.0001088/1.787, allocations: 92 kB / 0.6052 GB, free: 4.922 MB / 494.1 MB
Notification: Performance of NFFlatten.collectFunctions: time 0.02639/1.814, allocations: 15.98 MB / 0.6208 GB, free: 4.918 MB / 0.4981 GB
Notification: Performance of NFScalarize.scalarize: time 0.0002531/1.814, allocations: 227 kB / 0.6211 GB, free: 4.695 MB / 0.4981 GB
Notification: Performance of NFVerifyModel.verify: time 0.0008146/1.815, allocations: 0.6451 MB / 0.6217 GB, free: 4.047 MB / 0.4981 GB
Notification: Performance of NFConvertDAE.convert: time 0.01692/1.832, allocations: 9.016 MB / 0.6305 GB, free: 11.01 MB / 0.5137 GB
Notification: Performance of FrontEnd - DAE generated: time 5.13e-06/1.832, allocations: 0 / 0.6305 GB, free: 11.01 MB / 0.5137 GB
Notification: Performance of FrontEnd: time 1.864e-06/1.832, allocations: 0 / 0.6305 GB, free: 11.01 MB / 0.5137 GB
Notification: Performance of Transformations before backend: time 1.433e-05/1.832, allocations: 0 / 0.6305 GB, free: 11.01 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: 407
 * Number of variables: 407
Notification: Performance of Generate backend data structure: time 0.005049/1.837, allocations: 2.279 MB / 0.6327 GB, free: 8.676 MB / 0.5137 GB
Notification: Performance of prepare preOptimizeDAE: time 3.821e-05/1.837, allocations: 8.031 kB / 0.6327 GB, free: 8.668 MB / 0.5137 GB
Notification: Performance of preOpt normalInlineFunction (simulation): time 0.0001812/1.837, allocations: 134.2 kB / 0.6329 GB, free: 8.535 MB / 0.5137 GB
Notification: Performance of preOpt evaluateParameters (simulation): time 0.0005164/1.838, allocations: 476.6 kB / 0.6333 GB, free: 8.023 MB / 0.5137 GB
Notification: Performance of preOpt simplifyIfEquations (simulation): time 0.0001869/1.838, allocations: 180.8 kB / 0.6335 GB, free: 7.82 MB / 0.5137 GB
Notification: Performance of preOpt expandDerOperator (simulation): time 9.9e-05/1.838, allocations: 83.98 kB / 0.6336 GB, free: 7.738 MB / 0.5137 GB
Notification: Performance of preOpt clockPartitioning (simulation): time 0.001733/1.84, allocations: 1.395 MB / 0.6349 GB, free: 6.262 MB / 0.5137 GB
Notification: Performance of preOpt findStateOrder (simulation): time 2.343e-05/1.84, allocations: 7.875 kB / 0.6349 GB, free: 6.254 MB / 0.5137 GB
Notification: Performance of preOpt replaceEdgeChange (simulation): time 7.252e-05/1.84, allocations: 40 kB / 0.635 GB, free: 6.215 MB / 0.5137 GB
Notification: Performance of preOpt inlineArrayEqn (simulation): time 5.114e-05/1.84, allocations: 71.92 kB / 0.635 GB, free: 6.145 MB / 0.5137 GB
Notification: Performance of preOpt removeEqualRHS (simulation): time 0.001411/1.841, allocations: 0.9884 MB / 0.636 GB, free: 5.152 MB / 0.5137 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 0.005182/1.846, allocations: 6.357 MB / 0.6422 GB, free: 14.23 MB / 0.5294 GB
Notification: Performance of preOpt comSubExp (simulation): time 0.001116/1.848, allocations: 0.8498 MB / 0.643 GB, free: 13.38 MB / 0.5294 GB
Notification: Performance of preOpt resolveLoops (simulation): time 0.0007764/1.848, allocations: 0.6847 MB / 0.6437 GB, free: 12.69 MB / 0.5294 GB
Notification: Performance of preOpt evalFunc (simulation): time 0.3477/2.196, allocations: 80.99 MB / 0.7228 GB, free: 208 MB / 0.5919 GB
Notification: Performance of preOpt encapsulateWhenConditions (simulation): time 3.727e-05/2.196, allocations: 37.53 kB / 0.7228 GB, free: 208 MB / 0.5919 GB
Notification: Performance of pre-optimization done (n=247): time 3.576e-06/2.196, allocations: 0 / 0.7228 GB, free: 208 MB / 0.5919 GB
Notification: Performance of matching and sorting (n=247): time 0.007469/2.204, allocations: 3.679 MB / 0.7264 GB, free: 207.4 MB / 0.5919 GB
Notification: Performance of inlineWhenForInitialization (initialization): time 1.921e-05/2.204, allocations: 59.42 kB / 0.7265 GB, free: 207.4 MB / 0.5919 GB
Notification: Performance of selectInitializationVariablesDAE (initialization): time 0.0004871/2.204, allocations: 0.4944 MB / 0.727 GB, free: 207.2 MB / 0.5919 GB
Notification: Performance of collectPreVariables (initialization): time 3.597e-05/2.204, allocations: 36.11 kB / 0.727 GB, free: 207.2 MB / 0.5919 GB
Notification: Performance of collectInitialEqns (initialization): time 0.000167/2.204, allocations: 325.3 kB / 0.7273 GB, free: 207.1 MB / 0.5919 GB
Notification: Performance of collectInitialBindings (initialization): time 0.0003619/2.205, allocations: 0.7743 MB / 0.7281 GB, free: 206.5 MB / 0.5919 GB
Notification: Performance of simplifyInitialFunctions (initialization): time 0.000231/2.205, allocations: 215.5 kB / 0.7283 GB, free: 206.5 MB / 0.5919 GB
Notification: Performance of setup shared object (initialization): time 7.93e-05/2.205, allocations: 343.9 kB / 0.7286 GB, free: 206.2 MB / 0.5919 GB
Notification: Performance of preBalanceInitialSystem (initialization): time 0.0006156/2.206, allocations: 0.5023 MB / 0.7291 GB, free: 206.2 MB / 0.5919 GB
Notification: Performance of partitionIndependentBlocks (initialization): time 0.0007453/2.206, allocations: 0.7189 MB / 0.7298 GB, free: 206 MB / 0.5919 GB
Notification: Performance of analyzeInitialSystem (initialization): time 0.001527/2.208, allocations: 1.406 MB / 0.7312 GB, free: 205.7 MB / 0.5919 GB
Notification: Performance of solveInitialSystemEqSystem (initialization): time 5.59e-06/2.208, allocations: 2.219 kB / 0.7312 GB, free: 205.7 MB / 0.5919 GB
Notification: Performance of matching and sorting (n=268) (initialization): time 0.002617/2.211, allocations: 2.022 MB / 0.7332 GB, free: 205.5 MB / 0.5919 GB
Notification: Performance of prepare postOptimizeDAE: time 2.206e-05/2.211, allocations: 7.969 kB / 0.7332 GB, free: 205.5 MB / 0.5919 GB
Notification: Performance of postOpt simplifyComplexFunction (initialization): time 2.102e-05/2.211, allocations: 5.875 kB / 0.7332 GB, free: 205.5 MB / 0.5919 GB
Notification: Performance of postOpt tearingSystem (initialization): time 0.004014/2.215, allocations: 2.498 MB / 0.7356 GB, free: 205.4 MB / 0.5919 GB
Notification: Performance of postOpt solveSimpleEquations (initialization): time 0.0001076/2.215, allocations: 25.12 kB / 0.7356 GB, free: 205.4 MB / 0.5919 GB
Notification: Performance of postOpt calculateStrongComponentJacobians (initialization): time 0.003038/2.218, allocations: 3.711 MB / 0.7393 GB, free: 203.3 MB / 0.5919 GB
Notification: Performance of postOpt simplifyAllExpressions (initialization): time 0.0005922/2.218, allocations: 151.3 kB / 0.7394 GB, free: 203.2 MB / 0.5919 GB
Notification: Performance of postOpt collapseArrayExpressions (initialization): time 6.294e-05/2.219, allocations: 37.5 kB / 0.7394 GB, free: 203.2 MB / 0.5919 GB
Notification: Model statistics after passing the back-end for initialization:
 * Number of independent subsystems: 23
 * Number of states: 0 ()
 * Number of discrete variables: 20 (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 (34):
 * Single equations (assignments): 23
 * Array equations: 0
 * Algorithm blocks: 0
 * Record equations: 7
 * When equations: 0
 * If-equations: 0
 * Equation systems (not torn): 0
 * Torn equation systems: 4
 * 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): 4 systems
   {(1,3), (1,3), (1,3), (11,22)}
Notification: Performance of prepare postOptimizeDAE: time 0.0003618/2.219, allocations: 253.4 kB / 0.7397 GB, free: 203.1 MB / 0.5919 GB
Notification: Performance of postOpt lateInlineFunction (simulation): time 0.000118/2.219, allocations: 96.64 kB / 0.7398 GB, free: 203 MB / 0.5919 GB
Notification: Performance of postOpt wrapFunctionCalls (simulation): time 0.003284/2.222, allocations: 3.114 MB / 0.7428 GB, free: 202.7 MB / 0.5919 GB
Notification: Performance of postOpt simplifysemiLinear (simulation): time 9.267e-06/2.222, allocations: 3.844 kB / 0.7428 GB, free: 202.7 MB / 0.5919 GB
Notification: Performance of postOpt simplifyComplexFunction (simulation): time 6.372e-06/2.222, allocations: 0.6562 kB / 0.7428 GB, free: 202.7 MB / 0.5919 GB
Notification: Performance of postOpt removeConstants (simulation): time 0.0003241/2.223, allocations: 318.3 kB / 0.7431 GB, free: 202.5 MB / 0.5919 GB
Notification: Performance of postOpt simplifyTimeIndepFuncCalls (simulation): time 7.535e-05/2.223, allocations: 21.92 kB / 0.7431 GB, free: 202.5 MB / 0.5919 GB
Notification: Performance of postOpt simplifyAllExpressions (simulation): time 0.0003683/2.223, allocations: 23.66 kB / 0.7432 GB, free: 202.5 MB / 0.5919 GB
Notification: Performance of postOpt findZeroCrossings (simulation): time 0.0001096/2.223, allocations: 41.09 kB / 0.7432 GB, free: 202.5 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(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) = $cse15

Variables:
1: singularPressureLoss2.pro.duph:VARIABLE(unit = "m3/kg" )  "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real
2: singularPressureLoss2.pro.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific entropy" type: Real
3: singularPressureLoss2.pro.duhp:VARIABLE(unit = "1" )  "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real
4: singularPressureLoss2.pro.ddph:VARIABLE(unit = "s2/m2" )  "Derivative of density wrt. pressure at constant specific enthalpy" type: Real
5: singularPressureLoss2.pro.ddhp:VARIABLE(unit = "kg.s2/m5" )  "Derivative of density wrt. specific enthalpy at constant pressure" type: Real
6: singularPressureLoss2.pro.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 )  "Specific inner energy" type: Real
7: singularPressureLoss2.pro.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific heat capacity at constant presure" type: Real
8: $cse15.ddph:VARIABLE(protected = true )  type: Real unreplaceable
9: $cse15.cp:VARIABLE(protected = true )  type: Real unreplaceable
10: $cse15.x:VARIABLE(protected = true )  type: Real unreplaceable
[/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 Source_condenseur1.Q0 > 0.0 then singularPressureLoss1.h - Source_condenseur1.h0 else singularPressureLoss1.h - nTUWaterHeating.h
2/2 (1): 0.0 = if singularPressureLoss3.Q > 0.0 then singularPressureLoss3.h - sourceP.h0 else singularPressureLoss3.h - nTUWaterHeating.h
3/3 (10): $cse13 = ThermoSysPro.Properties.Fluid.Ph(singularPressureLoss3.Pm, singularPressureLoss3.h, singularPressureLoss3.mode, singularPressureLoss3.fluid)
4/13 (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) = $cse13
5/23 (1): singularPressureLoss3.Pm = 0.5 * (sourceP.P0 + nTUWaterHeating.P)
6/24 (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)
7/38 (1): nTUWaterHeating.Wcond = Source_condenseur.Q0 * nTUWaterHeating.promcF.cp * $cse7 * (nTUWaterHeating.TsatC - nTUWaterHeating.TeiF)
8/39 (10): $cse3 = ThermoSysPro.Properties.WaterSteam.IF97.Water_Ph(singularPressureLoss2.C2.P, nTUWaterHeating.HeiF, nTUWaterHeating.mode_eeF)
9/49 (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) = $cse3
10/59 (10): nTUWaterHeating.promcF = ThermoSysPro.Properties.WaterSteam.IF97.Water_Ph(0.5 * (singularPressureLoss2.C2.P + nTUWaterHeating.Se.P), 0.5 * (nTUWaterHeating.HeiF + nTUWaterHeating.HDesF), nTUWaterHeating.mode_mF)
11/69 (1): $cse7 = ThermoSysPro.Correlations.Thermal.WBHeatExchangerEfficiency(singularPressureLoss3.Q, Source_condenseur.Q0, 1e20, nTUWaterHeating.promcF.cp, nTUWaterHeating.KCond, nTUWaterHeating.SCondDes - 1e-9, 0.5)
12/70 (10): nTUWaterHeating.prompF = ThermoSysPro.Properties.WaterSteam.IF97.Water_Ph(singularPressureLoss2.C2.P, 0.5 * (singularPressureLoss2.h + nTUWaterHeating.HeiF), nTUWaterHeating.mode_eeF)
13/80 (1): nTUWaterHeating.Wcond = Source_condenseur.Q0 * (nTUWaterHeating.HDesF - nTUWaterHeating.HeiF)
14/81 (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
15/82 (1): nTUWaterHeating.Wflash = if nTUWaterHeating.flashepC.x > 0.0 then Source_condenseur1.Q0 * (singularPressureLoss1.h - nTUWaterHeating.HsateC) else 0.0
16/83 (10): nTUWaterHeating.flashepC = ThermoSysPro.Properties.WaterSteam.IF97.Water_Ph(nTUWaterHeating.P, singularPressureLoss1.h, nTUWaterHeating.mode_flash)
17/93 (1): 0.0 = if nTUWaterHeating.flashepC.x > 0.0 then nTUWaterHeating.Hep - nTUWaterHeating.HsateC else singularPressureLoss5.Q * nTUWaterHeating.Hep - (nTUWaterHeating.HsateC * singularPressureLoss3.Q + singularPressureLoss1.h * Source_condenseur1.Q0)
18/94 (1): $cse14 = ThermoSysPro.Functions.ThermoSquare(singularPressureLoss3.Q, singularPressureLoss3.eps)
19/95 (1): singularPressureLoss3.deltaP = singularPressureLoss3.K * $cse14 / singularPressureLoss3.rho
20/96 (1): singularPressureLoss5.Q = singularPressureLoss3.Q + Source_condenseur1.Q0
21/97 (1): $cse5 = min(singularPressureLoss5.Q * nTUWaterHeating.prompC.cp, Source_condenseur.Q0 * nTUWaterHeating.prompF.cp)
22/98 (1): nTUWaterHeating.Wpurge = $cse5 * $cse6 * (nTUWaterHeating.prosp.T - nTUWaterHeating.proeeF.T)
23/99 (1): $cse6 = ThermoSysPro.Correlations.Thermal.WBHeatExchangerEfficiency(singularPressureLoss5.Q, Source_condenseur.Q0, nTUWaterHeating.prompC.cp, nTUWaterHeating.prompF.cp, nTUWaterHeating.KPurge, 656.0, 0.0)
24/100 (1): 0.0 = if singularPressureLoss5.Q > 0.0 then singularPressureLoss5.h - nTUWaterHeating.h else singularPressureLoss5.h - Puit_condenseur1.h0
25/101 (10): nTUWaterHeating.prompC = ThermoSysPro.Properties.WaterSteam.IF97.Water_Ph(nTUWaterHeating.P, 0.5 * (nTUWaterHeating.Hep + singularPressureLoss5.h), nTUWaterHeating.mode_spC)
26/111 (1): nTUWaterHeating.Wpurge = singularPressureLoss5.Q * (nTUWaterHeating.Hep - singularPressureLoss5.h)
27/112 (10): nTUWaterHeating.prosp = ThermoSysPro.Properties.WaterSteam.IF97.Water_Ph(nTUWaterHeating.P, nTUWaterHeating.Hep, nTUWaterHeating.mode_spC)
28/122 (1): nTUWaterHeating.Wpurge = Source_condenseur.Q0 * (nTUWaterHeating.HeiF - singularPressureLoss2.h)
29/123 (10): $cse4 = ThermoSysPro.Properties.WaterSteam.IF97.Water_Ph(0.5 * (singularPressureLoss2.C2.P + nTUWaterHeating.Se.P), 0.5 * (singularPressureLoss2.h + nTUWaterHeating.HDesF), nTUWaterHeating.mode_eeF)
30/133 (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) = $cse4
31/143 (1): singularPressureLoss2.C2.P - nTUWaterHeating.Se.P = nTUWaterHeating.lambdaE * $cse8 / nTUWaterHeating.rho
32/144 (10): nTUWaterHeating.proeeF = ThermoSysPro.Properties.WaterSteam.IF97.Water_Ph(singularPressureLoss2.C2.P, singularPressureLoss2.h, nTUWaterHeating.mode_eeF)
33/154 (1): Source_condenseur.P0 - singularPressureLoss2.C2.P = singularPressureLoss2.deltaP
34/155 (1): singularPressureLoss2.deltaP = singularPressureLoss2.K * $cse16 / singularPressureLoss2.rho
35/156 (10): $cse15 = ThermoSysPro.Properties.Fluid.Ph(singularPressureLoss2.Pm, singularPressureLoss2.h, singularPressureLoss2.mode, singularPressureLoss2.fluid)
36/166 (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) = $cse15
37/176 (1): 0.0 = if Source_condenseur.Q0 > 0.0 then singularPressureLoss2.h - Source_condenseur.h0 else singularPressureLoss2.h - singularPressureLoss2.C2.h_vol
38/177 (1): 0.0 = if noEvent(Source_condenseur.Q0 > 0.0) then singularPressureLoss2.h - singularPressureLoss2.C2.h_vol else nTUWaterHeating.HDesF - nTUWaterHeating.Se.h_vol
39/178 (1): 0.0 = if Source_condenseur.Q0 > 0.0 then nTUWaterHeating.HDesF - nTUWaterHeating.Se.h_vol else nTUWaterHeating.HDesF - Puit_condenseur.h0
40/179 (1): singularPressureLoss2.Pm = 0.5 * (Source_condenseur.P0 + singularPressureLoss2.C2.P)
41/180 (1): sourceP.P0 - nTUWaterHeating.P = singularPressureLoss3.deltaP

Variables:
1: singularPressureLoss3.deltaP:VARIABLE(unit = "Pa" )  "Singular pressure loss" type: Real
2: singularPressureLoss2.Pm:VARIABLE(min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 )  "Average fluid pressure" type: Real
3: nTUWaterHeating.HDesF:VARIABLE(start = 9e5 unit = "J/kg" )  "Fluid specific enthalpy after deheating" type: Real
4: nTUWaterHeating.Se.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" )  "Fluid specific enthalpy in the control volume" type: Real
5: singularPressureLoss2.C2.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" )  "Fluid specific enthalpy in the control volume" type: Real
6: singularPressureLoss2.pro.duph:VARIABLE(unit = "m3/kg" )  "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real
7: singularPressureLoss2.pro.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific entropy" type: Real
8: singularPressureLoss2.pro.duhp:VARIABLE(unit = "1" )  "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real
9: singularPressureLoss2.pro.ddph:VARIABLE(unit = "s2/m2" )  "Derivative of density wrt. pressure at constant specific enthalpy" type: Real
10: singularPressureLoss2.pro.ddhp:VARIABLE(unit = "kg.s2/m5" )  "Derivative of density wrt. specific enthalpy at constant pressure" type: Real
11: singularPressureLoss2.pro.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 )  "Specific inner energy" type: Real
12: singularPressureLoss2.pro.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific heat capacity at constant presure" type: Real
13: $cse15.ddph:VARIABLE(protected = true )  type: Real unreplaceable
14: $cse15.cp:VARIABLE(protected = true )  type: Real unreplaceable
15: $cse15.x:VARIABLE(protected = true )  type: Real unreplaceable
16: singularPressureLoss2.h:VARIABLE(start = 1e5 unit = "J/kg" )  "Fluid specific enthalpy" type: Real
17: $cse15.T:VARIABLE(protected = true )  type: Real unreplaceable
18: $cse15.ddhp:VARIABLE(protected = true )  type: Real unreplaceable
19: $cse15.duhp:VARIABLE(protected = true )  type: Real unreplaceable
20: $cse15.s:VARIABLE(protected = true )  type: Real unreplaceable
21: $cse15.d:VARIABLE(protected = true )  type: Real unreplaceable
22: $cse15.u:VARIABLE(protected = true )  type: Real unreplaceable
23: $cse15.duph:VARIABLE(protected = true )  type: Real unreplaceable
24: singularPressureLoss2.pro.x:VARIABLE(min = 0.0 max = 1.0 unit = "1" )  "Vapor mass fraction" type: Real
25: singularPressureLoss2.T:VARIABLE(min = 200.0 max = 6000.0 start = 290.0 unit = "K" nominal = 300.0 )  "Fluid temperature" type: Real
26: singularPressureLoss2.rho:VARIABLE(min = 1e-9 max = 1e5 start = 998.0 unit = "kg/m3" nominal = 998.0 )  "Fluid density" type: Real
27: singularPressureLoss2.deltaP:VARIABLE(unit = "Pa" )  "Singular pressure loss" type: Real
28: nTUWaterHeating.proeeF.x:VARIABLE(min = 0.0 max = 1.0 unit = "1" )  "Vapor mass fraction" type: Real
29: nTUWaterHeating.proeeF.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific entropy" type: Real
30: nTUWaterHeating.proeeF.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 )  "Specific inner energy" type: Real
31: nTUWaterHeating.proeeF.ddph:VARIABLE(unit = "s2/m2" )  "Derivative of density wrt. pressure at constant specific enthalpy" type: Real
32: nTUWaterHeating.proeeF.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 )  "Density" type: Real
33: nTUWaterHeating.proeeF.duph:VARIABLE(unit = "m3/kg" )  "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real
34: nTUWaterHeating.proeeF.duhp:VARIABLE(unit = "1" )  "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real
35: nTUWaterHeating.proeeF.ddhp:VARIABLE(unit = "kg.s2/m5" )  "Derivative of density wrt. specific enthalpy at constant pressure" type: Real
36: nTUWaterHeating.proeeF.T:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 320.0 )  "Temperature" type: Real
37: nTUWaterHeating.proeeF.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific heat capacity at constant presure" type: Real
38: nTUWaterHeating.rho:VARIABLE(min = 1e-9 max = 1e5 start = 1000.0 unit = "kg/m3" nominal = 998.0 )  "Average water density" type: Real
39: nTUWaterHeating.promeF.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 )  "Specific inner energy" type: Real
40: nTUWaterHeating.promeF.duhp:VARIABLE(unit = "1" )  "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real
41: nTUWaterHeating.promeF.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific heat capacity at constant presure" type: Real
42: nTUWaterHeating.promeF.T:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 320.0 )  "Temperature" type: Real
43: nTUWaterHeating.promeF.duph:VARIABLE(unit = "m3/kg" )  "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real
44: $cse4.duph:VARIABLE(protected = true )  type: Real unreplaceable
45: nTUWaterHeating.promeF.x:VARIABLE(min = 0.0 max = 1.0 unit = "1" )  "Vapor mass fraction" type: Real
46: nTUWaterHeating.promeF.ddhp:VARIABLE(unit = "kg.s2/m5" )  "Derivative of density wrt. specific enthalpy at constant pressure" type: Real
47: nTUWaterHeating.promeF.ddph:VARIABLE(unit = "s2/m2" )  "Derivative of density wrt. pressure at constant specific enthalpy" type: Real
48: nTUWaterHeating.promeF.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific entropy" type: Real
49: $cse4.d:VARIABLE(protected = true )  type: Real unreplaceable
50: $cse4.ddph:VARIABLE(protected = true )  type: Real unreplaceable
51: $cse4.x:VARIABLE(protected = true )  type: Real unreplaceable
52: $cse4.duhp:VARIABLE(protected = true )  type: Real unreplaceable
53: $cse4.ddhp:VARIABLE(protected = true )  type: Real unreplaceable
54: $cse4.s:VARIABLE(protected = true )  type: Real unreplaceable
55: $cse4.T:VARIABLE(protected = true )  type: Real unreplaceable
56: $cse4.cp:VARIABLE(protected = true )  type: Real unreplaceable
57: nTUWaterHeating.Se.P:VARIABLE(flow=false min = 0.0 start = 8e6 unit = "Pa" nominal = 1e5 )  "Fluid pressure in the control volume" type: Real
58: $cse4.u:VARIABLE(protected = true )  type: Real unreplaceable
59: nTUWaterHeating.Wpurge:VARIABLE(start = 1.0 unit = "W" )  "Energy transfer during drain cooling" type: Real
60: nTUWaterHeating.prosp.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific heat capacity at constant presure" type: Real
61: nTUWaterHeating.prosp.duhp:VARIABLE(unit = "1" )  "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real
62: nTUWaterHeating.prosp.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 )  "Density" type: Real
63: nTUWaterHeating.prosp.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific entropy" type: Real
64: nTUWaterHeating.prosp.ddhp:VARIABLE(unit = "kg.s2/m5" )  "Derivative of density wrt. specific enthalpy at constant pressure" type: Real
65: nTUWaterHeating.prosp.x:VARIABLE(min = 0.0 max = 1.0 unit = "1" )  "Vapor mass fraction" type: Real
66: nTUWaterHeating.prosp.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 )  "Specific inner energy" type: Real
67: nTUWaterHeating.prosp.T:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 320.0 )  "Temperature" type: Real
68: nTUWaterHeating.prosp.duph:VARIABLE(unit = "m3/kg" )  "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real
69: nTUWaterHeating.prosp.ddph:VARIABLE(unit = "s2/m2" )  "Derivative of density wrt. pressure at constant specific enthalpy" type: Real
70: nTUWaterHeating.Hep:VARIABLE(start = 5e5 unit = "J/kg" )  "Mixing specific enthalpy of the drain and the condensate" type: Real
71: nTUWaterHeating.prompC.duhp:VARIABLE(unit = "1" )  "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real
72: nTUWaterHeating.prompC.ddph:VARIABLE(unit = "s2/m2" )  "Derivative of density wrt. pressure at constant specific enthalpy" type: Real
73: nTUWaterHeating.prompC.ddhp:VARIABLE(unit = "kg.s2/m5" )  "Derivative of density wrt. specific enthalpy at constant pressure" type: Real
74: nTUWaterHeating.prompC.x:VARIABLE(min = 0.0 max = 1.0 unit = "1" )  "Vapor mass fraction" type: Real
75: nTUWaterHeating.prompC.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific heat capacity at constant presure" type: Real
76: nTUWaterHeating.prompC.duph:VARIABLE(unit = "m3/kg" )  "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real
77: nTUWaterHeating.prompC.T:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 320.0 )  "Temperature" type: Real
78: nTUWaterHeating.prompC.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific entropy" type: Real
79: nTUWaterHeating.prompC.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 )  "Specific inner energy" type: Real
80: nTUWaterHeating.prompC.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 )  "Density" type: Real
81: singularPressureLoss5.h:VARIABLE(start = 1e5 unit = "J/kg" )  "Fluid specific enthalpy" type: Real
82: nTUWaterHeating.prompF.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific heat capacity at constant presure" type: Real
83: $cse6:VARIABLE(protected = true )  type: Real unreplaceable
84: $cse5:VARIABLE(protected = true )  type: Real unreplaceable
85: singularPressureLoss5.Q:VARIABLE(start = 100.0 unit = "kg/s" )  "Mass flow rate" type: Real
86: singularPressureLoss3.rho:VARIABLE(min = 1e-9 max = 1e5 start = 998.0 unit = "kg/m3" nominal = 998.0 )  "Fluid density" type: Real
87: $cse14:VARIABLE(protected = true )  type: Real unreplaceable
88: singularPressureLoss3.Q:VARIABLE(start = 100.0 unit = "kg/s" )  "Mass flow rate" type: Real
89: nTUWaterHeating.flashepC.T:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 320.0 )  "Temperature" type: Real
90: nTUWaterHeating.flashepC.ddhp:VARIABLE(unit = "kg.s2/m5" )  "Derivative of density wrt. specific enthalpy at constant pressure" type: Real
91: nTUWaterHeating.flashepC.duph:VARIABLE(unit = "m3/kg" )  "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real
92: nTUWaterHeating.flashepC.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 )  "Density" type: Real
93: nTUWaterHeating.flashepC.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 )  "Specific inner energy" type: Real
94: nTUWaterHeating.flashepC.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific entropy" type: Real
95: nTUWaterHeating.flashepC.x:VARIABLE(min = 0.0 max = 1.0 unit = "1" )  "Vapor mass fraction" type: Real
96: nTUWaterHeating.flashepC.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific heat capacity at constant presure" type: Real
97: nTUWaterHeating.flashepC.ddph:VARIABLE(unit = "s2/m2" )  "Derivative of density wrt. pressure at constant specific enthalpy" type: Real
98: nTUWaterHeating.flashepC.duhp:VARIABLE(unit = "1" )  "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real
99: singularPressureLoss1.h:VARIABLE(start = 1e5 unit = "J/kg" )  "Fluid specific enthalpy" type: Real
100: nTUWaterHeating.Wflash:VARIABLE(start = 1.0 unit = "W" )  "Energy transfer during partial vaporisation in the drain" type: Real
101: nTUWaterHeating.Wcond:VARIABLE(start = 1.0 unit = "W" )  "Energy transfer during condensation" type: Real
102: nTUWaterHeating.prompF.T:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 320.0 )  "Temperature" type: Real
103: nTUWaterHeating.prompF.duhp:VARIABLE(unit = "1" )  "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real
104: nTUWaterHeating.prompF.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific entropy" type: Real
105: nTUWaterHeating.prompF.x:VARIABLE(min = 0.0 max = 1.0 unit = "1" )  "Vapor mass fraction" type: Real
106: nTUWaterHeating.prompF.duph:VARIABLE(unit = "m3/kg" )  "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real
107: nTUWaterHeating.prompF.ddhp:VARIABLE(unit = "kg.s2/m5" )  "Derivative of density wrt. specific enthalpy at constant pressure" type: Real
108: nTUWaterHeating.prompF.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 )  "Density" type: Real
109: nTUWaterHeating.prompF.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 )  "Specific inner energy" type: Real
110: nTUWaterHeating.HeiF:VARIABLE(start = 9e5 unit = "J/kg" )  "Fluid specific enthalpy after drain cooling" type: Real
111: nTUWaterHeating.prompF.ddph:VARIABLE(unit = "s2/m2" )  "Derivative of density wrt. pressure at constant specific enthalpy" type: Real
112: $cse7:VARIABLE(protected = true )  type: Real unreplaceable
113: nTUWaterHeating.promcF.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific entropy" type: Real
114: nTUWaterHeating.promcF.duhp:VARIABLE(unit = "1" )  "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real
115: nTUWaterHeating.promcF.ddph:VARIABLE(unit = "s2/m2" )  "Derivative of density wrt. pressure at constant specific enthalpy" type: Real
116: nTUWaterHeating.promcF.T:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 320.0 )  "Temperature" type: Real
117: nTUWaterHeating.promcF.duph:VARIABLE(unit = "m3/kg" )  "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real
118: nTUWaterHeating.promcF.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 )  "Specific inner energy" type: Real
119: nTUWaterHeating.promcF.ddhp:VARIABLE(unit = "kg.s2/m5" )  "Derivative of density wrt. specific enthalpy at constant pressure" type: Real
120: nTUWaterHeating.promcF.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 )  "Density" type: Real
121: nTUWaterHeating.promcF.x:VARIABLE(min = 0.0 max = 1.0 unit = "1" )  "Vapor mass fraction" type: Real
122: nTUWaterHeating.promcF.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific heat capacity at constant presure" type: Real
123: nTUWaterHeating.proecF.duph:VARIABLE(unit = "m3/kg" )  "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real
124: nTUWaterHeating.proecF.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific heat capacity at constant presure" type: Real
125: nTUWaterHeating.proecF.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 )  "Specific inner energy" type: Real
126: nTUWaterHeating.proecF.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific entropy" type: Real
127: $cse3.d:VARIABLE(protected = true )  type: Real unreplaceable
128: $cse3.cp:VARIABLE(protected = true )  type: Real unreplaceable
129: $cse3.duhp:VARIABLE(protected = true )  type: Real unreplaceable
130: singularPressureLoss2.C2.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 )  "Fluid pressure in the control volume" type: Real
131: $cse3.s:VARIABLE(protected = true )  type: Real unreplaceable
132: $cse3.u:VARIABLE(protected = true )  type: Real unreplaceable
133: $cse3.ddhp:VARIABLE(protected = true )  type: Real unreplaceable
134: $cse3.duph:VARIABLE(protected = true )  type: Real unreplaceable
135: $cse3.ddph:VARIABLE(protected = true )  type: Real unreplaceable
136: $cse3.T:VARIABLE(protected = true )  type: Real unreplaceable
137: $cse3.x:VARIABLE(protected = true )  type: Real unreplaceable
138: nTUWaterHeating.proecF.x:VARIABLE(min = 0.0 max = 1.0 unit = "1" )  "Vapor mass fraction" type: Real
139: nTUWaterHeating.proecF.ddhp:VARIABLE(unit = "kg.s2/m5" )  "Derivative of density wrt. specific enthalpy at constant pressure" type: Real
140: nTUWaterHeating.proecF.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 )  "Density" type: Real
141: nTUWaterHeating.proecF.duhp:VARIABLE(unit = "1" )  "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real
142: nTUWaterHeating.proecF.ddph:VARIABLE(unit = "s2/m2" )  "Derivative of density wrt. pressure at constant specific enthalpy" type: Real
143: nTUWaterHeating.TeiF:VARIABLE(min = 200.0 max = 6000.0 start = 400.0 unit = "K" nominal = 300.0 )  "Fluid temperature after drain cooling" type: Real
144: nTUWaterHeating.vsatC.rho:VARIABLE(min = 0.0 unit = "kg/m3" )  "Density" type: Real
145: nTUWaterHeating.vsatC.cp:VARIABLE(unit = "J/(kg.K)" )  "Specific heat capacity at constant pressure" type: Real
146: nTUWaterHeating.TsatC:VARIABLE(min = 0.0 start = 400.0 unit = "K" nominal = 300.0 )  "Saturation temperature" type: Real
147: nTUWaterHeating.vsatC.P:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 )  "Pressure" type: Real
148: nTUWaterHeating.vsatC.cv:VARIABLE(unit = "J/(kg.K)" )  "Specific heat capacity at constant volume" type: Real
149: nTUWaterHeating.lsatC.P:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 )  "Pressure" type: Real
150: nTUWaterHeating.lsatC.cp:VARIABLE(unit = "J/(kg.K)" )  "Specific heat capacity at constant pressure" type: Real
151: nTUWaterHeating.lsatC.cv:VARIABLE(unit = "J/(kg.K)" )  "Specific heat capacity at constant volume" type: Real
152: nTUWaterHeating.vsatC.T:VARIABLE(min = 0.0 start = 288.15 unit = "K" nominal = 300.0 )  "Temperature" type: Real
153: 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
154: 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
155: nTUWaterHeating.lsatC.pt:VARIABLE()  "Derivative of pressure wrt. temperature" type: Real
156: nTUWaterHeating.vsatC.pt:VARIABLE()  "Derivative of pressure wrt. temperature" type: Real
157: nTUWaterHeating.lsatC.rho:VARIABLE(min = 0.0 unit = "kg/m3" )  "Density" type: Real
158: nTUWaterHeating.P:VARIABLE(min = 0.0 start = 1e6 unit = "Pa" nominal = 1e5 )  "Fluid pressure" type: Real
159: singularPressureLoss3.pro.ddhp:VARIABLE(unit = "kg.s2/m5" )  "Derivative of density wrt. specific enthalpy at constant pressure" type: Real
160: singularPressureLoss3.pro.duph:VARIABLE(unit = "m3/kg" )  "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real
161: singularPressureLoss3.pro.duhp:VARIABLE(unit = "1" )  "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real
162: singularPressureLoss3.pro.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific heat capacity at constant presure" type: Real
163: $cse13.duhp:VARIABLE(protected = true )  type: Real unreplaceable
164: singularPressureLoss3.T:VARIABLE(min = 200.0 max = 6000.0 start = 290.0 unit = "K" nominal = 300.0 )  "Fluid temperature" type: Real
165: singularPressureLoss3.pro.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific entropy" type: Real
166: singularPressureLoss3.pro.x:VARIABLE(min = 0.0 max = 1.0 unit = "1" )  "Vapor mass fraction" type: Real
167: singularPressureLoss3.pro.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 )  "Specific inner energy" type: Real
168: singularPressureLoss3.pro.ddph:VARIABLE(unit = "s2/m2" )  "Derivative of density wrt. pressure at constant specific enthalpy" type: Real
169: $cse13.cp:VARIABLE(protected = true )  type: Real unreplaceable
170: singularPressureLoss3.Pm:VARIABLE(min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 )  "Average fluid pressure" type: Real
171: $cse13.ddhp:VARIABLE(protected = true )  type: Real unreplaceable
172: $cse13.ddph:VARIABLE(protected = true )  type: Real unreplaceable
173: $cse13.x:VARIABLE(protected = true )  type: Real unreplaceable
174: $cse13.u:VARIABLE(protected = true )  type: Real unreplaceable
175: $cse13.duph:VARIABLE(protected = true )  type: Real unreplaceable
176: $cse13.s:VARIABLE(protected = true )  type: Real unreplaceable
177: $cse13.T:VARIABLE(protected = true )  type: Real unreplaceable
178: $cse13.d:VARIABLE(protected = true )  type: Real unreplaceable
179: singularPressureLoss3.h:VARIABLE(start = 1e5 unit = "J/kg" )  "Fluid specific enthalpy" type: Real
180: nTUWaterHeating.h:VARIABLE(start = 1e6 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 0.003377/2.227, allocations: 10 MB / 0.753 GB, free: 191.9 MB / 0.5919 GB
Error: post-optimization module createDAEmodeBDAE (simulation) failed.
Error: Internal error SimCode DAEmode: The model ThermoSysPro.Examples.SimpleExamples.TestNTUWaterHeating1 could not be translated