Running: ./testmodel.py --libraries=/home/hudson/saved_omc/libraries/.openmodelica/libraries --ompython_omhome=/usr ThermoSysPro_ThermoSysPro.Examples.SimpleExamples.TestStaticCondenser.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.TestStaticCondenser,tolerance=1e-06,outputFormat="empty",numberOfIntervals=5000,variableFilter="",fileNamePrefix="ThermoSysPro_ThermoSysPro.Examples.SimpleExamples.TestStaticCondenser")
translateModel(ThermoSysPro.Examples.SimpleExamples.TestStaticCondenser,tolerance=1e-06,outputFormat="empty",numberOfIntervals=5000,variableFilter="",fileNamePrefix="ThermoSysPro_ThermoSysPro.Examples.SimpleExamples.TestStaticCondenser")
Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermoSysPro 4.0.0-master/package.mo): time 0.8378/0.8378, allocations: 150.9 MB / 167.2 MB, free: 14.53 MB / 142.1 MB
Notification: Performance of FrontEnd - loaded program: time 0.00034/0.00034, allocations: 16.41 kB / 237.8 MB, free: 1.754 MB / 190.1 MB
Notification: Performance of FrontEnd - Absyn->SCode: time 0.05527/0.05562, allocations: 31.35 MB / 269.1 MB, free: 7.043 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.TestStaticCondenser): time 1.671/1.726, allocations: 298.8 MB / 0.5547 GB, free: 8.91 MB / 446.1 MB
Notification: Performance of NFInst.instExpressions: time 0.0409/1.767, allocations: 37.06 MB / 0.5909 GB, free: 3.703 MB / 478.1 MB
Notification: Performance of NFInst.updateImplicitVariability: time 0.0005591/1.768, allocations: 8 kB / 0.5909 GB, free: 3.695 MB / 478.1 MB
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermoSysPro 4.0.0-master/WaterSteam/BoundaryConditions/SourceQ.mo:24:3-25:52: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/SinkP.mo:33:3-34:47: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/StaticCondenser.mo:78:3-80:24:writable] Warning: Connector Cee 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/StaticCondenser.mo:81:3-83:17:writable] Warning: Connector Cse 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/StaticCondenser.mo:84:3-86:16:writable] Warning: Connector Cex 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/StaticCondenser.mo:87:3-88:83:writable] Warning: Connector Cvt 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/StaticCondenser.mo:108:3-109:83:writable] Warning: Connector Cep 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/StaticCondenser.mo:111:3-113:17:writable] Warning: Connector Cev 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/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).
Notification: Performance of NFTyping.typeComponents: time 0.0007002/1.768, allocations: 297.1 kB / 0.5911 GB, free: 3.406 MB / 478.1 MB
Notification: Performance of NFTyping.typeBindings: time 0.0008383/1.769, allocations: 483.9 kB / 0.5916 GB, free: 2.93 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 0.02411/1.793, allocations: 10.24 MB / 0.6016 GB, free: 8.668 MB / 494.1 MB
Notification: Performance of NFFlatten.flatten: time 0.002065/1.796, allocations: 1.665 MB / 0.6032 GB, free: 6.996 MB / 494.1 MB
Notification: Performance of NFFlatten.resolveConnections: time 0.0006666/1.796, allocations: 0.6049 MB / 0.6038 GB, free: 6.371 MB / 494.1 MB
Notification: Performance of NFEvalConstants.evaluate: time 0.0007477/1.797, allocations: 0.6304 MB / 0.6044 GB, free: 5.738 MB / 494.1 MB
Notification: Performance of NFSimplifyModel.simplify: time 0.000573/1.798, allocations: 0.5714 MB / 0.605 GB, free: 5.164 MB / 494.1 MB
Notification: Performance of NFPackage.collectConstants: time 0.0001246/1.798, allocations: 96 kB / 0.6051 GB, free: 5.07 MB / 494.1 MB
Notification: Performance of NFFlatten.collectFunctions: time 0.03075/1.828, allocations: 18.88 MB / 0.6235 GB, free: 2.172 MB / 0.4981 GB
Notification: Performance of NFScalarize.scalarize: time 0.0002961/1.829, allocations: 231 kB / 0.6237 GB, free: 1.945 MB / 0.4981 GB
Notification: Performance of NFVerifyModel.verify: time 0.000828/1.83, allocations: 0.6607 MB / 0.6244 GB, free: 1.281 MB / 0.4981 GB
Notification: Performance of NFConvertDAE.convert: time 0.02034/1.85, allocations: 9.874 MB / 0.634 GB, free: 7.383 MB / 0.5137 GB
Notification: Performance of FrontEnd - DAE generated: time 5.4e-06/1.85, allocations: 0 / 0.634 GB, free: 7.383 MB / 0.5137 GB
Notification: Performance of FrontEnd: time 1.954e-06/1.85, allocations: 4 kB / 0.634 GB, free: 7.379 MB / 0.5137 GB
Notification: Performance of Transformations before backend: time 6.065e-05/1.85, allocations: 0 / 0.634 GB, free: 7.379 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: 389
 * Number of variables: 389
Notification: Performance of Generate backend data structure: time 0.005849/1.856, allocations: 2.399 MB / 0.6364 GB, free: 4.922 MB / 0.5137 GB
Notification: Performance of prepare preOptimizeDAE: time 4.28e-05/1.856, allocations: 8.031 kB / 0.6364 GB, free: 4.914 MB / 0.5137 GB
Notification: Performance of preOpt normalInlineFunction (simulation): time 0.0002565/1.856, allocations: 150.1 kB / 0.6365 GB, free: 4.766 MB / 0.5137 GB
Notification: Performance of preOpt evaluateParameters (simulation): time 0.0006338/1.857, allocations: 499.6 kB / 0.637 GB, free: 4.234 MB / 0.5137 GB
Notification: Performance of preOpt simplifyIfEquations (simulation): time 6.791e-05/1.857, allocations: 82.05 kB / 0.6371 GB, free: 4.152 MB / 0.5137 GB
Notification: Performance of preOpt expandDerOperator (simulation): time 0.0001072/1.857, allocations: 96 kB / 0.6372 GB, free: 4.059 MB / 0.5137 GB
Notification: Performance of preOpt clockPartitioning (simulation): time 0.001879/1.859, allocations: 1.36 MB / 0.6385 GB, free: 2.586 MB / 0.5137 GB
Notification: Performance of preOpt findStateOrder (simulation): time 2.64e-05/1.859, allocations: 3.938 kB / 0.6385 GB, free: 2.582 MB / 0.5137 GB
Notification: Performance of preOpt replaceEdgeChange (simulation): time 8.932e-05/1.859, allocations: 47.98 kB / 0.6386 GB, free: 2.535 MB / 0.5137 GB
Notification: Performance of preOpt inlineArrayEqn (simulation): time 5.288e-05/1.859, allocations: 63.95 kB / 0.6386 GB, free: 2.473 MB / 0.5137 GB
Notification: Performance of preOpt removeEqualRHS (simulation): time 0.001344/1.86, allocations: 0.8671 MB / 0.6395 GB, free: 1.602 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 0.02434/1.885, allocations: 15.28 MB / 0.6544 GB, free: 0.8477 MB / 0.5294 GB
Notification: Performance of preOpt comSubExp (simulation): time 0.001213/1.886, allocations: 0.6402 MB / 0.655 GB, free: 208 kB / 0.5294 GB
Notification: Performance of preOpt resolveLoops (simulation): time 0.0006632/1.887, allocations: 449.2 kB / 0.6554 GB, free: 15.76 MB / 0.545 GB
Notification: Performance of preOpt evalFunc (simulation): time 0.3468/2.234, allocations: 81.11 MB / 0.7346 GB, free: 198.6 MB / 0.5919 GB
Notification: Performance of preOpt encapsulateWhenConditions (simulation): time 3.21e-05/2.234, allocations: 41.72 kB / 0.7347 GB, free: 198.6 MB / 0.5919 GB
Notification: Performance of pre-optimization done (n=181): time 5.41e-06/2.234, allocations: 0 / 0.7347 GB, free: 198.6 MB / 0.5919 GB
Notification: Performance of matching and sorting (n=181): time 0.01231/2.246, allocations: 3.475 MB / 0.7381 GB, free: 198 MB / 0.5919 GB
Notification: Performance of inlineWhenForInitialization (initialization): time 2.218e-05/2.246, allocations: 58.61 kB / 0.7381 GB, free: 198 MB / 0.5919 GB
Notification: Performance of selectInitializationVariablesDAE (initialization): time 0.0006309/2.247, allocations: 0.5965 MB / 0.7387 GB, free: 197.8 MB / 0.5919 GB
Notification: Performance of collectPreVariables (initialization): time 3.568e-05/2.247, allocations: 34.8 kB / 0.7387 GB, free: 197.8 MB / 0.5919 GB
Notification: Performance of collectInitialEqns (initialization): time 0.0001957/2.247, allocations: 403.5 kB / 0.7391 GB, free: 197.7 MB / 0.5919 GB
Notification: Performance of collectInitialBindings (initialization): time 0.0002779/2.247, allocations: 0.5751 MB / 0.7397 GB, free: 197.3 MB / 0.5919 GB
Notification: Performance of simplifyInitialFunctions (initialization): time 0.0002629/2.247, allocations: 228.7 kB / 0.7399 GB, free: 197.2 MB / 0.5919 GB
Notification: Performance of setup shared object (initialization): time 6.926e-05/2.248, allocations: 347.9 kB / 0.7402 GB, free: 196.9 MB / 0.5919 GB
Notification: Performance of preBalanceInitialSystem (initialization): time 0.0004852/2.248, allocations: 339.7 kB / 0.7406 GB, free: 196.9 MB / 0.5919 GB
Notification: Performance of partitionIndependentBlocks (initialization): time 0.0005831/2.249, allocations: 0.5645 MB / 0.7411 GB, free: 196.7 MB / 0.5919 GB
Notification: Performance of analyzeInitialSystem (initialization): time 0.001238/2.25, allocations: 1.015 MB / 0.7421 GB, free: 196.5 MB / 0.5919 GB
Notification: Performance of solveInitialSystemEqSystem (initialization): time 5.55e-06/2.25, allocations: 2.094 kB / 0.7421 GB, free: 196.5 MB / 0.5919 GB
Notification: Performance of matching and sorting (n=225) (initialization): time 0.00244/2.252, allocations: 1.575 MB / 0.7436 GB, free: 196.2 MB / 0.5919 GB
Notification: Performance of prepare postOptimizeDAE: time 2.09e-05/2.252, allocations: 10.55 kB / 0.7437 GB, free: 196.2 MB / 0.5919 GB
Notification: Performance of postOpt simplifyComplexFunction (initialization): time 2.153e-05/2.252, allocations: 6 kB / 0.7437 GB, free: 196.2 MB / 0.5919 GB
Notification: Performance of postOpt tearingSystem (initialization): time 0.003182/2.256, allocations: 1.513 MB / 0.7451 GB, free: 196.2 MB / 0.5919 GB
Notification: Performance of postOpt solveSimpleEquations (initialization): time 0.0002167/2.256, allocations: 63.55 kB / 0.7452 GB, free: 196.2 MB / 0.5919 GB
Notification: Performance of postOpt calculateStrongComponentJacobians (initialization): time 0.003601/2.259, allocations: 5.666 MB / 0.7507 GB, free: 191.6 MB / 0.5919 GB
Notification: Performance of postOpt simplifyAllExpressions (initialization): time 0.0005548/2.26, allocations: 137 kB / 0.7509 GB, free: 191.5 MB / 0.5919 GB
Notification: Performance of postOpt collapseArrayExpressions (initialization): time 5.533e-05/2.26, allocations: 39.09 kB / 0.7509 GB, free: 191.5 MB / 0.5919 GB
Notification: Model statistics after passing the back-end for initialization:
 * Number of independent subsystems: 25
 * Number of states: 0 ()
 * Number of discrete variables: 24 (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,singularPressureLoss1.C2.b,singularPressureLoss1.C1.a,singularPressureLoss.C2.b,singularPressureLoss.C1.a,sourceP2.C.b,sourceP1.C.b,sourceP.C.b,condenseur.Cev.a,condenseur.Cep.a,condenseur.Cvt.a,condenseur.Cex.b,condenseur.Cse.b,condenseur.Cee.a,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 (59):
 * Single equations (assignments): 47
 * Array equations: 0
 * Algorithm blocks: 0
 * Record equations: 4
 * When equations: 0
 * If-equations: 0
 * Equation systems (not torn): 0
 * Torn equation systems: 8
 * Mixed (continuous/discrete) equation systems: 0
Notification: Torn system details for strict tearing set:
 * Linear torn systems (#iteration vars, #inner vars, density): 1 system
   {(1,3,100.0%)}
 * Non-linear torn systems (#iteration vars, #inner vars): 7 systems
   {(1,3), (1,3), (1,3), (1,3), (1,3), (10,2), (5,12)}
Notification: Performance of prepare postOptimizeDAE: time 0.0003381/2.26, allocations: 254.1 kB / 0.7511 GB, free: 191.4 MB / 0.5919 GB
Notification: Performance of postOpt lateInlineFunction (simulation): time 0.0001145/2.261, allocations: 101.8 kB / 0.7512 GB, free: 191.4 MB / 0.5919 GB
Notification: Performance of postOpt wrapFunctionCalls (simulation): time 0.00311/2.264, allocations: 3.379 MB / 0.7545 GB, free: 190.8 MB / 0.5919 GB
Notification: Performance of postOpt simplifysemiLinear (simulation): time 9.097e-06/2.264, allocations: 8.547 kB / 0.7545 GB, free: 190.8 MB / 0.5919 GB
Notification: Performance of postOpt simplifyComplexFunction (simulation): time 9.097e-06/2.264, allocations: 3.938 kB / 0.7546 GB, free: 190.8 MB / 0.5919 GB
Notification: Performance of postOpt removeConstants (simulation): time 0.0003004/2.264, allocations: 311.2 kB / 0.7548 GB, free: 190.6 MB / 0.5919 GB
Notification: Performance of postOpt simplifyTimeIndepFuncCalls (simulation): time 8.077e-05/2.264, allocations: 23.25 kB / 0.7549 GB, free: 190.6 MB / 0.5919 GB
Notification: Performance of postOpt simplifyAllExpressions (simulation): time 0.0003171/2.264, allocations: 11.69 kB / 0.7549 GB, free: 190.6 MB / 0.5919 GB
Notification: Performance of postOpt findZeroCrossings (simulation): time 0.0001051/2.264, allocations: 45.53 kB / 0.7549 GB, free: 190.6 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(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) = $cse5

Variables:
1: singularPressureLoss3.pro.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific entropy" type: Real
2: singularPressureLoss3.pro.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific heat capacity at constant presure" type: Real
3: singularPressureLoss3.pro.ddhp:VARIABLE(unit = "kg.s2/m5" )  "Derivative of density wrt. specific enthalpy at constant pressure" type: Real
4: $cse5.d:VARIABLE(protected = true )  type: Real unreplaceable
5: $cse5.x:VARIABLE(protected = true )  type: Real unreplaceable
6: $cse5.duhp:VARIABLE(protected = true )  type: Real unreplaceable
7: $cse5.duph:VARIABLE(protected = true )  type: Real unreplaceable
8: $cse5.ddhp:VARIABLE(protected = true )  type: Real unreplaceable
9: $cse5.s:VARIABLE(protected = true )  type: Real unreplaceable
10: $cse5.u: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 (10): $cse3 = ThermoSysPro.Properties.Fluid.Ph(singularPressureLoss4.Pm, singularPressureLoss4.h, singularPressureLoss4.mode, singularPressureLoss4.fluid)
2/11 (10): ThermoSysPro.Properties.WaterSteam.Common.ThermoProperties_ph(singularPressureLoss4.T, singularPressureLoss4.rho, singularPressureLoss4.pro.u, singularPressureLoss4.pro.s, singularPressureLoss4.pro.cp, singularPressureLoss4.pro.ddhp, singularPressureLoss4.pro.ddph, singularPressureLoss4.pro.duph, singularPressureLoss4.pro.duhp, singularPressureLoss4.pro.x) = $cse3
3/21 (10): $cse16 = ThermoSysPro.Properties.WaterSteam.IF97.Water_Ph(condenseur.Pse, singularPressureLoss4.h, condenseur.mode_se)
4/31 (1): $cse19 = exp(condenseur.XKCO * condenseur.SCO * (condenseur.Tee - condenseur.Tse) / condenseur.W)
5/32 (1): condenseur.XKCO = condenseur.KCO * condenseur.COP * condenseur.KT2 * $cse20 / (condenseur.COPR * condenseur.KT1)
6/33 (1): condenseur.KT2 = 52.0 + 3.3 * (-273.16 + condenseur.Tee) + (-0.05) * (-273.16 + condenseur.Tee) ^ 2.0
7/34 (1): 0.0 = condenseur.Tsat + (condenseur.Tee - condenseur.Tsat) * $cse19 - condenseur.Tse
8/35 (10): $cse18 = ThermoSysPro.Properties.WaterSteam.IF97.Water_Ph(condenseur.Pee, singularPressureLoss2.h, condenseur.mode_ee)
9/45 (1): condenseur.Pse = if noEvent(condenseur.rho_ee > 0.0) then condenseur.Pee - condenseur.CPCE * ThermoSysPro.Functions.ThermoSquare(Source_condenseur.Q0, condenseur.eps) / condenseur.rho_ee else condenseur.Pee
10/46 (1): condenseur.Pse - Puit_condenseur.P0 = singularPressureLoss4.deltaP
11/47 (1): singularPressureLoss4.deltaP = singularPressureLoss4.K * $cse4 / singularPressureLoss4.rho
12/48 (1): singularPressureLoss4.Pm = 0.5 * (condenseur.Pse + Puit_condenseur.P0)
13/49 (10): ThermoSysPro.Properties.WaterSteam.Common.ThermoProperties_ph(condenseur.Tee, condenseur.rho_ee, condenseur.proee.u, condenseur.proee.s, condenseur.proee.cp, condenseur.proee.ddhp, condenseur.proee.ddph, condenseur.proee.duph, condenseur.proee.duhp, condenseur.proee.x) = $cse18
14/59 (10): ThermoSysPro.Properties.WaterSteam.Common.ThermoProperties_ph(condenseur.Tse, condenseur.prose.d, condenseur.prose.u, condenseur.prose.s, condenseur.prose.cp, condenseur.prose.ddhp, condenseur.prose.ddph, condenseur.prose.duph, condenseur.prose.duhp, condenseur.prose.x) = $cse16
15/69 (1): 0.0 = if Source_condenseur.Q0 > 0.0 then singularPressureLoss2.h - singularPressureLoss2.C2.h_vol else singularPressureLoss4.h - condenseur.Cse.h_vol
16/70 (1): 0.0 = if Source_condenseur.Q0 > 0.0 then singularPressureLoss2.h - Source_condenseur.h0 else singularPressureLoss2.h - singularPressureLoss2.C2.h_vol
17/71 (1): condenseur.W = Source_condenseur.Q0 * (singularPressureLoss4.h - singularPressureLoss2.h)
18/72 (1): condenseur.W = singularPressureLoss3.Q * (singularPressureLoss3.h - condenseur.Hsate) + singularPressureLoss1.Q * (singularPressureLoss1.h - condenseur.Hsate) + singularPressureLoss.Q * (singularPressureLoss.h - condenseur.Hsate)
19/73 (14): (ThermoSysPro.Properties.WaterSteam.Common.PropThermoSat(condenseur.lsat1.P, condenseur.lsat1.T, condenseur.lsat1.rho, condenseur.Hsate, condenseur.lsat1.cp, condenseur.lsat1.pt, condenseur.lsat1.cv), condenseur.vsat1) = ThermoSysPro.Properties.WaterSteam.IF97.Water_sat_P(condenseur.Pcond)
20/87 (1): condenseur.Pcond = ThermoSysPro.Properties.WaterSteam.BaseIF97.Basic.psat(condenseur.Tsat)
21/88 (1): sourceP1.P0 - condenseur.Pcond = singularPressureLoss.deltaP
22/89 (1): singularPressureLoss.deltaP = singularPressureLoss.K * $cse12 / singularPressureLoss.rho
23/90 (1): $cse12 = ThermoSysPro.Functions.ThermoSquare(singularPressureLoss.Q, singularPressureLoss.eps)
24/91 (1): singularPressureLoss5.Q = singularPressureLoss3.Q + singularPressureLoss1.Q + singularPressureLoss.Q
25/92 (1): condenseur.Hmv = (singularPressureLoss3.h * singularPressureLoss3.Q + singularPressureLoss.h * singularPressureLoss.Q + singularPressureLoss1.h * singularPressureLoss1.Q) / singularPressureLoss5.Q
26/93 (10): $cse11 = ThermoSysPro.Properties.Fluid.Ph(singularPressureLoss.Pm, singularPressureLoss.h, singularPressureLoss.mode, singularPressureLoss.fluid)
27/103 (10): ThermoSysPro.Properties.WaterSteam.Common.ThermoProperties_ph(singularPressureLoss.T, singularPressureLoss.rho, singularPressureLoss.pro.u, singularPressureLoss.pro.s, singularPressureLoss.pro.cp, singularPressureLoss.pro.ddhp, singularPressureLoss.pro.ddph, singularPressureLoss.pro.duph, singularPressureLoss.pro.duhp, singularPressureLoss.pro.x) = $cse11
28/113 (1): 0.0 = if singularPressureLoss.Q > 0.0 then singularPressureLoss.h - sourceP1.h0 else singularPressureLoss.h - condenseur.Hmv
29/114 (1): 0.0 = if singularPressureLoss1.Q > 0.0 then singularPressureLoss1.h - sourceP2.h0 else singularPressureLoss1.h - condenseur.Hmv
30/115 (10): $cse9 = ThermoSysPro.Properties.Fluid.Ph(singularPressureLoss1.Pm, singularPressureLoss1.h, singularPressureLoss1.mode, singularPressureLoss1.fluid)
31/125 (1): singularPressureLoss1.deltaP = singularPressureLoss1.K * $cse10 / singularPressureLoss1.rho
32/126 (1): $cse10 = ThermoSysPro.Functions.ThermoSquare(singularPressureLoss1.Q, singularPressureLoss1.eps)
33/127 (10): ThermoSysPro.Properties.WaterSteam.Common.ThermoProperties_ph(singularPressureLoss1.T, singularPressureLoss1.rho, singularPressureLoss1.pro.u, singularPressureLoss1.pro.s, singularPressureLoss1.pro.cp, singularPressureLoss1.pro.ddhp, singularPressureLoss1.pro.ddph, singularPressureLoss1.pro.duph, singularPressureLoss1.pro.duhp, singularPressureLoss1.pro.x) = $cse9
34/137 (1): 0.0 = if singularPressureLoss3.Q > 0.0 then singularPressureLoss3.h - sourceP.h0 else singularPressureLoss3.h - condenseur.Hmv
35/138 (10): $cse5 = ThermoSysPro.Properties.Fluid.Ph(singularPressureLoss3.Pm, singularPressureLoss3.h, singularPressureLoss3.mode, singularPressureLoss3.fluid)
36/148 (1): singularPressureLoss3.deltaP = singularPressureLoss3.K * $cse6 / singularPressureLoss3.rho
37/149 (1): $cse6 = ThermoSysPro.Functions.ThermoSquare(singularPressureLoss3.Q, singularPressureLoss3.eps)
38/150 (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) = $cse5
39/160 (1): singularPressureLoss.Pm = 0.5 * (sourceP1.P0 + condenseur.Pcond)
40/161 (1): sourceP2.P0 - condenseur.Pcond = singularPressureLoss1.deltaP
41/162 (1): singularPressureLoss1.Pm = 0.5 * (sourceP2.P0 + condenseur.Pcond)
42/163 (1): sourceP.P0 - condenseur.Pcond = singularPressureLoss3.deltaP
43/164 (1): singularPressureLoss3.Pm = 0.5 * (sourceP.P0 + condenseur.Pcond)
44/165 (1): 0.0 = if Source_condenseur.Q0 > 0.0 then singularPressureLoss4.h - condenseur.Cse.h_vol else singularPressureLoss4.h - Puit_condenseur.h

Variables:
1: condenseur.Cse.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" )  "Fluid specific enthalpy in the control volume" type: Real
2: singularPressureLoss3.Pm:VARIABLE(min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 )  "Average fluid pressure" type: Real
3: singularPressureLoss3.deltaP:VARIABLE(unit = "Pa" )  "Singular pressure loss" type: Real
4: singularPressureLoss1.Pm:VARIABLE(min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 )  "Average fluid pressure" type: Real
5: singularPressureLoss1.deltaP:VARIABLE(unit = "Pa" )  "Singular pressure loss" type: Real
6: singularPressureLoss.Pm:VARIABLE(min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 )  "Average fluid pressure" type: Real
7: singularPressureLoss3.T:VARIABLE(min = 200.0 max = 6000.0 start = 290.0 unit = "K" nominal = 300.0 )  "Fluid temperature" type: Real
8: singularPressureLoss3.pro.ddph:VARIABLE(unit = "s2/m2" )  "Derivative of density wrt. pressure at constant specific enthalpy" type: Real
9: singularPressureLoss3.pro.x:VARIABLE(min = 0.0 max = 1.0 unit = "1" )  "Vapor mass fraction" type: Real
10: singularPressureLoss3.Q:VARIABLE(start = 100.0 unit = "kg/s" fixed = true )  "Mass flow rate" type: Real
11: $cse6:VARIABLE(protected = true )  type: Real unreplaceable
12: singularPressureLoss3.rho:VARIABLE(min = 1e-9 max = 1e5 start = 998.0 unit = "kg/m3" nominal = 998.0 )  "Fluid density" type: Real
13: singularPressureLoss3.pro.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 )  "Specific inner energy" type: Real
14: singularPressureLoss3.pro.duph:VARIABLE(unit = "m3/kg" )  "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real
15: singularPressureLoss3.pro.duhp:VARIABLE(unit = "1" )  "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real
16: singularPressureLoss3.pro.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific entropy" type: Real
17: singularPressureLoss3.pro.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific heat capacity at constant presure" type: Real
18: singularPressureLoss3.pro.ddhp:VARIABLE(unit = "kg.s2/m5" )  "Derivative of density wrt. specific enthalpy at constant pressure" type: Real
19: $cse5.d:VARIABLE(protected = true )  type: Real unreplaceable
20: $cse5.x:VARIABLE(protected = true )  type: Real unreplaceable
21: $cse5.duhp:VARIABLE(protected = true )  type: Real unreplaceable
22: $cse5.duph:VARIABLE(protected = true )  type: Real unreplaceable
23: $cse5.ddhp:VARIABLE(protected = true )  type: Real unreplaceable
24: $cse5.s:VARIABLE(protected = true )  type: Real unreplaceable
25: $cse5.u:VARIABLE(protected = true )  type: Real unreplaceable
26: $cse5.ddph:VARIABLE(protected = true )  type: Real unreplaceable
27: $cse5.cp:VARIABLE(protected = true )  type: Real unreplaceable
28: $cse5.T:VARIABLE(protected = true )  type: Real unreplaceable
29: singularPressureLoss3.h:VARIABLE(start = 1e5 unit = "J/kg" )  "Fluid specific enthalpy" type: Real
30: singularPressureLoss1.pro.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific heat capacity at constant presure" type: Real
31: singularPressureLoss1.pro.ddhp:VARIABLE(unit = "kg.s2/m5" )  "Derivative of density wrt. specific enthalpy at constant pressure" type: Real
32: singularPressureLoss1.pro.duph:VARIABLE(unit = "m3/kg" )  "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real
33: singularPressureLoss1.pro.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 )  "Specific inner energy" type: Real
34: singularPressureLoss1.pro.x:VARIABLE(min = 0.0 max = 1.0 unit = "1" )  "Vapor mass fraction" type: Real
35: singularPressureLoss1.pro.duhp:VARIABLE(unit = "1" )  "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real
36: singularPressureLoss1.Q:VARIABLE(start = 1e-5 unit = "kg/s" fixed = true )  "Mass flow rate" type: Real
37: $cse10:VARIABLE(protected = true )  type: Real unreplaceable
38: singularPressureLoss1.rho:VARIABLE(min = 1e-9 max = 1e5 start = 998.0 unit = "kg/m3" nominal = 998.0 )  "Fluid density" type: Real
39: singularPressureLoss1.T:VARIABLE(min = 200.0 max = 6000.0 start = 290.0 unit = "K" nominal = 300.0 )  "Fluid temperature" type: Real
40: singularPressureLoss1.pro.ddph:VARIABLE(unit = "s2/m2" )  "Derivative of density wrt. pressure at constant specific enthalpy" type: Real
41: singularPressureLoss1.pro.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific entropy" type: Real
42: $cse9.duph:VARIABLE(protected = true )  type: Real unreplaceable
43: $cse9.d:VARIABLE(protected = true )  type: Real unreplaceable
44: $cse9.s:VARIABLE(protected = true )  type: Real unreplaceable
45: $cse9.ddph:VARIABLE(protected = true )  type: Real unreplaceable
46: $cse9.duhp:VARIABLE(protected = true )  type: Real unreplaceable
47: $cse9.x:VARIABLE(protected = true )  type: Real unreplaceable
48: $cse9.cp:VARIABLE(protected = true )  type: Real unreplaceable
49: $cse9.u:VARIABLE(protected = true )  type: Real unreplaceable
50: $cse9.ddhp:VARIABLE(protected = true )  type: Real unreplaceable
51: $cse9.T:VARIABLE(protected = true )  type: Real unreplaceable
52: singularPressureLoss1.h:VARIABLE(start = 1e5 unit = "J/kg" )  "Fluid specific enthalpy" type: Real
53: condenseur.Hmv:VARIABLE(start = 2.5e6 unit = "J/kg" )  "Fluid input average specific enthalpy" type: Real
54: singularPressureLoss.pro.duph:VARIABLE(unit = "m3/kg" )  "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real
55: singularPressureLoss.pro.duhp:VARIABLE(unit = "1" )  "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real
56: singularPressureLoss.pro.x:VARIABLE(min = 0.0 max = 1.0 unit = "1" )  "Vapor mass fraction" type: Real
57: singularPressureLoss.pro.ddph:VARIABLE(unit = "s2/m2" )  "Derivative of density wrt. pressure at constant specific enthalpy" type: Real
58: singularPressureLoss.pro.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 )  "Specific inner energy" type: Real
59: singularPressureLoss.pro.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific heat capacity at constant presure" type: Real
60: singularPressureLoss.pro.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific entropy" type: Real
61: singularPressureLoss.pro.ddhp:VARIABLE(unit = "kg.s2/m5" )  "Derivative of density wrt. specific enthalpy at constant pressure" type: Real
62: singularPressureLoss.T:VARIABLE(min = 200.0 max = 6000.0 start = 290.0 unit = "K" nominal = 300.0 )  "Fluid temperature" type: Real
63: singularPressureLoss.rho:VARIABLE(min = 1e-9 max = 1e5 start = 998.0 unit = "kg/m3" nominal = 998.0 )  "Fluid density" type: Real
64: $cse11.d:VARIABLE(protected = true )  type: Real unreplaceable
65: $cse11.cp:VARIABLE(protected = true )  type: Real unreplaceable
66: $cse11.duhp:VARIABLE(protected = true )  type: Real unreplaceable
67: $cse11.ddhp:VARIABLE(protected = true )  type: Real unreplaceable
68: $cse11.T:VARIABLE(protected = true )  type: Real unreplaceable
69: $cse11.ddph:VARIABLE(protected = true )  type: Real unreplaceable
70: $cse11.x:VARIABLE(protected = true )  type: Real unreplaceable
71: $cse11.duph:VARIABLE(protected = true )  type: Real unreplaceable
72: $cse11.u:VARIABLE(protected = true )  type: Real unreplaceable
73: $cse11.s:VARIABLE(protected = true )  type: Real unreplaceable
74: singularPressureLoss.h:VARIABLE(start = 1e5 unit = "J/kg" )  "Fluid specific enthalpy" type: Real
75: singularPressureLoss5.Q:VARIABLE(start = 100.0 unit = "kg/s" )  "Mass flow rate" type: Real
76: singularPressureLoss.Q:VARIABLE(start = 1e-5 unit = "kg/s" fixed = true )  "Mass flow rate" type: Real
77: $cse12:VARIABLE(protected = true )  type: Real unreplaceable
78: singularPressureLoss.deltaP:VARIABLE(unit = "Pa" )  "Singular pressure loss" type: Real
79: condenseur.Tsat:VARIABLE(min = 0.0 start = 500.0 unit = "K" nominal = 300.0 )  "Water temperature at the saturation point" type: Real
80: condenseur.lsat1.pt:VARIABLE()  "Derivative of pressure wrt. temperature" type: Real
81: condenseur.vsat1.cp:VARIABLE(unit = "J/(kg.K)" )  "Specific heat capacity at constant pressure" type: Real
82: condenseur.vsat1.pt:VARIABLE()  "Derivative of pressure wrt. temperature" type: Real
83: condenseur.Pcond:VARIABLE(min = 0.0 start = 2154.77 unit = "Pa" fixed = false nominal = 1e5 )  "Vapor pressure inside the condenser" type: Real
84: condenseur.vsat1.P:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 )  "Pressure" type: Real
85: condenseur.lsat1.cp:VARIABLE(unit = "J/(kg.K)" )  "Specific heat capacity at constant pressure" type: Real
86: condenseur.vsat1.cv:VARIABLE(unit = "J/(kg.K)" )  "Specific heat capacity at constant volume" type: Real
87: condenseur.vsat1.T:VARIABLE(min = 0.0 start = 288.15 unit = "K" nominal = 300.0 )  "Temperature" type: Real
88: condenseur.lsat1.P:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 )  "Pressure" type: Real
89: condenseur.lsat1.rho:VARIABLE(min = 0.0 unit = "kg/m3" )  "Density" type: Real
90: condenseur.lsat1.cv:VARIABLE(unit = "J/(kg.K)" )  "Specific heat capacity at constant volume" type: Real
91: condenseur.lsat1.T:VARIABLE(min = 0.0 start = 288.15 unit = "K" nominal = 300.0 )  "Temperature" type: Real
92: condenseur.vsat1.rho:VARIABLE(min = 0.0 unit = "kg/m3" )  "Density" type: Real
93: condenseur.vsat1.h:VARIABLE(unit = "J/kg" )  "Specific enthalpy" type: Real
94: condenseur.Hsate:VARIABLE(start = 2e5 unit = "J/kg" )  "Water specific enthalpy at the saturation point" type: Real
95: condenseur.W:VARIABLE(unit = "W" )  "Heat power released to the cold source" type: Real
96: singularPressureLoss2.h:VARIABLE(start = 1e5 unit = "J/kg" )  "Fluid specific enthalpy" type: Real
97: singularPressureLoss2.C2.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" )  "Fluid specific enthalpy in the control volume" type: Real
98: condenseur.prose.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific heat capacity at constant presure" type: Real
99: condenseur.proee.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific entropy" type: Real
100: condenseur.proee.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific heat capacity at constant presure" type: Real
101: condenseur.rho_ee:VARIABLE(min = 1e-9 max = 1e5 start = 900.0 unit = "kg/m3" nominal = 998.0 )  "Cooling water density at the inlet" type: Real
102: condenseur.proee.ddph:VARIABLE(unit = "s2/m2" )  "Derivative of density wrt. pressure at constant specific enthalpy" type: Real
103: condenseur.proee.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 )  "Specific inner energy" type: Real
104: condenseur.proee.ddhp:VARIABLE(unit = "kg.s2/m5" )  "Derivative of density wrt. specific enthalpy at constant pressure" type: Real
105: condenseur.proee.duhp:VARIABLE(unit = "1" )  "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real
106: condenseur.proee.duph:VARIABLE(unit = "m3/kg" )  "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real
107: singularPressureLoss4.Pm:VARIABLE(min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 )  "Average fluid pressure" type: Real
108: singularPressureLoss4.rho:VARIABLE(min = 1e-9 max = 1e5 start = 998.0 unit = "kg/m3" nominal = 998.0 )  "Fluid density" type: Real
109: singularPressureLoss4.deltaP:VARIABLE(unit = "Pa" )  "Singular pressure loss" type: Real
110: condenseur.Pse:VARIABLE(min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 )  "Cooling water pressure at the outlet" type: Real
111: condenseur.Pee:VARIABLE(min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 )  "Cooling water pressure at the inlet" type: Real
112: $cse18.s:VARIABLE(protected = true )  type: Real unreplaceable
113: $cse18.d:VARIABLE(protected = true )  type: Real unreplaceable
114: $cse18.u:VARIABLE(protected = true )  type: Real unreplaceable
115: $cse18.cp:VARIABLE(protected = true )  type: Real unreplaceable
116: $cse18.duph:VARIABLE(protected = true )  type: Real unreplaceable
117: $cse18.T:VARIABLE(protected = true )  type: Real unreplaceable
118: $cse18.ddph:VARIABLE(protected = true )  type: Real unreplaceable
119: $cse18.duhp:VARIABLE(protected = true )  type: Real unreplaceable
120: $cse18.ddhp:VARIABLE(protected = true )  type: Real unreplaceable
121: $cse18.x:VARIABLE(protected = true )  type: Real unreplaceable
122: condenseur.proee.x:VARIABLE(min = 0.0 max = 1.0 unit = "1" )  "Vapor mass fraction" type: Real
123: $cse19:VARIABLE(protected = true )  type: Real unreplaceable
124: condenseur.Tee:VARIABLE(min = 200.0 max = 6000.0 start = 300.0 unit = "K" nominal = 300.0 )  "Cooling water temperature at the inlet" type: Real
125: condenseur.KT2:VARIABLE(start = 50.0 unit = "W/(m2.K)" )  "Second reference value for the exchange coefficient" type: Real
126: condenseur.XKCO:VARIABLE(start = 200.0 unit = "W/(m2.K)" )  "Heat transfer coefficient" type: Real
127: condenseur.Tse:VARIABLE(min = 200.0 max = 6000.0 start = 400.0 unit = "K" nominal = 300.0 )  "Cooling water temperature at the outlet" type: Real
128: condenseur.prose.ddph:VARIABLE(unit = "s2/m2" )  "Derivative of density wrt. pressure at constant specific enthalpy" type: Real
129: condenseur.prose.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific entropy" type: Real
130: condenseur.prose.x:VARIABLE(min = 0.0 max = 1.0 unit = "1" )  "Vapor mass fraction" type: Real
131: condenseur.prose.duph:VARIABLE(unit = "m3/kg" )  "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real
132: condenseur.prose.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 )  "Specific inner energy" type: Real
133: condenseur.prose.duhp:VARIABLE(unit = "1" )  "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real
134: condenseur.prose.ddhp:VARIABLE(unit = "kg.s2/m5" )  "Derivative of density wrt. specific enthalpy at constant pressure" type: Real
135: condenseur.prose.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 )  "Density" type: Real
136: $cse16.u:VARIABLE(protected = true )  type: Real unreplaceable
137: $cse16.ddph:VARIABLE(protected = true )  type: Real unreplaceable
138: $cse16.duph:VARIABLE(protected = true )  type: Real unreplaceable
139: $cse16.duhp:VARIABLE(protected = true )  type: Real unreplaceable
140: $cse16.x:VARIABLE(protected = true )  type: Real unreplaceable
141: $cse16.ddhp:VARIABLE(protected = true )  type: Real unreplaceable
142: $cse16.d:VARIABLE(protected = true )  type: Real unreplaceable
143: $cse16.cp:VARIABLE(protected = true )  type: Real unreplaceable
144: $cse16.T:VARIABLE(protected = true )  type: Real unreplaceable
145: $cse16.s:VARIABLE(protected = true )  type: Real unreplaceable
146: singularPressureLoss4.pro.x:VARIABLE(min = 0.0 max = 1.0 unit = "1" )  "Vapor mass fraction" type: Real
147: singularPressureLoss4.pro.ddhp:VARIABLE(unit = "kg.s2/m5" )  "Derivative of density wrt. specific enthalpy at constant pressure" type: Real
148: singularPressureLoss4.pro.duph:VARIABLE(unit = "m3/kg" )  "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real
149: singularPressureLoss4.pro.duhp:VARIABLE(unit = "1" )  "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real
150: singularPressureLoss4.pro.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific heat capacity at constant presure" type: Real
151: singularPressureLoss4.pro.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 )  "Specific inner energy" type: Real
152: singularPressureLoss4.pro.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific entropy" type: Real
153: singularPressureLoss4.T:VARIABLE(min = 200.0 max = 6000.0 start = 290.0 unit = "K" nominal = 300.0 )  "Fluid temperature" type: Real
154: $cse3.s:VARIABLE(protected = true )  type: Real unreplaceable
155: $cse3.cp:VARIABLE(protected = true )  type: Real unreplaceable
156: $cse3.ddph:VARIABLE(protected = true )  type: Real unreplaceable
157: $cse3.T:VARIABLE(protected = true )  type: Real unreplaceable
158: $cse3.x:VARIABLE(protected = true )  type: Real unreplaceable
159: singularPressureLoss4.h:VARIABLE(start = 1e5 unit = "J/kg" )  "Fluid specific enthalpy" type: Real
160: $cse3.ddhp:VARIABLE(protected = true )  type: Real unreplaceable
161: $cse3.u:VARIABLE(protected = true )  type: Real unreplaceable
162: $cse3.duhp:VARIABLE(protected = true )  type: Real unreplaceable
163: $cse3.d:VARIABLE(protected = true )  type: Real unreplaceable
164: $cse3.duph:VARIABLE(protected = true )  type: Real unreplaceable
165: singularPressureLoss4.pro.ddph:VARIABLE(unit = "s2/m2" )  "Derivative of density wrt. pressure at constant 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 0.003027/2.268, allocations: 8.153 MB / 0.7629 GB, free: 181.8 MB / 0.5919 GB
Error: post-optimization module createDAEmodeBDAE (simulation) failed.
Error: Internal error SimCode DAEmode: The model ThermoSysPro.Examples.SimpleExamples.TestStaticCondenser could not be translated