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 0.8298/0.8298, allocations: 150.9 MB / 167.2 MB, free: 14.54 MB / 142.1 MB
Notification: Performance of FrontEnd - loaded program: time 0.0003901/0.0003901, allocations: 16.09 kB / 237.8 MB, free: 1.758 MB / 190.1 MB
Notification: Performance of FrontEnd - Absyn->SCode: time 0.0611/0.06151, allocations: 31.35 MB / 269.1 MB, free: 7.027 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 1.696/1.757, allocations: 299 MB / 0.5548 GB, free: 9.055 MB / 446.1 MB
Notification: Performance of NFInst.instExpressions: time 0.04052/1.798, allocations: 37.06 MB / 0.591 GB, free: 3.84 MB / 478.1 MB
Notification: Performance of NFInst.updateImplicitVariability: time 0.0008664/1.799, allocations: 8 kB / 0.591 GB, free: 3.832 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 0.0007907/1.8, allocations: 321.8 kB / 0.5913 GB, free: 3.52 MB / 478.1 MB
Notification: Performance of NFTyping.typeBindings: time 0.000955/1.801, allocations: 0.5507 MB / 0.5919 GB, free: 2.965 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 0.02449/1.825, allocations: 10.41 MB / 0.602 GB, free: 8.531 MB / 494.1 MB
Notification: Performance of NFFlatten.flatten: time 0.002168/1.827, allocations: 1.665 MB / 0.6037 GB, free: 6.859 MB / 494.1 MB
Notification: Performance of NFFlatten.resolveConnections: time 0.0006541/1.828, allocations: 0.6166 MB / 0.6043 GB, free: 6.223 MB / 494.1 MB
Notification: Performance of NFEvalConstants.evaluate: time 0.0006397/1.829, allocations: 0.6265 MB / 0.6049 GB, free: 5.594 MB / 494.1 MB
Notification: Performance of NFSimplifyModel.simplify: time 0.000539/1.829, allocations: 0.5753 MB / 0.6054 GB, free: 5.016 MB / 494.1 MB
Notification: Performance of NFPackage.collectConstants: time 0.0001151/1.829, allocations: 96 kB / 0.6055 GB, free: 4.922 MB / 494.1 MB
Notification: Performance of NFFlatten.collectFunctions: time 0.03195/1.861, allocations: 18.87 MB / 0.6239 GB, free: 2.031 MB / 0.4981 GB
Notification: Performance of NFScalarize.scalarize: time 0.0003085/1.861, allocations: 235 kB / 0.6242 GB, free: 1.801 MB / 0.4981 GB
Notification: Performance of NFVerifyModel.verify: time 0.0008109/1.862, allocations: 0.6646 MB / 0.6248 GB, free: 1.133 MB / 0.4981 GB
Notification: Performance of NFConvertDAE.convert: time 0.0204/1.883, allocations: 9.89 MB / 0.6345 GB, free: 7.215 MB / 0.5137 GB
Notification: Performance of FrontEnd - DAE generated: time 5.5e-06/1.883, allocations: 0 / 0.6345 GB, free: 7.215 MB / 0.5137 GB
Notification: Performance of FrontEnd: time 1.392e-06/1.883, allocations: 4 kB / 0.6345 GB, free: 7.211 MB / 0.5137 GB
Notification: Performance of Transformations before backend: time 5.819e-05/1.883, allocations: 0 / 0.6345 GB, free: 7.211 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 0.005386/1.888, allocations: 2.488 MB / 0.6369 GB, free: 4.656 MB / 0.5137 GB
Notification: Performance of prepare preOptimizeDAE: time 4.292e-05/1.888, allocations: 8.031 kB / 0.6369 GB, free: 4.648 MB / 0.5137 GB
Notification: Performance of preOpt normalInlineFunction (simulation): time 0.0002292/1.889, allocations: 151 kB / 0.6371 GB, free: 4.5 MB / 0.5137 GB
Notification: Performance of preOpt evaluateParameters (simulation): time 0.000626/1.889, allocations: 0.496 MB / 0.6375 GB, free: 3.961 MB / 0.5137 GB
Notification: Performance of preOpt simplifyIfEquations (simulation): time 6.439e-05/1.889, allocations: 74.05 kB / 0.6376 GB, free: 3.887 MB / 0.5137 GB
Notification: Performance of preOpt expandDerOperator (simulation): time 0.0001132/1.889, allocations: 103.9 kB / 0.6377 GB, free: 3.785 MB / 0.5137 GB
Notification: Performance of preOpt clockPartitioning (simulation): time 0.001823/1.891, allocations: 1.36 MB / 0.639 GB, free: 2.312 MB / 0.5137 GB
Notification: Performance of preOpt findStateOrder (simulation): time 2.693e-05/1.891, allocations: 3.938 kB / 0.6391 GB, free: 2.309 MB / 0.5137 GB
Notification: Performance of preOpt replaceEdgeChange (simulation): time 7.639e-05/1.891, allocations: 44 kB / 0.6391 GB, free: 2.266 MB / 0.5137 GB
Notification: Performance of preOpt inlineArrayEqn (simulation): time 6.294e-05/1.891, allocations: 59.95 kB / 0.6392 GB, free: 2.207 MB / 0.5137 GB
Notification: Performance of preOpt removeEqualRHS (simulation): time 0.001319/1.893, allocations: 0.871 MB / 0.64 GB, free: 1.332 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 0.02407/1.917, allocations: 15.3 MB / 0.6549 GB, free: 0.5586 MB / 0.5294 GB
Notification: Performance of preOpt comSubExp (simulation): time 0.001218/1.918, allocations: 0.6309 MB / 0.6556 GB, free: 15.92 MB / 0.545 GB
Notification: Performance of preOpt resolveLoops (simulation): time 0.0006583/1.919, allocations: 458.8 kB / 0.656 GB, free: 15.47 MB / 0.545 GB
Notification: Performance of preOpt evalFunc (simulation): time 0.3477/2.266, allocations: 81.11 MB / 0.7352 GB, free: 199 MB / 0.5919 GB
Notification: Performance of preOpt encapsulateWhenConditions (simulation): time 3.455e-05/2.266, allocations: 43.42 kB / 0.7352 GB, free: 199 MB / 0.5919 GB
Notification: Performance of pre-optimization done (n=181): time 3.176e-06/2.266, allocations: 0 / 0.7352 GB, free: 199 MB / 0.5919 GB
Notification: Performance of matching and sorting (n=181): time 0.01206/2.279, allocations: 3.478 MB / 0.7386 GB, free: 198.4 MB / 0.5919 GB
Notification: Performance of inlineWhenForInitialization (initialization): time 1.895e-05/2.279, allocations: 55.78 kB / 0.7387 GB, free: 198.4 MB / 0.5919 GB
Notification: Performance of selectInitializationVariablesDAE (initialization): time 0.0006203/2.279, allocations: 0.6002 MB / 0.7393 GB, free: 198.2 MB / 0.5919 GB
Notification: Performance of collectPreVariables (initialization): time 3.517e-05/2.279, allocations: 35.33 kB / 0.7393 GB, free: 198.2 MB / 0.5919 GB
Notification: Performance of collectInitialEqns (initialization): time 0.0001893/2.279, allocations: 410.8 kB / 0.7397 GB, free: 198 MB / 0.5919 GB
Notification: Performance of collectInitialBindings (initialization): time 0.0002872/2.28, allocations: 0.6104 MB / 0.7403 GB, free: 197.7 MB / 0.5919 GB
Notification: Performance of simplifyInitialFunctions (initialization): time 0.0002511/2.28, allocations: 235.3 kB / 0.7405 GB, free: 197.7 MB / 0.5919 GB
Notification: Performance of setup shared object (initialization): time 6.3e-05/2.28, allocations: 341.5 kB / 0.7409 GB, free: 197.4 MB / 0.5919 GB
Notification: Performance of preBalanceInitialSystem (initialization): time 0.0004814/2.281, allocations: 339.5 kB / 0.7412 GB, free: 197.4 MB / 0.5919 GB
Notification: Performance of partitionIndependentBlocks (initialization): time 0.0005957/2.281, allocations: 0.5615 MB / 0.7417 GB, free: 197.2 MB / 0.5919 GB
Notification: Performance of analyzeInitialSystem (initialization): time 0.001232/2.282, allocations: 1.019 MB / 0.7427 GB, free: 196.9 MB / 0.5919 GB
Notification: Performance of solveInitialSystemEqSystem (initialization): time 4.498e-06/2.282, allocations: 0 / 0.7427 GB, free: 196.9 MB / 0.5919 GB
Notification: Performance of matching and sorting (n=225) (initialization): time 0.002362/2.285, allocations: 1.586 MB / 0.7443 GB, free: 196.7 MB / 0.5919 GB
Notification: Performance of prepare postOptimizeDAE: time 1.876e-05/2.285, allocations: 10.34 kB / 0.7443 GB, free: 196.7 MB / 0.5919 GB
Notification: Performance of postOpt simplifyComplexFunction (initialization): time 2.189e-05/2.285, allocations: 4.312 kB / 0.7443 GB, free: 196.7 MB / 0.5919 GB
Notification: Performance of postOpt tearingSystem (initialization): time 0.003338/2.288, allocations: 1.505 MB / 0.7458 GB, free: 196.6 MB / 0.5919 GB
Notification: Performance of postOpt solveSimpleEquations (initialization): time 0.0002296/2.288, allocations: 66.98 kB / 0.7458 GB, free: 196.6 MB / 0.5919 GB
Notification: Performance of postOpt calculateStrongComponentJacobians (initialization): time 0.003728/2.292, allocations: 5.664 MB / 0.7513 GB, free: 192.1 MB / 0.5919 GB
Notification: Performance of postOpt simplifyAllExpressions (initialization): time 0.0004907/2.293, allocations: 140.5 kB / 0.7515 GB, free: 192 MB / 0.5919 GB
Notification: Performance of postOpt collapseArrayExpressions (initialization): time 5.638e-05/2.293, allocations: 38.91 kB / 0.7515 GB, free: 192 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 0.0002981/2.293, allocations: 257.1 kB / 0.7518 GB, free: 191.9 MB / 0.5919 GB
Notification: Performance of postOpt lateInlineFunction (simulation): time 0.0001075/2.293, allocations: 102.7 kB / 0.7519 GB, free: 191.8 MB / 0.5919 GB
Notification: Performance of postOpt wrapFunctionCalls (simulation): time 0.003271/2.296, allocations: 3.39 MB / 0.7552 GB, free: 191.1 MB / 0.5919 GB
Notification: Performance of postOpt simplifysemiLinear (simulation): time 9.968e-06/2.296, allocations: 3.984 kB / 0.7552 GB, free: 191.1 MB / 0.5919 GB
Notification: Performance of postOpt simplifyComplexFunction (simulation): time 7.725e-06/2.296, allocations: 0 / 0.7552 GB, free: 191.1 MB / 0.5919 GB
Notification: Performance of postOpt removeConstants (simulation): time 0.0003084/2.297, allocations: 321 kB / 0.7555 GB, free: 190.9 MB / 0.5919 GB
Notification: Performance of postOpt simplifyTimeIndepFuncCalls (simulation): time 8.405e-05/2.297, allocations: 21.45 kB / 0.7555 GB, free: 190.9 MB / 0.5919 GB
Notification: Performance of postOpt simplifyAllExpressions (simulation): time 0.0003044/2.297, allocations: 15.69 kB / 0.7555 GB, free: 190.9 MB / 0.5919 GB
Notification: Performance of postOpt findZeroCrossings (simulation): time 0.0001075/2.297, allocations: 43.62 kB / 0.7556 GB, free: 190.9 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 0.003184/2.3, allocations: 8.156 MB / 0.7635 GB, free: 182.1 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