Running: ./testmodel.py --libraries=/home/hudson/saved_omc/libraries/.openmodelica/libraries --ompython_omhome=/usr ThermoSysPro_ThermoSysPro.Examples.SimpleExamples.TestVolumes2.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.TestVolumes2,tolerance=1e-06,outputFormat="empty",numberOfIntervals=5000,variableFilter="",fileNamePrefix="ThermoSysPro_ThermoSysPro.Examples.SimpleExamples.TestVolumes2")
translateModel(ThermoSysPro.Examples.SimpleExamples.TestVolumes2,tolerance=1e-06,outputFormat="empty",numberOfIntervals=5000,variableFilter="",fileNamePrefix="ThermoSysPro_ThermoSysPro.Examples.SimpleExamples.TestVolumes2")
Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermoSysPro 4.0.0-master/package.mo): time 0.8242/0.8242, allocations: 150.9 MB / 167.2 MB, free: 14.45 MB / 142.1 MB
Notification: Performance of FrontEnd - loaded program: time 0.0003501/0.0003502, allocations: 15.7 kB / 237.8 MB, free: 1.754 MB / 190.1 MB
Notification: Performance of FrontEnd - Absyn->SCode: time 0.05952/0.05989, allocations: 31.35 MB / 269.1 MB, free: 7.012 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.TestVolumes2): time 1.629/1.689, allocations: 299.7 MB / 0.5555 GB, free: 8.066 MB / 446.1 MB
Notification: Performance of NFInst.instExpressions: time 0.5172/2.206, allocations: 188.1 MB / 0.7392 GB, free: 15.57 MB / 0.6075 GB
Notification: Performance of NFInst.updateImplicitVariability: time 0.0006927/2.207, allocations: 10.5 kB / 0.7392 GB, free: 15.57 MB / 0.6075 GB
[/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/LumpedStraightPipe.mo:49:3-50:42: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/LumpedStraightPipe.mo:51:3-53:37: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/LumpedStraightPipe.mo:49:3-50:42: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/LumpedStraightPipe.mo:51:3-53:37: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/ControlValve.mo:45:3-47:43: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/ControlValve.mo:48:3-50:38: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/ControlValve.mo:45:3-47:43: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/ControlValve.mo:48:3-50:38: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/ControlValve.mo:45:3-47:43: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/ControlValve.mo:48:3-50:38: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/ControlValve.mo:45:3-47:43: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/ControlValve.mo:48:3-50:38: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/ControlValve.mo:45:3-47:43: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/ControlValve.mo:48:3-50:38: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/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/PressureLosses/LumpedStraightPipe.mo:49:3-50:42: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/LumpedStraightPipe.mo:51:3-53:37: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/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/Volumes/VolumeC.mo:29:3-31:42:writable] Warning: Connector Ce1 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/Volumes/VolumeC.mo:32:3-34:37:writable] Warning: Connector Ce2 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/Volumes/VolumeC.mo:35:3-37:37:writable] Warning: Connector Cs 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/Volumes/VolumeC.mo:38:3-40:43:writable] Warning: Connector Ce3 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/Volumes/VolumeA.mo:25:3-27:42:writable] Warning: Connector Ce1 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/Volumes/VolumeA.mo:28:3-30:37:writable] Warning: Connector Ce2 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/Volumes/VolumeA.mo:31:3-33:37:writable] Warning: Connector Cs1 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/Volumes/VolumeA.mo:38:3-40:43:writable] Warning: Connector Cs2 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 0.0009301/2.208, allocations: 363.4 kB / 0.7396 GB, free: 15.57 MB / 0.6075 GB
Notification: Performance of NFTyping.typeBindings: time 0.001154/2.209, allocations: 0.5976 MB / 0.7402 GB, free: 15.56 MB / 0.6075 GB
[/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 0.02992/2.239, allocations: 11.9 MB / 0.7518 GB, free: 15.3 MB / 0.6075 GB
Notification: Performance of NFFlatten.flatten: time 0.002772/2.242, allocations: 2.101 MB / 0.7538 GB, free: 15.3 MB / 0.6075 GB
Notification: Performance of NFFlatten.resolveConnections: time 0.0008924/2.243, allocations: 0.7863 MB / 0.7546 GB, free: 15.16 MB / 0.6075 GB
Notification: Performance of NFEvalConstants.evaluate: time 0.001079/2.244, allocations: 0.7983 MB / 0.7554 GB, free: 15.16 MB / 0.6075 GB
Notification: Performance of NFSimplifyModel.simplify: time 0.0007226/2.245, allocations: 0.7747 MB / 0.7561 GB, free: 15.16 MB / 0.6075 GB
Notification: Performance of NFPackage.collectConstants: time 0.0001481/2.245, allocations: 121.3 kB / 0.7562 GB, free: 15.16 MB / 0.6075 GB
Notification: Performance of NFFlatten.collectFunctions: time 0.03634/2.281, allocations: 20.16 MB / 0.7759 GB, free: 11.36 MB / 0.6075 GB
Notification: Performance of NFScalarize.scalarize: time 0.0004627/2.282, allocations: 322.7 kB / 0.7762 GB, free: 11.31 MB / 0.6075 GB
Notification: Performance of NFVerifyModel.verify: time 0.001336/2.283, allocations: 0.8251 MB / 0.777 GB, free: 11.27 MB / 0.6075 GB
Notification: Performance of NFConvertDAE.convert: time 0.02396/2.307, allocations: 11.11 MB / 0.7879 GB, free: 7.02 MB / 0.6075 GB
Notification: Performance of FrontEnd - DAE generated: time 6.512e-06/2.307, allocations: 0 / 0.7879 GB, free: 7.02 MB / 0.6075 GB
Notification: Performance of FrontEnd: time 1.774e-06/2.307, allocations: 2.406 kB / 0.7879 GB, free: 7.02 MB / 0.6075 GB
Notification: Performance of Transformations before backend: time 2.777e-05/2.307, allocations: 0 / 0.7879 GB, free: 7.02 MB / 0.6075 GB
Notification: Model statistics after passing the front-end and creating the data structures used by the back-end:
 * Number of equations: 429
 * Number of variables: 429
Notification: Performance of Generate backend data structure: time 0.007225/2.314, allocations: 2.997 MB / 0.7908 GB, free: 5.203 MB / 0.6075 GB
Notification: Performance of prepare preOptimizeDAE: time 4.02e-05/2.314, allocations: 10.12 kB / 0.7908 GB, free: 5.203 MB / 0.6075 GB
Notification: Performance of preOpt normalInlineFunction (simulation): time 0.0002333/2.314, allocations: 182.3 kB / 0.791 GB, free: 5.109 MB / 0.6075 GB
Notification: Performance of preOpt evaluateParameters (simulation): time 0.0007791/2.315, allocations: 0.6599 MB / 0.7917 GB, free: 4.672 MB / 0.6075 GB
Notification: Performance of preOpt simplifyIfEquations (simulation): time 6.734e-05/2.315, allocations: 93.64 kB / 0.7917 GB, free: 4.668 MB / 0.6075 GB
Notification: Performance of preOpt expandDerOperator (simulation): time 0.000134/2.315, allocations: 117.5 kB / 0.7919 GB, free: 4.664 MB / 0.6075 GB
Notification: Performance of preOpt clockPartitioning (simulation): time 0.00212/2.318, allocations: 1.641 MB / 0.7935 GB, free: 4.012 MB / 0.6075 GB
Notification: Performance of preOpt findStateOrder (simulation): time 2.847e-05/2.318, allocations: 6.469 kB / 0.7935 GB, free: 4.012 MB / 0.6075 GB
Notification: Performance of preOpt replaceEdgeChange (simulation): time 8.477e-05/2.318, allocations: 58.39 kB / 0.7935 GB, free: 4.004 MB / 0.6075 GB
Notification: Performance of preOpt inlineArrayEqn (simulation): time 4.438e-05/2.318, allocations: 64.3 kB / 0.7936 GB, free: 3.992 MB / 0.6075 GB
Notification: Performance of preOpt removeEqualRHS (simulation): time 0.002095/2.32, allocations: 1.125 MB / 0.7947 GB, free: 3.609 MB / 0.6075 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 0.08147/2.401, allocations: 42.12 MB / 0.8358 GB, free: 7.074 MB / 0.6544 GB
Notification: Performance of preOpt comSubExp (simulation): time 0.001896/2.403, allocations: 0.8798 MB / 0.8367 GB, free: 6.191 MB / 0.6544 GB
Notification: Performance of preOpt resolveLoops (simulation): time 0.001068/2.404, allocations: 0.5833 MB / 0.8372 GB, free: 5.609 MB / 0.6544 GB
Notification: Performance of preOpt evalFunc (simulation): time 0.3201/2.724, allocations: 151.4 MB / 0.9851 GB, free: 13.66 MB / 0.8262 GB
Notification: Performance of preOpt encapsulateWhenConditions (simulation): time 4.376e-05/2.725, allocations: 39.84 kB / 0.9851 GB, free: 13.61 MB / 0.8262 GB
Notification: Performance of pre-optimization done (n=197): time 5.2e-06/2.725, allocations: 0 / 0.9851 GB, free: 13.61 MB / 0.8262 GB
Notification: Performance of matching and sorting (n=197): time 0.01792/2.742, allocations: 4.307 MB / 0.9893 GB, free: 9.297 MB / 0.8262 GB
Notification: Performance of inlineWhenForInitialization (initialization): time 6.459e-05/2.743, allocations: 111.5 kB / 0.9894 GB, free: 9.164 MB / 0.8262 GB
Notification: Performance of selectInitializationVariablesDAE (initialization): time 0.001129/2.744, allocations: 0.836 MB / 0.9902 GB, free: 8.305 MB / 0.8262 GB
Notification: Performance of collectPreVariables (initialization): time 6.964e-05/2.744, allocations: 37.7 kB / 0.9903 GB, free: 8.262 MB / 0.8262 GB
Notification: Performance of collectInitialEqns (initialization): time 0.0003918/2.744, allocations: 0.5764 MB / 0.9908 GB, free: 7.68 MB / 0.8262 GB
Notification: Performance of collectInitialBindings (initialization): time 0.0004986/2.745, allocations: 0.635 MB / 0.9915 GB, free: 7.051 MB / 0.8262 GB
Notification: Performance of simplifyInitialFunctions (initialization): time 0.0003573/2.745, allocations: 262.4 kB / 0.9917 GB, free: 6.789 MB / 0.8262 GB
Notification: Performance of setup shared object (initialization): time 9.824e-05/2.745, allocations: 305.1 kB / 0.992 GB, free: 6.488 MB / 0.8262 GB
Notification: Performance of preBalanceInitialSystem (initialization): time 0.0009741/2.746, allocations: 472.2 kB / 0.9924 GB, free: 6.027 MB / 0.8262 GB
Notification: Performance of partitionIndependentBlocks (initialization): time 0.00143/2.748, allocations: 0.7898 MB / 0.9932 GB, free: 5.113 MB / 0.8262 GB
Notification: Performance of analyzeInitialSystem (initialization): time 0.003306/2.751, allocations: 1.382 MB / 0.9946 GB, free: 3.645 MB / 0.8262 GB
Notification: Performance of solveInitialSystemEqSystem (initialization): time 9.087e-06/2.751, allocations: 4 kB / 0.9946 GB, free: 3.641 MB / 0.8262 GB
Notification: Performance of matching and sorting (n=245) (initialization): time 0.004783/2.756, allocations: 1.878 MB / 0.9964 GB, free: 1.805 MB / 0.8262 GB
Notification: Performance of prepare postOptimizeDAE: time 2.738e-05/2.756, allocations: 11.16 kB / 0.9964 GB, free: 1.797 MB / 0.8262 GB
Notification: Performance of postOpt simplifyComplexFunction (initialization): time 2.472e-05/2.756, allocations: 16 kB / 0.9964 GB, free: 1.781 MB / 0.8262 GB
Notification: Performance of postOpt tearingSystem (initialization): time 0.009849/2.766, allocations: 2.379 MB / 0.9988 GB, free: 15.4 MB / 0.8419 GB
Notification: Performance of postOpt solveSimpleEquations (initialization): time 0.0007012/2.766, allocations: 107.7 kB / 0.9989 GB, free: 15.29 MB / 0.8419 GB
Notification: Performance of postOpt calculateStrongComponentJacobians (initialization): time 0.004718/2.771, allocations: 1.857 MB / 1.001 GB, free: 13.41 MB / 0.8419 GB
Notification: Performance of postOpt simplifyAllExpressions (initialization): time 0.001441/2.773, allocations: 178.2 kB / 1.001 GB, free: 13.23 MB / 0.8419 GB
Notification: Performance of postOpt collapseArrayExpressions (initialization): time 0.0001327/2.773, allocations: 47.98 kB / 1.001 GB, free: 13.19 MB / 0.8419 GB
Notification: Model statistics after passing the back-end for initialization:
 * Number of independent subsystems: 40
 * Number of states: 0 ()
 * Number of discrete variables: 30 (volumeA.Cs2.b,volumeA.Cs1.b,volumeA.Ce2.a,volumeA.Ce1.a,volumeC.Ce3.a,volumeC.Cs.b,volumeC.Ce2.a,volumeC.Ce1.a,sinkP1.C.a,lumpedStraightPipe2.C2.b,lumpedStraightPipe2.C1.a,sinkP.C.a,controlValve4.C2.b,controlValve4.C1.a,controlValve3.C2.b,controlValve3.C1.a,controlValve2.C2.b,controlValve2.C1.a,controlValve1.C2.b,controlValve1.C1.a,controlValve.C2.b,controlValve.C1.a,lumpedStraightPipe1.C2.b,lumpedStraightPipe1.C1.a,lumpedStraightPipe.C2.b,lumpedStraightPipe.C1.a,sourceP1.C.b,sourceP.C.b,volumeA.Ce1.b,volumeC.Ce1.b)
 * Number of discrete states: 0 ()
 * Number of clocked states: 0 ()
 * Top-level inputs: 0
Notification: Strong component statistics for initialization (69):
 * Single equations (assignments): 64
 * Array equations: 0
 * Algorithm blocks: 0
 * Record equations: 4
 * When equations: 0
 * If-equations: 0
 * Equation systems (not torn): 0
 * Torn equation systems: 1
 * Mixed (continuous/discrete) equation systems: 0
Notification: Torn system details for strict tearing set:
 * Linear torn systems (#iteration vars, #inner vars, density): 0 systems
 * Non-linear torn systems (#iteration vars, #inner vars): 1 system
   {(18,33)}
Notification: Performance of prepare postOptimizeDAE: time 0.0007063/2.773, allocations: 303.8 kB / 1.001 GB, free: 12.88 MB / 0.8419 GB
Notification: Performance of postOpt lateInlineFunction (simulation): time 0.0003267/2.774, allocations: 126.2 kB / 1.001 GB, free: 12.76 MB / 0.8419 GB
Notification: Performance of postOpt wrapFunctionCalls (simulation): time 0.009073/2.783, allocations: 5.67 MB / 1.007 GB, free: 6.918 MB / 0.8419 GB
Notification: Performance of postOpt simplifysemiLinear (simulation): time 1.383e-05/2.783, allocations: 7.641 kB / 1.007 GB, free: 6.914 MB / 0.8419 GB
Notification: Performance of postOpt simplifyComplexFunction (simulation): time 6.993e-06/2.783, allocations: 0 / 1.007 GB, free: 6.914 MB / 0.8419 GB
Notification: Performance of postOpt removeConstants (simulation): time 0.0006811/2.784, allocations: 326.4 kB / 1.007 GB, free: 6.574 MB / 0.8419 GB
Notification: Performance of postOpt simplifyTimeIndepFuncCalls (simulation): time 0.0002375/2.784, allocations: 35.69 kB / 1.007 GB, free: 6.539 MB / 0.8419 GB
Notification: Performance of postOpt simplifyAllExpressions (simulation): time 0.000897/2.785, allocations: 47.94 kB / 1.007 GB, free: 6.492 MB / 0.8419 GB
Notification: Performance of postOpt findZeroCrossings (simulation): time 0.0002043/2.785, allocations: 64.92 kB / 1.007 GB, free: 6.43 MB / 0.8419 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(lumpedStraightPipe1.T, lumpedStraightPipe1.rho, lumpedStraightPipe1.pro.u, lumpedStraightPipe1.pro.s, lumpedStraightPipe1.pro.cp, lumpedStraightPipe1.pro.ddhp, lumpedStraightPipe1.pro.ddph, lumpedStraightPipe1.pro.duph, lumpedStraightPipe1.pro.duhp, lumpedStraightPipe1.pro.x) = $cse15

Variables:
1: lumpedStraightPipe1.Pm:VARIABLE(min = 0.0 start = 3e5 unit = "Pa" nominal = 1e5 )  "Fluid average pressure" type: Real
2: $cse15.d:VARIABLE(protected = true )  type: Real unreplaceable
3: $cse15.ddhp:VARIABLE(protected = true )  type: Real unreplaceable
4: $cse15.duhp:VARIABLE(protected = true )  type: Real unreplaceable
5: $cse15.s:VARIABLE(protected = true )  type: Real unreplaceable
6: $cse15.cp:VARIABLE(protected = true )  type: Real unreplaceable
7: $cse15.duph:VARIABLE(protected = true )  type: Real unreplaceable
8: $cse15.ddph:VARIABLE(protected = true )  type: Real unreplaceable
9: $cse15.T:VARIABLE(protected = true )  type: Real unreplaceable
10: $cse15.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 (1): 0.0 = controlValve1.Q + (-controlValve4.Q) - controlValve.Q
2/2 (1): $cse12 = ThermoSysPro.Functions.ThermoSquare(controlValve1.Q, controlValve1.eps)
3/3 (1): controlValve1.deltaP * controlValve1.Cv * abs(controlValve1.Cv) = 1.733e12 * $cse12 / controlValve1.rho ^ 2.0
4/4 (10): $cse11 = ThermoSysPro.Properties.Fluid.Ph(controlValve1.Pm, controlValve1.h, controlValve1.mode, controlValve1.fluid)
5/14 (10): ThermoSysPro.Properties.WaterSteam.Common.ThermoProperties_ph(controlValve1.T, controlValve1.rho, controlValve1.pro.u, controlValve1.pro.s, controlValve1.pro.cp, controlValve1.pro.ddhp, controlValve1.pro.ddph, controlValve1.pro.duph, controlValve1.pro.duhp, controlValve1.pro.x) = $cse11
6/24 (1): controlValve1.Pm = 0.5 * (lumpedStraightPipe1.C2.P + volumeA.P)
7/25 (1): controlValve.deltaP = volumeA.P - volumeC.P
8/26 (1): controlValve.deltaP * controlValve.Cv * abs(controlValve.Cv) = 1.733e12 * $cse14 / controlValve.rho ^ 2.0
9/27 (10): $cse13 = ThermoSysPro.Properties.Fluid.Ph(controlValve.Pm, controlValve.h, controlValve.mode, controlValve.fluid)
10/37 (10): ThermoSysPro.Properties.WaterSteam.Common.ThermoProperties_ph(controlValve.T, controlValve.rho, controlValve.pro.u, controlValve.pro.s, controlValve.pro.cp, controlValve.pro.ddhp, controlValve.pro.ddph, controlValve.pro.duph, controlValve.pro.duhp, controlValve.pro.x) = $cse13
11/47 (1): controlValve.Pm = 0.5 * (volumeA.P + volumeC.P)
12/48 (1): sourceP.P0 - volumeC.P = lumpedStraightPipe.deltaP
13/49 (1): lumpedStraightPipe.deltaP = lumpedStraightPipe.deltaPf + 9.80665 * lumpedStraightPipe.rho * (lumpedStraightPipe.z2 - lumpedStraightPipe.z1)
14/50 (1): lumpedStraightPipe.deltaPf = 0.5 * lumpedStraightPipe.khi * $cse18 / (lumpedStraightPipe.A ^ 2.0 * lumpedStraightPipe.rho)
15/51 (1): $cse18 = ThermoSysPro.Functions.ThermoSquare(lumpedStraightPipe.Q, lumpedStraightPipe.eps)
16/52 (1): 0.0 = if lumpedStraightPipe.Q > 0.0 then lumpedStraightPipe.h - sourceP.h else lumpedStraightPipe.h - volumeC.h
17/53 (10): $cse17 = ThermoSysPro.Properties.Fluid.Ph(lumpedStraightPipe.Pm, lumpedStraightPipe.h, lumpedStraightPipe.mode, lumpedStraightPipe.fluid)
18/63 (10): ThermoSysPro.Properties.WaterSteam.Common.ThermoProperties_ph(lumpedStraightPipe.T, lumpedStraightPipe.rho, lumpedStraightPipe.pro.u, lumpedStraightPipe.pro.s, lumpedStraightPipe.pro.cp, lumpedStraightPipe.pro.ddhp, lumpedStraightPipe.pro.ddph, lumpedStraightPipe.pro.duph, lumpedStraightPipe.pro.duhp, lumpedStraightPipe.pro.x) = $cse17
19/73 (1): 0.0 = lumpedStraightPipe.Q + controlValve.Q - lumpedStraightPipe2.Q
20/74 (1): $cse14 = ThermoSysPro.Functions.ThermoSquare(controlValve.Q, controlValve.eps)
21/75 (1): 0.0 = if controlValve.Q > 0.0 then controlValve.h - volumeA.h else controlValve.h - volumeC.h
22/76 (1): lumpedStraightPipe.Pm = 0.5 * (sourceP.P0 + volumeC.P)
23/77 (1): controlValve2.deltaP = volumeC.P - controlValve2.C2.P
24/78 (1): controlValve2.deltaP * controlValve2.Cv * abs(controlValve2.Cv) = 1.733e12 * $cse10 / controlValve2.rho ^ 2.0
25/79 (1): $cse10 = ThermoSysPro.Functions.ThermoSquare(lumpedStraightPipe2.Q, controlValve2.eps)
26/80 (1): $cse4 = ThermoSysPro.Functions.ThermoSquare(lumpedStraightPipe2.Q, lumpedStraightPipe2.eps)
27/81 (1): lumpedStraightPipe2.deltaPf = 0.5 * lumpedStraightPipe2.khi * $cse4 / (lumpedStraightPipe2.A ^ 2.0 * lumpedStraightPipe2.rho)
28/82 (1): lumpedStraightPipe2.deltaP = lumpedStraightPipe2.deltaPf + 9.80665 * lumpedStraightPipe2.rho * (lumpedStraightPipe2.z2 - lumpedStraightPipe2.z1)
29/83 (10): $cse3 = ThermoSysPro.Properties.Fluid.Ph(lumpedStraightPipe2.Pm, lumpedStraightPipe2.h, lumpedStraightPipe2.mode, lumpedStraightPipe2.fluid)
30/93 (10): ThermoSysPro.Properties.WaterSteam.Common.ThermoProperties_ph(lumpedStraightPipe2.T, lumpedStraightPipe2.rho, lumpedStraightPipe2.pro.u, lumpedStraightPipe2.pro.s, lumpedStraightPipe2.pro.cp, lumpedStraightPipe2.pro.ddhp, lumpedStraightPipe2.pro.ddph, lumpedStraightPipe2.pro.duph, lumpedStraightPipe2.pro.duhp, lumpedStraightPipe2.pro.x) = $cse3
31/103 (1): lumpedStraightPipe2.Pm = 0.5 * (controlValve3.C2.P + sinkP1.P0)
32/104 (1): controlValve3.deltaP = controlValve2.C2.P - controlValve3.C2.P
33/105 (1): controlValve3.deltaP * controlValve3.Cv * abs(controlValve3.Cv) = 1.733e12 * $cse8 / controlValve3.rho ^ 2.0
34/106 (10): $cse7 = ThermoSysPro.Properties.Fluid.Ph(controlValve3.Pm, lumpedStraightPipe2.h, controlValve3.mode, controlValve3.fluid)
35/116 (10): ThermoSysPro.Properties.WaterSteam.Common.ThermoProperties_ph(controlValve3.T, controlValve3.rho, controlValve3.pro.u, controlValve3.pro.s, controlValve3.pro.cp, controlValve3.pro.ddhp, controlValve3.pro.ddph, controlValve3.pro.duph, controlValve3.pro.duhp, controlValve3.pro.x) = $cse7
36/126 (1): controlValve3.Pm = 0.5 * (controlValve2.C2.P + controlValve3.C2.P)
37/127 (1): controlValve2.Pm = 0.5 * (volumeC.P + controlValve2.C2.P)
38/128 (10): $cse9 = ThermoSysPro.Properties.Fluid.Ph(controlValve2.Pm, lumpedStraightPipe2.h, controlValve2.mode, controlValve2.fluid)
39/138 (10): ThermoSysPro.Properties.WaterSteam.Common.ThermoProperties_ph(controlValve2.T, controlValve2.rho, controlValve2.pro.u, controlValve2.pro.s, controlValve2.pro.cp, controlValve2.pro.ddhp, controlValve2.pro.ddph, controlValve2.pro.duph, controlValve2.pro.duhp, controlValve2.pro.x) = $cse9
40/148 (1): controlValve3.C2.P - sinkP1.P0 = lumpedStraightPipe2.deltaP
41/149 (1): $cse8 = ThermoSysPro.Functions.ThermoSquare(lumpedStraightPipe2.Q, controlValve3.eps)
42/150 (1): 0.0 = if lumpedStraightPipe2.Q > 0.0 then lumpedStraightPipe2.h - volumeC.h else lumpedStraightPipe2.h - controlValve2.C2.h_vol
43/151 (1): 0.0 = if lumpedStraightPipe2.Q > 0.0 then lumpedStraightPipe2.h - controlValve2.C2.h_vol else lumpedStraightPipe2.h - controlValve3.C2.h_vol
44/152 (1): 0.0 = if lumpedStraightPipe2.Q > 0.0 then lumpedStraightPipe2.h - controlValve3.C2.h_vol else lumpedStraightPipe2.h - sinkP1.h
45/153 (1): controlValve1.deltaP = lumpedStraightPipe1.C2.P - volumeA.P
46/154 (1): controlValve4.deltaP = volumeA.P - sinkP.P0
47/155 (1): controlValve4.deltaP * controlValve4.Cv * abs(controlValve4.Cv) = 1.733e12 * $cse6 / controlValve4.rho ^ 2.0
48/156 (1): $cse6 = ThermoSysPro.Functions.ThermoSquare(controlValve4.Q, controlValve4.eps)
49/157 (1): 0.0 = if controlValve4.Q > 0.0 then controlValve4.h - volumeA.h else controlValve4.h - sinkP.h
50/158 (10): $cse5 = ThermoSysPro.Properties.Fluid.Ph(controlValve4.Pm, controlValve4.h, controlValve4.mode, controlValve4.fluid)
51/168 (10): ThermoSysPro.Properties.WaterSteam.Common.ThermoProperties_ph(controlValve4.T, controlValve4.rho, controlValve4.pro.u, controlValve4.pro.s, controlValve4.pro.cp, controlValve4.pro.ddhp, controlValve4.pro.ddph, controlValve4.pro.duph, controlValve4.pro.duhp, controlValve4.pro.x) = $cse5
52/178 (1): controlValve4.Pm = 0.5 * (volumeA.P + sinkP.P0)
53/179 (1): $cse16 = ThermoSysPro.Functions.ThermoSquare(controlValve1.Q, lumpedStraightPipe1.eps)
54/180 (1): lumpedStraightPipe1.deltaPf = 0.5 * lumpedStraightPipe1.khi * $cse16 / (lumpedStraightPipe1.A ^ 2.0 * lumpedStraightPipe1.rho)
55/181 (1): lumpedStraightPipe1.deltaP = lumpedStraightPipe1.deltaPf + 9.80665 * lumpedStraightPipe1.rho * (lumpedStraightPipe1.z2 - lumpedStraightPipe1.z1)
56/182 (10): $cse15 = ThermoSysPro.Properties.Fluid.Ph(lumpedStraightPipe1.Pm, controlValve1.h, lumpedStraightPipe1.mode, lumpedStraightPipe1.fluid)
57/192 (1): lumpedStraightPipe1.Pm = 0.5 * (sourceP1.P0 + lumpedStraightPipe1.C2.P)
58/193 (1): sourceP1.P0 - lumpedStraightPipe1.C2.P = lumpedStraightPipe1.deltaP
59/194 (10): ThermoSysPro.Properties.WaterSteam.Common.ThermoProperties_ph(lumpedStraightPipe1.T, lumpedStraightPipe1.rho, lumpedStraightPipe1.pro.u, lumpedStraightPipe1.pro.s, lumpedStraightPipe1.pro.cp, lumpedStraightPipe1.pro.ddhp, lumpedStraightPipe1.pro.ddph, lumpedStraightPipe1.pro.duph, lumpedStraightPipe1.pro.duhp, lumpedStraightPipe1.pro.x) = $cse15
60/204 (1): 0.0 = if controlValve1.Q > 0.0 then controlValve1.h - sourceP1.h else controlValve1.h - lumpedStraightPipe1.C2.h_vol
61/205 (1): 0.0 = if controlValve1.Q > 0.0 then controlValve1.h - lumpedStraightPipe1.C2.h_vol else controlValve1.h - volumeA.h

Variables:
1: controlValve1.h:VARIABLE(start = 71016.0 unit = "J/kg" )  "Fluid specific enthalpy" type: Real
2: lumpedStraightPipe1.C2.h_vol:VARIABLE(flow=false start = 71028.65153712753 unit = "J/kg" )  "Fluid specific enthalpy in the control volume" type: Real
3: lumpedStraightPipe1.pro.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 )  "Specific inner energy" type: Real
4: lumpedStraightPipe1.pro.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific entropy" type: Real
5: lumpedStraightPipe1.T:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 300.0 )  "Fluid temperature" type: Real
6: lumpedStraightPipe1.pro.ddph:VARIABLE(unit = "s2/m2" )  "Derivative of density wrt. pressure at constant specific enthalpy" type: Real
7: lumpedStraightPipe1.pro.duhp:VARIABLE(unit = "1" )  "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real
8: lumpedStraightPipe1.pro.ddhp:VARIABLE(unit = "kg.s2/m5" )  "Derivative of density wrt. specific enthalpy at constant pressure" type: Real
9: lumpedStraightPipe1.pro.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific heat capacity at constant presure" type: Real
10: lumpedStraightPipe1.deltaP:VARIABLE(unit = "Pa" )  "Total pressure loss" type: Real
11: lumpedStraightPipe1.C2.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 )  "Fluid pressure in the control volume" type: Real
12: lumpedStraightPipe1.Pm:VARIABLE(min = 0.0 start = 3e5 unit = "Pa" nominal = 1e5 )  "Fluid average pressure" type: Real
13: $cse15.d:VARIABLE(protected = true )  type: Real unreplaceable
14: $cse15.ddhp:VARIABLE(protected = true )  type: Real unreplaceable
15: $cse15.duhp:VARIABLE(protected = true )  type: Real unreplaceable
16: $cse15.s:VARIABLE(protected = true )  type: Real unreplaceable
17: $cse15.cp:VARIABLE(protected = true )  type: Real unreplaceable
18: $cse15.duph:VARIABLE(protected = true )  type: Real unreplaceable
19: $cse15.ddph:VARIABLE(protected = true )  type: Real unreplaceable
20: $cse15.T:VARIABLE(protected = true )  type: Real unreplaceable
21: $cse15.u:VARIABLE(protected = true )  type: Real unreplaceable
22: $cse15.x:VARIABLE(protected = true )  type: Real unreplaceable
23: lumpedStraightPipe1.pro.duph:VARIABLE(unit = "m3/kg" )  "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real
24: lumpedStraightPipe1.pro.x:VARIABLE(min = 0.0 max = 1.0 unit = "1" )  "Vapor mass fraction" type: Real
25: lumpedStraightPipe1.deltaPf:VARIABLE(unit = "Pa" )  "Friction pressure loss" type: Real
26: lumpedStraightPipe1.rho:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 )  "Fluid density" type: Real
27: $cse16:VARIABLE(protected = true )  type: Real unreplaceable
28: controlValve4.Pm:VARIABLE(min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 )  "Fluid average pressure" type: Real
29: controlValve4.rho:VARIABLE(min = 1e-9 max = 1e5 start = 998.0 unit = "kg/m3" nominal = 998.0 )  "Fluid density" type: Real
30: controlValve4.pro.duph:VARIABLE(unit = "m3/kg" )  "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real
31: controlValve4.pro.ddph:VARIABLE(unit = "s2/m2" )  "Derivative of density wrt. pressure at constant specific enthalpy" type: Real
32: controlValve4.pro.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific heat capacity at constant presure" type: Real
33: controlValve4.pro.ddhp:VARIABLE(unit = "kg.s2/m5" )  "Derivative of density wrt. specific enthalpy at constant pressure" type: Real
34: controlValve4.pro.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific entropy" type: Real
35: controlValve4.T:VARIABLE(min = 200.0 max = 6000.0 start = 290.0 unit = "K" nominal = 300.0 )  "Fluid temperature" type: Real
36: controlValve4.pro.duhp:VARIABLE(unit = "1" )  "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real
37: controlValve4.pro.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 )  "Specific inner energy" type: Real
38: controlValve4.pro.x:VARIABLE(min = 0.0 max = 1.0 unit = "1" )  "Vapor mass fraction" type: Real
39: $cse5.ddph:VARIABLE(protected = true )  type: Real unreplaceable
40: $cse5.duph:VARIABLE(protected = true )  type: Real unreplaceable
41: $cse5.ddhp:VARIABLE(protected = true )  type: Real unreplaceable
42: $cse5.duhp:VARIABLE(protected = true )  type: Real unreplaceable
43: $cse5.s:VARIABLE(protected = true )  type: Real unreplaceable
44: $cse5.u:VARIABLE(protected = true )  type: Real unreplaceable
45: $cse5.T:VARIABLE(protected = true )  type: Real unreplaceable
46: $cse5.x:VARIABLE(protected = true )  type: Real unreplaceable
47: $cse5.cp:VARIABLE(protected = true )  type: Real unreplaceable
48: $cse5.d:VARIABLE(protected = true )  type: Real unreplaceable
49: controlValve4.h:VARIABLE(start = 70826.0 unit = "J/kg" )  "Fluid specific enthalpy" type: Real
50: controlValve4.Q:VARIABLE(start = 500.0 unit = "kg/s" )  "Mass flow rate" type: Real
51: $cse6:VARIABLE(protected = true )  type: Real unreplaceable
52: controlValve4.deltaP:VARIABLE(unit = "Pa" )  "Singular pressure loss" type: Real
53: controlValve1.deltaP:VARIABLE(unit = "Pa" )  "Singular pressure loss" type: Real
54: controlValve3.C2.h_vol:VARIABLE(flow=false start = 71029.67205985427 unit = "J/kg" )  "Fluid specific enthalpy in the control volume" type: Real
55: controlValve2.C2.h_vol:VARIABLE(flow=false start = 71029.67205985432 unit = "J/kg" )  "Fluid specific enthalpy in the control volume" type: Real
56: lumpedStraightPipe2.h:VARIABLE(start = 70990.0 unit = "J/kg" )  "Fluid specific enthalpy" type: Real
57: $cse8:VARIABLE(protected = true )  type: Real unreplaceable
58: lumpedStraightPipe2.deltaP:VARIABLE(unit = "Pa" )  "Total pressure loss" type: Real
59: controlValve2.pro.ddhp:VARIABLE(unit = "kg.s2/m5" )  "Derivative of density wrt. specific enthalpy at constant pressure" type: Real
60: controlValve2.pro.x:VARIABLE(min = 0.0 max = 1.0 unit = "1" )  "Vapor mass fraction" type: Real
61: controlValve2.pro.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 )  "Specific inner energy" type: Real
62: controlValve2.rho:VARIABLE(min = 1e-9 max = 1e5 start = 998.0 unit = "kg/m3" nominal = 998.0 )  "Fluid density" type: Real
63: controlValve2.pro.duph:VARIABLE(unit = "m3/kg" )  "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real
64: controlValve2.pro.ddph:VARIABLE(unit = "s2/m2" )  "Derivative of density wrt. pressure at constant specific enthalpy" type: Real
65: controlValve2.pro.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific entropy" type: Real
66: controlValve2.T:VARIABLE(min = 200.0 max = 6000.0 start = 290.0 unit = "K" nominal = 300.0 )  "Fluid temperature" type: Real
67: controlValve2.pro.duhp:VARIABLE(unit = "1" )  "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real
68: controlValve2.pro.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific heat capacity at constant presure" type: Real
69: $cse9.T:VARIABLE(protected = true )  type: Real unreplaceable
70: $cse9.duph:VARIABLE(protected = true )  type: Real unreplaceable
71: $cse9.s:VARIABLE(protected = true )  type: Real unreplaceable
72: $cse9.duhp:VARIABLE(protected = true )  type: Real unreplaceable
73: $cse9.cp:VARIABLE(protected = true )  type: Real unreplaceable
74: $cse9.d:VARIABLE(protected = true )  type: Real unreplaceable
75: $cse9.ddph:VARIABLE(protected = true )  type: Real unreplaceable
76: $cse9.x:VARIABLE(protected = true )  type: Real unreplaceable
77: $cse9.ddhp:VARIABLE(protected = true )  type: Real unreplaceable
78: $cse9.u:VARIABLE(protected = true )  type: Real unreplaceable
79: controlValve2.Pm:VARIABLE(min = 0.0 start = 2e5 unit = "Pa" nominal = 1e5 )  "Fluid average pressure" type: Real
80: controlValve2.C2.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 )  "Fluid pressure in the control volume" type: Real
81: controlValve3.pro.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 )  "Specific inner energy" type: Real
82: $cse7.d:VARIABLE(protected = true )  type: Real unreplaceable
83: $cse7.x:VARIABLE(protected = true )  type: Real unreplaceable
84: $cse7.cp:VARIABLE(protected = true )  type: Real unreplaceable
85: $cse7.ddhp:VARIABLE(protected = true )  type: Real unreplaceable
86: $cse7.duhp:VARIABLE(protected = true )  type: Real unreplaceable
87: controlValve3.Pm:VARIABLE(min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 )  "Fluid average pressure" type: Real
88: $cse7.u:VARIABLE(protected = true )  type: Real unreplaceable
89: $cse7.T:VARIABLE(protected = true )  type: Real unreplaceable
90: $cse7.s:VARIABLE(protected = true )  type: Real unreplaceable
91: $cse7.duph:VARIABLE(protected = true )  type: Real unreplaceable
92: $cse7.ddph:VARIABLE(protected = true )  type: Real unreplaceable
93: controlValve3.pro.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific entropy" type: Real
94: controlValve3.pro.duph:VARIABLE(unit = "m3/kg" )  "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real
95: controlValve3.pro.duhp:VARIABLE(unit = "1" )  "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real
96: controlValve3.pro.x:VARIABLE(min = 0.0 max = 1.0 unit = "1" )  "Vapor mass fraction" type: Real
97: controlValve3.pro.ddhp:VARIABLE(unit = "kg.s2/m5" )  "Derivative of density wrt. specific enthalpy at constant pressure" type: Real
98: controlValve3.T:VARIABLE(min = 200.0 max = 6000.0 start = 290.0 unit = "K" nominal = 300.0 )  "Fluid temperature" type: Real
99: controlValve3.pro.ddph:VARIABLE(unit = "s2/m2" )  "Derivative of density wrt. pressure at constant specific enthalpy" type: Real
100: controlValve3.pro.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific heat capacity at constant presure" type: Real
101: controlValve3.rho:VARIABLE(min = 1e-9 max = 1e5 start = 998.0 unit = "kg/m3" nominal = 998.0 )  "Fluid density" type: Real
102: controlValve3.deltaP:VARIABLE(unit = "Pa" )  "Singular pressure loss" type: Real
103: controlValve3.C2.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 )  "Fluid pressure in the control volume" type: Real
104: lumpedStraightPipe2.pro.ddph:VARIABLE(unit = "s2/m2" )  "Derivative of density wrt. pressure at constant specific enthalpy" type: Real
105: $cse3.ddhp:VARIABLE(protected = true )  type: Real unreplaceable
106: $cse3.cp:VARIABLE(protected = true )  type: Real unreplaceable
107: $cse3.s:VARIABLE(protected = true )  type: Real unreplaceable
108: $cse3.duph:VARIABLE(protected = true )  type: Real unreplaceable
109: $cse3.duhp:VARIABLE(protected = true )  type: Real unreplaceable
110: $cse3.u:VARIABLE(protected = true )  type: Real unreplaceable
111: $cse3.d:VARIABLE(protected = true )  type: Real unreplaceable
112: lumpedStraightPipe2.Pm:VARIABLE(min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 )  "Fluid average pressure" type: Real
113: $cse3.T:VARIABLE(protected = true )  type: Real unreplaceable
114: $cse3.x:VARIABLE(protected = true )  type: Real unreplaceable
115: $cse3.ddph:VARIABLE(protected = true )  type: Real unreplaceable
116: lumpedStraightPipe2.pro.ddhp:VARIABLE(unit = "kg.s2/m5" )  "Derivative of density wrt. specific enthalpy at constant pressure" type: Real
117: lumpedStraightPipe2.pro.duhp:VARIABLE(unit = "1" )  "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real
118: lumpedStraightPipe2.pro.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 )  "Specific inner energy" type: Real
119: lumpedStraightPipe2.pro.duph:VARIABLE(unit = "m3/kg" )  "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real
120: lumpedStraightPipe2.pro.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific entropy" type: Real
121: lumpedStraightPipe2.T:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 300.0 )  "Fluid temperature" type: Real
122: lumpedStraightPipe2.pro.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific heat capacity at constant presure" type: Real
123: lumpedStraightPipe2.pro.x:VARIABLE(min = 0.0 max = 1.0 unit = "1" )  "Vapor mass fraction" type: Real
124: lumpedStraightPipe2.deltaPf:VARIABLE(unit = "Pa" )  "Friction pressure loss" type: Real
125: lumpedStraightPipe2.rho:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 )  "Fluid density" type: Real
126: $cse4:VARIABLE(protected = true )  type: Real unreplaceable
127: lumpedStraightPipe2.Q:VARIABLE(start = 100.0 unit = "kg/s" )  "Mass flow rate" type: Real
128: $cse10:VARIABLE(protected = true )  type: Real unreplaceable
129: controlValve2.deltaP:VARIABLE(unit = "Pa" )  "Singular pressure loss" type: Real
130: lumpedStraightPipe.Pm:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 )  "Fluid average pressure" type: Real
131: controlValve.h:VARIABLE(start = 70897.0 unit = "J/kg" )  "Fluid specific enthalpy" type: Real
132: $cse14:VARIABLE(protected = true )  type: Real unreplaceable
133: controlValve.Q:VARIABLE(start = 0.0 unit = "kg/s" )  "Mass flow rate" type: Real
134: lumpedStraightPipe.pro.ddph:VARIABLE(unit = "s2/m2" )  "Derivative of density wrt. pressure at constant specific enthalpy" type: Real
135: lumpedStraightPipe.T:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 300.0 )  "Fluid temperature" type: Real
136: lumpedStraightPipe.rho:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 )  "Fluid density" type: Real
137: lumpedStraightPipe.pro.duhp:VARIABLE(unit = "1" )  "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real
138: lumpedStraightPipe.pro.ddhp:VARIABLE(unit = "kg.s2/m5" )  "Derivative of density wrt. specific enthalpy at constant pressure" type: Real
139: lumpedStraightPipe.pro.duph:VARIABLE(unit = "m3/kg" )  "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real
140: lumpedStraightPipe.pro.x:VARIABLE(min = 0.0 max = 1.0 unit = "1" )  "Vapor mass fraction" type: Real
141: lumpedStraightPipe.pro.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 )  "Specific inner energy" type: Real
142: lumpedStraightPipe.pro.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific heat capacity at constant presure" type: Real
143: lumpedStraightPipe.pro.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific entropy" type: Real
144: $cse17.duhp:VARIABLE(protected = true )  type: Real unreplaceable
145: $cse17.T:VARIABLE(protected = true )  type: Real unreplaceable
146: $cse17.ddph:VARIABLE(protected = true )  type: Real unreplaceable
147: $cse17.cp:VARIABLE(protected = true )  type: Real unreplaceable
148: $cse17.x:VARIABLE(protected = true )  type: Real unreplaceable
149: $cse17.ddhp:VARIABLE(protected = true )  type: Real unreplaceable
150: $cse17.s:VARIABLE(protected = true )  type: Real unreplaceable
151: $cse17.duph:VARIABLE(protected = true )  type: Real unreplaceable
152: $cse17.d:VARIABLE(protected = true )  type: Real unreplaceable
153: $cse17.u:VARIABLE(protected = true )  type: Real unreplaceable
154: lumpedStraightPipe.h:VARIABLE(start = 70990.0 unit = "J/kg" )  "Fluid specific enthalpy" type: Real
155: lumpedStraightPipe.Q:VARIABLE(start = 100.0 unit = "kg/s" )  "Mass flow rate" type: Real
156: $cse18:VARIABLE(protected = true )  type: Real unreplaceable
157: lumpedStraightPipe.deltaPf:VARIABLE(unit = "Pa" )  "Friction pressure loss" type: Real
158: lumpedStraightPipe.deltaP:VARIABLE(unit = "Pa" )  "Total pressure loss" type: Real
159: volumeC.P:VARIABLE(min = 0.0 start = 3e5 unit = "Pa" nominal = 1e5 )  "Fluid pressure" type: Real
160: controlValve.pro.duhp:VARIABLE(unit = "1" )  "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real
161: controlValve.pro.duph:VARIABLE(unit = "m3/kg" )  "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real
162: controlValve.pro.x:VARIABLE(min = 0.0 max = 1.0 unit = "1" )  "Vapor mass fraction" type: Real
163: controlValve.pro.ddph:VARIABLE(unit = "s2/m2" )  "Derivative of density wrt. pressure at constant specific enthalpy" type: Real
164: $cse13.T:VARIABLE(protected = true )  type: Real unreplaceable
165: $cse13.duph:VARIABLE(protected = true )  type: Real unreplaceable
166: controlValve.Pm:VARIABLE(min = 0.0 start = 2e5 unit = "Pa" nominal = 1e5 )  "Fluid average pressure" type: Real
167: $cse13.cp:VARIABLE(protected = true )  type: Real unreplaceable
168: $cse13.x:VARIABLE(protected = true )  type: Real unreplaceable
169: $cse13.ddhp:VARIABLE(protected = true )  type: Real unreplaceable
170: $cse13.s:VARIABLE(protected = true )  type: Real unreplaceable
171: $cse13.d:VARIABLE(protected = true )  type: Real unreplaceable
172: $cse13.u:VARIABLE(protected = true )  type: Real unreplaceable
173: $cse13.ddph:VARIABLE(protected = true )  type: Real unreplaceable
174: $cse13.duhp:VARIABLE(protected = true )  type: Real unreplaceable
175: controlValve.pro.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 )  "Specific inner energy" type: Real
176: controlValve.pro.ddhp:VARIABLE(unit = "kg.s2/m5" )  "Derivative of density wrt. specific enthalpy at constant pressure" type: Real
177: controlValve.pro.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific heat capacity at constant presure" type: Real
178: controlValve.pro.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific entropy" type: Real
179: controlValve.T:VARIABLE(min = 200.0 max = 6000.0 start = 290.0 unit = "K" nominal = 300.0 )  "Fluid temperature" type: Real
180: controlValve.rho:VARIABLE(min = 1e-9 max = 1e5 start = 998.0 unit = "kg/m3" nominal = 998.0 )  "Fluid density" type: Real
181: controlValve.deltaP:VARIABLE(unit = "Pa" )  "Singular pressure loss" type: Real
182: volumeA.P:VARIABLE(min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 )  "Fluid pressure" type: Real
183: controlValve1.pro.duhp:VARIABLE(unit = "1" )  "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real
184: $cse11.cp:VARIABLE(protected = true )  type: Real unreplaceable
185: $cse11.duhp:VARIABLE(protected = true )  type: Real unreplaceable
186: $cse11.s:VARIABLE(protected = true )  type: Real unreplaceable
187: $cse11.duph:VARIABLE(protected = true )  type: Real unreplaceable
188: $cse11.ddph:VARIABLE(protected = true )  type: Real unreplaceable
189: $cse11.d:VARIABLE(protected = true )  type: Real unreplaceable
190: $cse11.u:VARIABLE(protected = true )  type: Real unreplaceable
191: controlValve1.Pm:VARIABLE(min = 0.0 start = 2e5 unit = "Pa" nominal = 1e5 )  "Fluid average pressure" type: Real
192: $cse11.T:VARIABLE(protected = true )  type: Real unreplaceable
193: $cse11.x:VARIABLE(protected = true )  type: Real unreplaceable
194: $cse11.ddhp:VARIABLE(protected = true )  type: Real unreplaceable
195: controlValve1.pro.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 )  "Specific inner energy" type: Real
196: controlValve1.pro.x:VARIABLE(min = 0.0 max = 1.0 unit = "1" )  "Vapor mass fraction" type: Real
197: controlValve1.pro.ddhp:VARIABLE(unit = "kg.s2/m5" )  "Derivative of density wrt. specific enthalpy at constant pressure" type: Real
198: controlValve1.pro.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific entropy" type: Real
199: controlValve1.pro.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific heat capacity at constant presure" type: Real
200: controlValve1.pro.ddph:VARIABLE(unit = "s2/m2" )  "Derivative of density wrt. pressure at constant specific enthalpy" type: Real
201: controlValve1.T:VARIABLE(min = 200.0 max = 6000.0 start = 290.0 unit = "K" nominal = 300.0 )  "Fluid temperature" type: Real
202: controlValve1.pro.duph:VARIABLE(unit = "m3/kg" )  "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real
203: controlValve1.rho:VARIABLE(min = 1e-9 max = 1e5 start = 998.0 unit = "kg/m3" nominal = 998.0 )  "Fluid density" type: Real
204: $cse12:VARIABLE(protected = true )  type: Real unreplaceable
205: controlValve1.Q:VARIABLE(start = 500.0 unit = "kg/s" )  "Mass flow rate" 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 0.1986/2.984, allocations: 11.73 MB / 1.019 GB, free: 453.6 MB / 0.8419 GB
Error: post-optimization module createDAEmodeBDAE (simulation) failed.
Error: Internal error SimCode DAEmode: The model ThermoSysPro.Examples.SimpleExamples.TestVolumes2 could not be translated