Running: ./testmodel.py --libraries=/home/hudson/saved_omc/libraries/.openmodelica/libraries --ompython_omhome=/usr ThermoSysPro_ThermoSysPro.Examples.SimpleExamples.TestJunctions3.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.TestJunctions3,tolerance=1e-06,outputFormat="empty",numberOfIntervals=5000,variableFilter="",fileNamePrefix="ThermoSysPro_ThermoSysPro.Examples.SimpleExamples.TestJunctions3")
translateModel(ThermoSysPro.Examples.SimpleExamples.TestJunctions3,tolerance=1e-06,outputFormat="empty",numberOfIntervals=5000,variableFilter="",fileNamePrefix="ThermoSysPro_ThermoSysPro.Examples.SimpleExamples.TestJunctions3")
Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermoSysPro 4.0.0-master/package.mo): time 0.847/0.8471, allocations: 150.9 MB / 167.2 MB, free: 14.52 MB / 142.1 MB
Notification: Performance of FrontEnd - loaded program: time 0.0003563/0.0003563, allocations: 17.36 kB / 237.8 MB, free: 1.938 MB / 190.1 MB
Notification: Performance of FrontEnd - Absyn->SCode: time 0.05631/0.05668, allocations: 31.35 MB / 269.1 MB, free: 7.172 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.TestJunctions3): time 1.617/1.673, allocations: 299.2 MB / 0.555 GB, free: 8.555 MB / 446.1 MB
Notification: Performance of NFInst.instExpressions: time 0.491/2.164, allocations: 187.9 MB / 0.7385 GB, free: 15.5 MB / 0.6075 GB
Notification: Performance of NFInst.updateImplicitVariability: time 0.000587/2.165, allocations: 10.28 kB / 0.7385 GB, free: 15.5 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/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/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/Junctions/Mixer8.mo:12:3-14:68:writable] Warning: Connector Ce5 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/Junctions/Mixer8.mo:15:3-17:69:writable] Warning: Connector Ce6 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/Junctions/Mixer8.mo:18:3-20:68:writable] Warning: Connector Ce7 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/Junctions/Mixer8.mo:21:3-23:75: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/Junctions/Mixer8.mo:24:3-26:74: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/Junctions/Mixer8.mo:27:3-29:72: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/Junctions/Mixer8.mo:30:3-32:73: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/Junctions/Mixer8.mo:33:3-35:74:writable] Warning: Connector Ce8 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/Junctions/Mixer8.mo:37:3-39:66:writable] Warning: Connector Ce4 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/Junctions/Mixer8.mo:12:3-14:68:writable] Warning: Connector Ce5 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/Junctions/Mixer8.mo:15:3-17:69:writable] Warning: Connector Ce6 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/Junctions/Mixer8.mo:18:3-20:68:writable] Warning: Connector Ce7 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/Junctions/Mixer8.mo:21:3-23:75: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/Junctions/Mixer8.mo:24:3-26:74: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/Junctions/Mixer8.mo:27:3-29:72: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/Junctions/Mixer8.mo:30:3-32:73: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/Junctions/Mixer8.mo:33:3-35:74:writable] Warning: Connector Ce8 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/Junctions/Mixer8.mo:37:3-39:66:writable] Warning: Connector Ce4 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/Junctions/Mixer8.mo:12:3-14:68:writable] Warning: Connector Ce5 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/Junctions/Mixer8.mo:15:3-17:69:writable] Warning: Connector Ce6 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/Junctions/Mixer8.mo:18:3-20:68:writable] Warning: Connector Ce7 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/Junctions/Mixer8.mo:21:3-23:75: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/Junctions/Mixer8.mo:24:3-26:74: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/Junctions/Mixer8.mo:27:3-29:72: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/Junctions/Mixer8.mo:30:3-32:73: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/Junctions/Mixer8.mo:33:3-35:74:writable] Warning: Connector Ce8 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/Junctions/Mixer8.mo:37:3-39:66:writable] Warning: Connector Ce4 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 0.0008959/2.166, allocations: 322.1 kB / 0.7388 GB, free: 15.5 MB / 0.6075 GB
Notification: Performance of NFTyping.typeBindings: time 0.001004/2.167, allocations: 0.516 MB / 0.7393 GB, free: 15.49 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 0.03088/2.198, allocations: 11.79 MB / 0.7508 GB, free: 15.25 MB / 0.6075 GB
Notification: Performance of NFFlatten.flatten: time 0.002352/2.2, allocations: 1.919 MB / 0.7527 GB, free: 15.25 MB / 0.6075 GB
Notification: Performance of NFFlatten.resolveConnections: time 0.000753/2.201, allocations: 0.6726 MB / 0.7534 GB, free: 15.14 MB / 0.6075 GB
Notification: Performance of NFEvalConstants.evaluate: time 0.000935/2.202, allocations: 0.72 MB / 0.7541 GB, free: 15.14 MB / 0.6075 GB
Notification: Performance of NFSimplifyModel.simplify: time 0.000664/2.203, allocations: 0.6899 MB / 0.7548 GB, free: 15.14 MB / 0.6075 GB
Notification: Performance of NFPackage.collectConstants: time 0.0001385/2.203, allocations: 120.2 kB / 0.7549 GB, free: 15.14 MB / 0.6075 GB
Notification: Performance of NFFlatten.collectFunctions: time 0.037/2.24, allocations: 20.18 MB / 0.7746 GB, free: 11.49 MB / 0.6075 GB
Notification: Performance of NFScalarize.scalarize: time 0.0004971/2.24, allocations: 292.8 kB / 0.7748 GB, free: 11.45 MB / 0.6075 GB
Notification: Performance of NFVerifyModel.verify: time 0.001497/2.242, allocations: 0.761 MB / 0.7756 GB, free: 11.41 MB / 0.6075 GB
Notification: Performance of NFConvertDAE.convert: time 0.0309/2.273, allocations: 10.99 MB / 0.7863 GB, free: 7.297 MB / 0.6075 GB
Notification: Performance of FrontEnd - DAE generated: time 7.695e-06/2.273, allocations: 2.75 kB / 0.7863 GB, free: 7.297 MB / 0.6075 GB
Notification: Performance of FrontEnd: time 1.683e-06/2.273, allocations: 0 / 0.7863 GB, free: 7.297 MB / 0.6075 GB
Notification: Performance of Transformations before backend: time 2.204e-05/2.273, allocations: 0 / 0.7863 GB, free: 7.297 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: 431
 * Number of variables: 431
Notification: Performance of Generate backend data structure: time 0.007483/2.28, allocations: 2.826 MB / 0.7891 GB, free: 5.609 MB / 0.6075 GB
Notification: Performance of prepare preOptimizeDAE: time 4.283e-05/2.28, allocations: 10.34 kB / 0.7891 GB, free: 5.609 MB / 0.6075 GB
Notification: Performance of preOpt normalInlineFunction (simulation): time 0.0002418/2.28, allocations: 171.1 kB / 0.7893 GB, free: 5.523 MB / 0.6075 GB
Notification: Performance of preOpt evaluateParameters (simulation): time 0.0007425/2.281, allocations: 0.5656 MB / 0.7898 GB, free: 5.148 MB / 0.6075 GB
Notification: Performance of preOpt simplifyIfEquations (simulation): time 6.29e-05/2.281, allocations: 100.2 kB / 0.7899 GB, free: 5.145 MB / 0.6075 GB
Notification: Performance of preOpt expandDerOperator (simulation): time 0.0001176/2.281, allocations: 127.9 kB / 0.79 GB, free: 5.141 MB / 0.6075 GB
Notification: Performance of preOpt clockPartitioning (simulation): time 0.002169/2.284, allocations: 1.759 MB / 0.7917 GB, free: 4.293 MB / 0.6075 GB
Notification: Performance of preOpt findStateOrder (simulation): time 3.123e-05/2.284, allocations: 7.844 kB / 0.7918 GB, free: 4.293 MB / 0.6075 GB
Notification: Performance of preOpt replaceEdgeChange (simulation): time 8.893e-05/2.284, allocations: 57.94 kB / 0.7918 GB, free: 4.293 MB / 0.6075 GB
Notification: Performance of preOpt inlineArrayEqn (simulation): time 4.307e-05/2.284, allocations: 62.59 kB / 0.7919 GB, free: 4.285 MB / 0.6075 GB
Notification: Performance of preOpt removeEqualRHS (simulation): time 0.001619/2.285, allocations: 1.028 MB / 0.7929 GB, free: 4.145 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 0.06373/2.349, allocations: 36.87 MB / 0.8289 GB, free: 14.41 MB / 0.6544 GB
Notification: Performance of preOpt comSubExp (simulation): time 0.001323/2.351, allocations: 0.6054 MB / 0.8295 GB, free: 13.8 MB / 0.6544 GB
Notification: Performance of preOpt resolveLoops (simulation): time 0.0007102/2.351, allocations: 416.4 kB / 0.8299 GB, free: 13.39 MB / 0.6544 GB
Notification: Performance of preOpt evalFunc (simulation): time 0.3001/2.651, allocations: 151.4 MB / 0.9777 GB, free: 5.438 MB / 0.8106 GB
Notification: Performance of preOpt encapsulateWhenConditions (simulation): time 4.261e-05/2.651, allocations: 35.75 kB / 0.9777 GB, free: 5.395 MB / 0.8106 GB
Notification: Performance of pre-optimization done (n=146): time 3.446e-06/2.651, allocations: 0 / 0.9777 GB, free: 5.395 MB / 0.8106 GB
Notification: Performance of matching and sorting (n=146): time 0.007328/2.659, allocations: 2.278 MB / 0.98 GB, free: 3.102 MB / 0.8106 GB
Notification: Performance of inlineWhenForInitialization (initialization): time 3.509e-05/2.659, allocations: 58 kB / 0.98 GB, free: 3.035 MB / 0.8106 GB
Notification: Performance of selectInitializationVariablesDAE (initialization): time 0.001091/2.66, allocations: 0.8326 MB / 0.9808 GB, free: 2.195 MB / 0.8106 GB
Notification: Performance of collectPreVariables (initialization): time 5.042e-05/2.66, allocations: 33.7 kB / 0.9809 GB, free: 2.156 MB / 0.8106 GB
Notification: Performance of collectInitialEqns (initialization): time 0.000422/2.66, allocations: 0.636 MB / 0.9815 GB, free: 1.516 MB / 0.8106 GB
Notification: Performance of collectInitialBindings (initialization): time 0.0003689/2.661, allocations: 493.1 kB / 0.9819 GB, free: 1.039 MB / 0.8106 GB
Notification: Performance of simplifyInitialFunctions (initialization): time 0.0003869/2.661, allocations: 306.5 kB / 0.9822 GB, free: 0.7305 MB / 0.8106 GB
Notification: Performance of setup shared object (initialization): time 0.0001336/2.661, allocations: 357.9 kB / 0.9826 GB, free: 384 kB / 0.8106 GB
Notification: Performance of preBalanceInitialSystem (initialization): time 0.0007422/2.662, allocations: 383.1 kB / 0.9829 GB, free: 0 / 0.8106 GB
Notification: Performance of partitionIndependentBlocks (initialization): time 0.001213/2.663, allocations: 1.067 MB / 0.984 GB, free: 14.62 MB / 0.8262 GB
Notification: Performance of analyzeInitialSystem (initialization): time 0.00213/2.665, allocations: 1.613 MB / 0.9856 GB, free: 12.79 MB / 0.8262 GB
Notification: Performance of solveInitialSystemEqSystem (initialization): time 1.599e-05/2.666, allocations: 12 kB / 0.9856 GB, free: 12.77 MB / 0.8262 GB
Notification: Performance of matching and sorting (n=253) (initialization): time 0.003145/2.669, allocations: 1.802 MB / 0.9873 GB, free: 11.08 MB / 0.8262 GB
Notification: Performance of prepare postOptimizeDAE: time 2.772e-05/2.669, allocations: 12 kB / 0.9873 GB, free: 11.07 MB / 0.8262 GB
Notification: Performance of postOpt simplifyComplexFunction (initialization): time 3.316e-05/2.669, allocations: 26.38 kB / 0.9874 GB, free: 11.04 MB / 0.8262 GB
Notification: Performance of postOpt tearingSystem (initialization): time 0.004458/2.673, allocations: 1.293 MB / 0.9886 GB, free: 9.754 MB / 0.8262 GB
Notification: Performance of postOpt solveSimpleEquations (initialization): time 0.0004923/2.674, allocations: 163.6 kB / 0.9888 GB, free: 9.594 MB / 0.8262 GB
Notification: Performance of postOpt calculateStrongComponentJacobians (initialization): time 0.002036/2.676, allocations: 1.305 MB / 0.9901 GB, free: 8.262 MB / 0.8262 GB
Notification: Performance of postOpt simplifyAllExpressions (initialization): time 0.001102/2.677, allocations: 205.7 kB / 0.9903 GB, free: 8.059 MB / 0.8262 GB
Notification: Performance of postOpt collapseArrayExpressions (initialization): time 0.0001584/2.677, allocations: 75.98 kB / 0.9903 GB, free: 7.984 MB / 0.8262 GB
Notification: Model statistics after passing the back-end for initialization:
 * Number of independent subsystems: 103
 * Number of states: 0 ()
 * Number of discrete variables: 60 (staticVolume2.Ce4.a,staticVolume2.Ce8.a,staticVolume2.Cs.b,staticVolume2.Ce1.a,staticVolume2.Ce2.a,staticVolume2.Ce3.a,staticVolume2.Ce7.a,staticVolume2.Ce6.a,staticVolume2.Ce5.a,staticVolume1.Ce4.a,staticVolume1.Ce8.a,staticVolume1.Cs.b,staticVolume1.Ce1.a,staticVolume1.Ce2.a,staticVolume1.Ce3.a,staticVolume1.Ce7.a,staticVolume1.Ce6.a,staticVolume1.Ce5.a,staticVolume.Ce4.a,staticVolume.Ce8.a,staticVolume.Cs.b,staticVolume.Ce1.a,staticVolume.Ce2.a,staticVolume.Ce3.a,staticVolume.Ce7.a,staticVolume.Ce6.a,staticVolume.Ce5.a,pipe2.C2.b,pipe2.C1.a,pipe1.C2.b,pipe1.C1.a,puitsP2.C.a,valve3.C2.b,valve3.C1.a,valve2.C2.b,valve2.C1.a,valve1.C2.b,valve1.C1.a,sourceP1.C.b,sourceP.C.b,staticVolume2.Ce8.b,staticVolume2.Ce7.b,staticVolume2.Ce6.b,staticVolume2.Ce5.b,staticVolume2.Ce3.b,staticVolume2.Ce2.b,staticVolume2.Ce1.b,staticVolume1.Ce7.b,staticVolume1.Ce6.b,staticVolume1.Ce5.b,staticVolume1.Ce4.b,staticVolume1.Ce3.b,staticVolume1.Ce2.b,staticVolume.Ce8.b,staticVolume.Ce7.b,staticVolume.Ce6.b,staticVolume.Ce5.b,staticVolume.Ce3.b,staticVolume.Ce2.b,staticVolume.Ce1.b)
 * Number of discrete states: 0 ()
 * Number of clocked states: 0 ()
 * Top-level inputs: 0
Notification: Strong component statistics for initialization (124):
 * Single equations (assignments): 117
 * Array equations: 0
 * Algorithm blocks: 0
 * Record equations: 6
 * 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
   {(13,18)}
Notification: Performance of prepare postOptimizeDAE: time 0.000567/2.678, allocations: 342.7 kB / 0.9907 GB, free: 7.641 MB / 0.8262 GB
Notification: Performance of postOpt lateInlineFunction (simulation): time 0.0002375/2.678, allocations: 110.5 kB / 0.9908 GB, free: 7.531 MB / 0.8262 GB
Notification: Performance of postOpt wrapFunctionCalls (simulation): time 0.004574/2.682, allocations: 4.049 MB / 0.9947 GB, free: 3.379 MB / 0.8262 GB
Notification: Performance of postOpt simplifysemiLinear (simulation): time 1.341e-05/2.683, allocations: 11.92 kB / 0.9947 GB, free: 3.367 MB / 0.8262 GB
Notification: Performance of postOpt simplifyComplexFunction (simulation): time 5.09e-06/2.683, allocations: 3.984 kB / 0.9947 GB, free: 3.363 MB / 0.8262 GB
Notification: Performance of postOpt removeConstants (simulation): time 0.0004986/2.683, allocations: 275.5 kB / 0.995 GB, free: 3.074 MB / 0.8262 GB
Notification: Performance of postOpt simplifyTimeIndepFuncCalls (simulation): time 0.0001776/2.683, allocations: 23.78 kB / 0.995 GB, free: 3.051 MB / 0.8262 GB
Notification: Performance of postOpt simplifyAllExpressions (simulation): time 0.0004751/2.684, allocations: 27.97 kB / 0.995 GB, free: 3.023 MB / 0.8262 GB
Notification: Performance of postOpt findZeroCrossings (simulation): time 0.0001196/2.684, allocations: 44.5 kB / 0.9951 GB, free: 2.98 MB / 0.8262 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(valve2.T, valve2.rho, valve2.pro.u, valve2.pro.s, valve2.pro.cp, valve2.pro.ddhp, valve2.pro.ddph, valve2.pro.duph, valve2.pro.duhp, valve2.pro.x) = $cse4

Variables:
1: valve2.pro.ddph:VARIABLE(unit = "s2/m2" )  "Derivative of density wrt. pressure at constant specific enthalpy" type: Real
2: valve2.pro.duhp:VARIABLE(unit = "1" )  "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real
3: valve2.pro.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific entropy" type: Real
4: valve2.pro.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific heat capacity at constant presure" type: Real
5: valve2.pro.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 )  "Specific inner energy" type: Real
6: $cse4.duph:VARIABLE(protected = true )  type: Real unreplaceable
7: $cse4.ddhp:VARIABLE(protected = true )  type: Real unreplaceable
8: $cse4.duhp:VARIABLE(protected = true )  type: Real unreplaceable
9: $cse4.cp:VARIABLE(protected = true )  type: Real unreplaceable
10: $cse4.ddph: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): valve1.deltaP = staticVolume.P - staticVolume1.P
2/2 (1): valve1.deltaP * valve1.Cv * abs(valve1.Cv) = 1.733e12 * $cse1 / valve1.rho ^ 2.0
3/3 (10): $cse2 = ThermoSysPro.Properties.Fluid.Ph(valve1.Pm, valve1.h, valve1.mode, valve1.fluid)
4/13 (10): ThermoSysPro.Properties.WaterSteam.Common.ThermoProperties_ph(valve1.T, valve1.rho, valve1.pro.u, valve1.pro.s, valve1.pro.cp, valve1.pro.ddhp, valve1.pro.ddph, valve1.pro.duph, valve1.pro.duhp, valve1.pro.x) = $cse2
5/23 (1): valve1.Pm = 0.5 * (staticVolume.P + staticVolume1.P)
6/24 (1): pipe1.Pm = 0.5 * (sourceP.P0 + staticVolume.P)
7/25 (10): $cse8 = ThermoSysPro.Properties.Fluid.Ph(pipe1.Pm, pipe1.h, pipe1.mode, pipe1.fluid)
8/35 (10): ThermoSysPro.Properties.WaterSteam.Common.ThermoProperties_ph(pipe1.T, pipe1.rho, pipe1.pro.u, pipe1.pro.s, pipe1.pro.cp, pipe1.pro.ddhp, pipe1.pro.ddph, pipe1.pro.duph, pipe1.pro.duhp, pipe1.pro.x) = $cse8
9/45 (1): pipe1.deltaPf = 0.5 * pipe1.khi * $cse7 / (pipe1.A ^ 2.0 * pipe1.rho)
10/46 (1): $cse7 = ThermoSysPro.Functions.ThermoSquare(pipe1.Q, pipe1.eps)
11/47 (1): $cse1 = ThermoSysPro.Functions.ThermoSquare(pipe1.Q, valve1.eps)
12/48 (1): 0.0 = pipe1.Q * valve1.h + pipe2.Q * valve2.h - valve3.Q * valve3.h
13/49 (10): $cse6 = ThermoSysPro.Properties.Fluid.Ph(valve3.Pm, valve3.h, valve3.mode, valve3.fluid)
14/59 (10): ThermoSysPro.Properties.WaterSteam.Common.ThermoProperties_ph(valve3.T, valve3.rho, valve3.pro.u, valve3.pro.s, valve3.pro.cp, valve3.pro.ddhp, valve3.pro.ddph, valve3.pro.duph, valve3.pro.duhp, valve3.pro.x) = $cse6
15/69 (1): valve3.deltaP * valve3.Cv * abs(valve3.Cv) = 1.733e12 * $cse5 / valve3.rho ^ 2.0
16/70 (1): valve3.deltaP = staticVolume1.P - puitsP2.P0
17/71 (1): valve3.Pm = 0.5 * (staticVolume1.P + puitsP2.P0)
18/72 (1): valve2.Pm = 0.5 * (staticVolume2.P + staticVolume1.P)
19/73 (1): pipe2.Pm = 0.5 * (sourceP1.P0 + staticVolume2.P)
20/74 (10): $cse10 = ThermoSysPro.Properties.Fluid.Ph(pipe2.Pm, pipe2.h, pipe2.mode, pipe2.fluid)
21/84 (10): ThermoSysPro.Properties.WaterSteam.Common.ThermoProperties_ph(pipe2.T, pipe2.rho, pipe2.pro.u, pipe2.pro.s, pipe2.pro.cp, pipe2.pro.ddhp, pipe2.pro.ddph, pipe2.pro.duph, pipe2.pro.duhp, pipe2.pro.x) = $cse10
22/94 (1): pipe2.deltaPf = 0.5 * pipe2.khi * $cse9 / (pipe2.A ^ 2.0 * pipe2.rho)
23/95 (1): $cse9 = ThermoSysPro.Functions.ThermoSquare(pipe2.Q, pipe2.eps)
24/96 (1): $cse3 = ThermoSysPro.Functions.ThermoSquare(pipe2.Q, valve2.eps)
25/97 (1): valve2.deltaP * valve2.Cv * abs(valve2.Cv) = 1.733e12 * $cse3 / valve2.rho ^ 2.0
26/98 (10): $cse4 = ThermoSysPro.Properties.Fluid.Ph(valve2.Pm, valve2.h, valve2.mode, valve2.fluid)
27/108 (10): ThermoSysPro.Properties.WaterSteam.Common.ThermoProperties_ph(valve2.T, valve2.rho, valve2.pro.u, valve2.pro.s, valve2.pro.cp, valve2.pro.ddhp, valve2.pro.ddph, valve2.pro.duph, valve2.pro.duhp, valve2.pro.x) = $cse4
28/118 (1): 0.0 = pipe2.Q * (pipe2.h - valve2.h)
29/119 (1): 0.0 = if pipe2.Q > 0.0 then valve2.h - staticVolume2.h else valve2.h - staticVolume1.h
30/120 (1): 0.0 = if pipe2.Q > 0.0 then pipe2.h - sourceP1.h else pipe2.h - staticVolume2.h
31/121 (1): 0.0 = pipe1.Q + pipe2.Q - valve3.Q
32/122 (1): $cse5 = ThermoSysPro.Functions.ThermoSquare(valve3.Q, valve3.eps)
33/123 (1): 0.0 = if valve3.Q > 0.0 then valve3.h - staticVolume1.h else valve3.h - puitsP2.h
34/124 (1): 0.0 = if pipe1.Q > 0.0 then valve1.h - staticVolume.h else valve1.h - staticVolume1.h
35/125 (1): 0.0 = pipe1.Q * (pipe1.h - valve1.h)
36/126 (1): 0.0 = if pipe1.Q > 0.0 then pipe1.h - sourceP.h else pipe1.h - staticVolume.h
37/127 (1): pipe2.deltaP = pipe2.deltaPf + 9.80665 * pipe2.rho * (pipe2.z2 - pipe2.z1)
38/128 (1): sourceP1.P0 - staticVolume2.P = pipe2.deltaP
39/129 (1): valve2.deltaP = staticVolume2.P - staticVolume1.P
40/130 (1): pipe1.deltaP = pipe1.deltaPf + 9.80665 * pipe1.rho * (pipe1.z2 - pipe1.z1)
41/131 (1): sourceP.P0 - staticVolume.P = pipe1.deltaP

Variables:
1: pipe1.deltaP:VARIABLE(unit = "Pa" )  "Total pressure loss" type: Real
2: pipe1.deltaPf:VARIABLE(unit = "Pa" )  "Friction pressure loss" type: Real
3: valve2.deltaP:VARIABLE(unit = "Pa" )  "Singular pressure loss" type: Real
4: pipe2.deltaP:VARIABLE(unit = "Pa" )  "Total pressure loss" type: Real
5: pipe2.deltaPf:VARIABLE(unit = "Pa" )  "Friction pressure loss" type: Real
6: staticVolume.h:VARIABLE(start = 1e6 unit = "J/kg" )  "Fluid specific enthalpy" type: Real
7: pipe1.h:VARIABLE(start = 1e5 unit = "J/kg" )  "Fluid specific enthalpy" type: Real
8: valve1.h:VARIABLE(start = 1e5 unit = "J/kg" )  "Fluid specific enthalpy" type: Real
9: staticVolume1.h:VARIABLE(start = 1e6 unit = "J/kg" )  "Fluid specific enthalpy" type: Real
10: $cse5:VARIABLE(protected = true )  type: Real unreplaceable
11: valve3.Q:VARIABLE(start = 804.6933031325926 unit = "kg/s" )  "Mass flow rate" type: Real
12: pipe2.h:VARIABLE(start = 1e5 unit = "J/kg" )  "Fluid specific enthalpy" type: Real
13: staticVolume2.h:VARIABLE(start = 1e6 unit = "J/kg" )  "Fluid specific enthalpy" type: Real
14: valve2.h:VARIABLE(start = 1e5 unit = "J/kg" )  "Fluid specific enthalpy" type: Real
15: valve2.pro.ddph:VARIABLE(unit = "s2/m2" )  "Derivative of density wrt. pressure at constant specific enthalpy" type: Real
16: valve2.pro.duhp:VARIABLE(unit = "1" )  "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real
17: valve2.pro.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific entropy" type: Real
18: valve2.pro.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific heat capacity at constant presure" type: Real
19: valve2.pro.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 )  "Specific inner energy" type: Real
20: $cse4.duph:VARIABLE(protected = true )  type: Real unreplaceable
21: $cse4.ddhp:VARIABLE(protected = true )  type: Real unreplaceable
22: $cse4.duhp:VARIABLE(protected = true )  type: Real unreplaceable
23: $cse4.cp:VARIABLE(protected = true )  type: Real unreplaceable
24: $cse4.ddph:VARIABLE(protected = true )  type: Real unreplaceable
25: $cse4.d:VARIABLE(protected = true )  type: Real unreplaceable
26: valve2.Pm:VARIABLE(min = 0.0 start = 118970.64778985853 unit = "Pa" nominal = 1e5 )  "Fluid average pressure" type: Real
27: $cse4.u:VARIABLE(protected = true )  type: Real unreplaceable
28: $cse4.T:VARIABLE(protected = true )  type: Real unreplaceable
29: $cse4.x:VARIABLE(protected = true )  type: Real unreplaceable
30: $cse4.s:VARIABLE(protected = true )  type: Real unreplaceable
31: valve2.pro.ddhp:VARIABLE(unit = "kg.s2/m5" )  "Derivative of density wrt. specific enthalpy at constant pressure" type: Real
32: valve2.T:VARIABLE(min = 200.0 max = 6000.0 start = 290.0 unit = "K" nominal = 300.0 )  "Fluid temperature" type: Real
33: valve2.pro.x:VARIABLE(min = 0.0 max = 1.0 unit = "1" )  "Vapor mass fraction" type: Real
34: valve2.pro.duph:VARIABLE(unit = "m3/kg" )  "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real
35: valve2.rho:VARIABLE(min = 1e-9 max = 1e5 start = 998.0 unit = "kg/m3" nominal = 998.0 )  "Fluid density" type: Real
36: $cse3:VARIABLE(protected = true )  type: Real unreplaceable
37: pipe2.Q:VARIABLE(start = 100.0 unit = "kg/s" )  "Mass flow rate" type: Real
38: $cse9:VARIABLE(protected = true )  type: Real unreplaceable
39: pipe2.pro.ddhp:VARIABLE(unit = "kg.s2/m5" )  "Derivative of density wrt. specific enthalpy at constant pressure" type: Real
40: pipe2.pro.x:VARIABLE(min = 0.0 max = 1.0 unit = "1" )  "Vapor mass fraction" type: Real
41: pipe2.pro.ddph:VARIABLE(unit = "s2/m2" )  "Derivative of density wrt. pressure at constant specific enthalpy" type: Real
42: pipe2.rho:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 )  "Fluid density" type: Real
43: pipe2.pro.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific heat capacity at constant presure" type: Real
44: pipe2.pro.duhp:VARIABLE(unit = "1" )  "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real
45: pipe2.T:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 300.0 )  "Fluid temperature" type: Real
46: pipe2.pro.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific entropy" type: Real
47: pipe2.pro.duph:VARIABLE(unit = "m3/kg" )  "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real
48: pipe2.pro.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 )  "Specific inner energy" type: Real
49: $cse10.ddhp:VARIABLE(protected = true )  type: Real unreplaceable
50: $cse10.x:VARIABLE(protected = true )  type: Real unreplaceable
51: $cse10.d:VARIABLE(protected = true )  type: Real unreplaceable
52: $cse10.u:VARIABLE(protected = true )  type: Real unreplaceable
53: $cse10.duhp:VARIABLE(protected = true )  type: Real unreplaceable
54: $cse10.ddph:VARIABLE(protected = true )  type: Real unreplaceable
55: $cse10.cp:VARIABLE(protected = true )  type: Real unreplaceable
56: $cse10.s:VARIABLE(protected = true )  type: Real unreplaceable
57: $cse10.duph:VARIABLE(protected = true )  type: Real unreplaceable
58: $cse10.T:VARIABLE(protected = true )  type: Real unreplaceable
59: pipe2.Pm:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 )  "Fluid average pressure" type: Real
60: staticVolume2.P:VARIABLE(min = 0.0 start = 1e6 unit = "Pa" nominal = 1e5 )  "Fluid pressure" type: Real
61: valve3.Pm:VARIABLE(min = 0.0 start = 108776.21727782265 unit = "Pa" nominal = 1e5 )  "Fluid average pressure" type: Real
62: staticVolume1.P:VARIABLE(min = 0.0 start = 1e6 unit = "Pa" nominal = 1e5 )  "Fluid pressure" type: Real
63: valve3.deltaP:VARIABLE(unit = "Pa" )  "Singular pressure loss" type: Real
64: valve3.pro.duph:VARIABLE(unit = "m3/kg" )  "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real
65: valve3.pro.duhp:VARIABLE(unit = "1" )  "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real
66: valve3.pro.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific heat capacity at constant presure" type: Real
67: valve3.pro.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific entropy" type: Real
68: valve3.pro.x:VARIABLE(min = 0.0 max = 1.0 unit = "1" )  "Vapor mass fraction" type: Real
69: valve3.rho:VARIABLE(min = 1e-9 max = 1e5 start = 998.0 unit = "kg/m3" nominal = 998.0 )  "Fluid density" type: Real
70: valve3.pro.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 )  "Specific inner energy" type: Real
71: valve3.pro.ddhp:VARIABLE(unit = "kg.s2/m5" )  "Derivative of density wrt. specific enthalpy at constant pressure" type: Real
72: valve3.pro.ddph:VARIABLE(unit = "s2/m2" )  "Derivative of density wrt. pressure at constant specific enthalpy" type: Real
73: valve3.T:VARIABLE(min = 200.0 max = 6000.0 start = 290.0 unit = "K" nominal = 300.0 )  "Fluid temperature" type: Real
74: $cse6.d:VARIABLE(protected = true )  type: Real unreplaceable
75: $cse6.T:VARIABLE(protected = true )  type: Real unreplaceable
76: $cse6.ddph:VARIABLE(protected = true )  type: Real unreplaceable
77: $cse6.x:VARIABLE(protected = true )  type: Real unreplaceable
78: $cse6.u:VARIABLE(protected = true )  type: Real unreplaceable
79: $cse6.cp:VARIABLE(protected = true )  type: Real unreplaceable
80: $cse6.duph:VARIABLE(protected = true )  type: Real unreplaceable
81: $cse6.duhp:VARIABLE(protected = true )  type: Real unreplaceable
82: $cse6.s:VARIABLE(protected = true )  type: Real unreplaceable
83: $cse6.ddhp:VARIABLE(protected = true )  type: Real unreplaceable
84: valve3.h:VARIABLE(start = 1e5 unit = "J/kg" )  "Fluid specific enthalpy" type: Real
85: $cse1:VARIABLE(protected = true )  type: Real unreplaceable
86: pipe1.Q:VARIABLE(start = 100.0 unit = "kg/s" )  "Mass flow rate" type: Real
87: $cse7:VARIABLE(protected = true )  type: Real unreplaceable
88: pipe1.pro.ddhp:VARIABLE(unit = "kg.s2/m5" )  "Derivative of density wrt. specific enthalpy at constant pressure" type: Real
89: pipe1.pro.x:VARIABLE(min = 0.0 max = 1.0 unit = "1" )  "Vapor mass fraction" type: Real
90: pipe1.pro.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific heat capacity at constant presure" type: Real
91: pipe1.pro.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 )  "Specific inner energy" type: Real
92: pipe1.rho:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 )  "Fluid density" type: Real
93: pipe1.pro.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific entropy" type: Real
94: pipe1.T:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 300.0 )  "Fluid temperature" type: Real
95: pipe1.pro.ddph:VARIABLE(unit = "s2/m2" )  "Derivative of density wrt. pressure at constant specific enthalpy" type: Real
96: pipe1.pro.duhp:VARIABLE(unit = "1" )  "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real
97: pipe1.pro.duph:VARIABLE(unit = "m3/kg" )  "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real
98: $cse8.duhp:VARIABLE(protected = true )  type: Real unreplaceable
99: $cse8.ddph:VARIABLE(protected = true )  type: Real unreplaceable
100: $cse8.d:VARIABLE(protected = true )  type: Real unreplaceable
101: $cse8.duph:VARIABLE(protected = true )  type: Real unreplaceable
102: $cse8.s:VARIABLE(protected = true )  type: Real unreplaceable
103: $cse8.ddhp:VARIABLE(protected = true )  type: Real unreplaceable
104: $cse8.cp:VARIABLE(protected = true )  type: Real unreplaceable
105: $cse8.x:VARIABLE(protected = true )  type: Real unreplaceable
106: $cse8.u:VARIABLE(protected = true )  type: Real unreplaceable
107: $cse8.T:VARIABLE(protected = true )  type: Real unreplaceable
108: pipe1.Pm:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 )  "Fluid average pressure" type: Real
109: staticVolume.P:VARIABLE(min = 0.0 start = 1e6 unit = "Pa" nominal = 1e5 )  "Fluid pressure" type: Real
110: valve1.pro.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 )  "Specific inner energy" type: Real
111: valve1.pro.ddhp:VARIABLE(unit = "kg.s2/m5" )  "Derivative of density wrt. specific enthalpy at constant pressure" type: Real
112: valve1.pro.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific heat capacity at constant presure" type: Real
113: valve1.pro.ddph:VARIABLE(unit = "s2/m2" )  "Derivative of density wrt. pressure at constant specific enthalpy" type: Real
114: valve1.T:VARIABLE(min = 200.0 max = 6000.0 start = 290.0 unit = "K" nominal = 300.0 )  "Fluid temperature" type: Real
115: valve1.pro.duhp:VARIABLE(unit = "1" )  "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real
116: valve1.pro.x:VARIABLE(min = 0.0 max = 1.0 unit = "1" )  "Vapor mass fraction" type: Real
117: $cse2.ddhp:VARIABLE(protected = true )  type: Real unreplaceable
118: valve1.Pm:VARIABLE(min = 0.0 start = 120690.8728732298 unit = "Pa" nominal = 1e5 )  "Fluid average pressure" type: Real
119: $cse2.duph:VARIABLE(protected = true )  type: Real unreplaceable
120: $cse2.duhp:VARIABLE(protected = true )  type: Real unreplaceable
121: $cse2.u:VARIABLE(protected = true )  type: Real unreplaceable
122: $cse2.cp:VARIABLE(protected = true )  type: Real unreplaceable
123: $cse2.x:VARIABLE(protected = true )  type: Real unreplaceable
124: $cse2.T:VARIABLE(protected = true )  type: Real unreplaceable
125: $cse2.s:VARIABLE(protected = true )  type: Real unreplaceable
126: $cse2.d:VARIABLE(protected = true )  type: Real unreplaceable
127: $cse2.ddph:VARIABLE(protected = true )  type: Real unreplaceable
128: valve1.pro.duph:VARIABLE(unit = "m3/kg" )  "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real
129: valve1.pro.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific entropy" type: Real
130: valve1.rho:VARIABLE(min = 1e-9 max = 1e5 start = 998.0 unit = "kg/m3" nominal = 998.0 )  "Fluid density" type: Real
131: valve1.deltaP:VARIABLE(unit = "Pa" )  "Singular pressure loss" 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 0.004462/2.688, allocations: 4.925 MB / 0.9999 GB, free: 13.23 MB / 0.8419 GB
Error: post-optimization module createDAEmodeBDAE (simulation) failed.
Error: Internal error SimCode DAEmode: The model ThermoSysPro.Examples.SimpleExamples.TestJunctions3 could not be translated