Running: ./testmodel.py --libraries=/home/hudson/saved_omc/libraries/.openmodelica/libraries --ompython_omhome=/usr ThermoSysPro_ThermoSysPro.Properties.WaterSteamSimple.Validation.Bench.Test1_IF97.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.Properties.WaterSteamSimple.Validation.Bench.Test1_IF97,tolerance=1e-06,outputFormat="empty",numberOfIntervals=5000,variableFilter="",fileNamePrefix="ThermoSysPro_ThermoSysPro.Properties.WaterSteamSimple.Validation.Bench.Test1_IF97") translateModel(ThermoSysPro.Properties.WaterSteamSimple.Validation.Bench.Test1_IF97,tolerance=1e-06,outputFormat="empty",numberOfIntervals=5000,variableFilter="",fileNamePrefix="ThermoSysPro_ThermoSysPro.Properties.WaterSteamSimple.Validation.Bench.Test1_IF97") Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermoSysPro 4.0.0-master/package.mo): time 0.8419/0.8419, allocations: 150.9 MB / 167.2 MB, free: 14.52 MB / 142.1 MB Notification: Performance of FrontEnd - loaded program: time 0.000349/0.0003491, allocations: 16.88 kB / 237.8 MB, free: 1.816 MB / 190.1 MB Notification: Performance of FrontEnd - Absyn->SCode: time 0.05343/0.0538, allocations: 31.34 MB / 269.1 MB, free: 7.062 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.Properties.WaterSteamSimple.Validation.Bench.Test1_IF97): time 1.636/1.69, allocations: 297.9 MB / 0.5537 GB, free: 9.93 MB / 446.1 MB Notification: Performance of NFInst.instExpressions: time 0.4963/2.187, allocations: 187.3 MB / 0.7365 GB, free: 15.83 MB / 0.6075 GB Notification: Performance of NFInst.updateImplicitVariability: time 0.0007322/2.187, allocations: 10.22 kB / 0.7365 GB, free: 15.82 MB / 0.6075 GB [/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/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/Machines/StaticCentrifugalPump.mo:60:3-62:42: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/Machines/StaticCentrifugalPump.mo:63:3-65:37: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/Machines/StaticCentrifugalPump.mo:60:3-62:42: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/Machines/StaticCentrifugalPump.mo:63:3-65:37: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/Volumes/VolumeD.mo:29:3-31:42:writable] Warning: Connector Ce 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/VolumeD.mo:32:3-34:37: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/VolumeD.mo:35:3-37:43:writable] Warning: Connector Cs2 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/VolumeD.mo:38:3-40:37:writable] Warning: Connector Cs3 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/IdealCheckValve.mo:22:3-23:46: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/IdealCheckValve.mo:24:3-25:48: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/IdealCheckValve.mo:22:3-23:46: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/IdealCheckValve.mo:24:3-25:48: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/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/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). Notification: Performance of NFTyping.typeComponents: time 0.0008084/2.188, allocations: 257.1 kB / 0.7368 GB, free: 15.82 MB / 0.6075 GB Notification: Performance of NFTyping.typeBindings: time 0.001093/2.189, allocations: 429.7 kB / 0.7372 GB, free: 15.82 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 0.02786/2.217, allocations: 11.74 MB / 0.7487 GB, free: 15.58 MB / 0.6075 GB Notification: Performance of NFFlatten.flatten: time 0.001597/2.219, allocations: 1.459 MB / 0.7501 GB, free: 15.58 MB / 0.6075 GB Notification: Performance of NFFlatten.resolveConnections: time 0.0005685/2.219, allocations: 0.5495 MB / 0.7506 GB, free: 15.5 MB / 0.6075 GB Notification: Performance of NFEvalConstants.evaluate: time 0.0006512/2.22, allocations: 0.5553 MB / 0.7512 GB, free: 15.5 MB / 0.6075 GB Notification: Performance of NFSimplifyModel.simplify: time 0.0004972/2.221, allocations: 0.5377 MB / 0.7517 GB, free: 15.5 MB / 0.6075 GB Notification: Performance of NFPackage.collectConstants: time 0.0001215/2.221, allocations: 95.66 kB / 0.7518 GB, free: 15.5 MB / 0.6075 GB Notification: Performance of NFFlatten.collectFunctions: time 0.0329/2.254, allocations: 20.13 MB / 0.7714 GB, free: 12.48 MB / 0.6075 GB Notification: Performance of NFScalarize.scalarize: time 0.0004037/2.254, allocations: 230 kB / 0.7717 GB, free: 12.44 MB / 0.6075 GB Notification: Performance of NFVerifyModel.verify: time 0.0008986/2.255, allocations: 0.5857 MB / 0.7722 GB, free: 12.4 MB / 0.6075 GB Notification: Performance of NFConvertDAE.convert: time 0.02167/2.277, allocations: 10.59 MB / 0.7826 GB, free: 8.488 MB / 0.6075 GB Notification: Performance of FrontEnd - DAE generated: time 5.972e-06/2.277, allocations: 1.203 kB / 0.7826 GB, free: 8.488 MB / 0.6075 GB Notification: Performance of FrontEnd: time 2.154e-06/2.277, allocations: 0 / 0.7826 GB, free: 8.488 MB / 0.6075 GB Notification: Performance of Transformations before backend: time 1.369e-05/2.277, allocations: 2.156 kB / 0.7826 GB, free: 8.488 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: 301 * Number of variables: 301 Notification: Performance of Generate backend data structure: time 0.007249/2.284, allocations: 2.523 MB / 0.785 GB, free: 6.969 MB / 0.6075 GB Notification: Performance of prepare preOptimizeDAE: time 3.591e-05/2.284, allocations: 11.06 kB / 0.7851 GB, free: 6.969 MB / 0.6075 GB Notification: Performance of preOpt normalInlineFunction (simulation): time 0.0001844/2.284, allocations: 133.2 kB / 0.7852 GB, free: 6.898 MB / 0.6075 GB Notification: Performance of preOpt evaluateParameters (simulation): time 0.0005543/2.285, allocations: 0.494 MB / 0.7857 GB, free: 6.551 MB / 0.6075 GB Notification: Performance of preOpt simplifyIfEquations (simulation): time 9.016e-05/2.285, allocations: 124.2 kB / 0.7858 GB, free: 6.484 MB / 0.6075 GB Notification: Performance of preOpt expandDerOperator (simulation): time 0.0001048/2.285, allocations: 91.19 kB / 0.7859 GB, free: 6.48 MB / 0.6075 GB Notification: Performance of preOpt clockPartitioning (simulation): time 0.001654/2.287, allocations: 1.196 MB / 0.787 GB, free: 5.977 MB / 0.6075 GB Notification: Performance of preOpt findStateOrder (simulation): time 2.297e-05/2.287, allocations: 5.906 kB / 0.787 GB, free: 5.977 MB / 0.6075 GB Notification: Performance of preOpt replaceEdgeChange (simulation): time 7.19e-05/2.287, allocations: 47.16 kB / 0.7871 GB, free: 5.973 MB / 0.6075 GB Notification: Performance of preOpt inlineArrayEqn (simulation): time 3.373e-05/2.287, allocations: 45.06 kB / 0.7871 GB, free: 5.965 MB / 0.6075 GB Notification: Performance of preOpt removeEqualRHS (simulation): time 0.001321/2.288, allocations: 0.8071 MB / 0.7879 GB, free: 5.859 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 0.02435/2.312, allocations: 15.44 MB / 0.803 GB, free: 9.438 MB / 0.6231 GB Notification: Performance of preOpt comSubExp (simulation): time 0.001559/2.314, allocations: 0.7478 MB / 0.8037 GB, free: 9 MB / 0.6231 GB Notification: Performance of preOpt resolveLoops (simulation): time 0.0008652/2.315, allocations: 490.6 kB / 0.8042 GB, free: 8.711 MB / 0.6231 GB Notification: Performance of preOpt evalFunc (simulation): time 0.3319/2.647, allocations: 151.4 MB / 0.952 GB, free: 0.8164 MB / 0.7794 GB Notification: Performance of preOpt encapsulateWhenConditions (simulation): time 0.00119/2.648, allocations: 0.5168 MB / 0.9525 GB, free: 292 kB / 0.7794 GB Notification: Performance of pre-optimization done (n=141): time 3.877e-06/2.648, allocations: 0 / 0.9525 GB, free: 292 kB / 0.7794 GB Notification: Performance of matching and sorting (n=141): time 0.02242/2.67, allocations: 4.316 MB / 0.9567 GB, free: 11.95 MB / 0.795 GB Notification: Performance of inlineWhenForInitialization (initialization): time 8.088e-05/2.671, allocations: 137.1 kB / 0.9569 GB, free: 11.79 MB / 0.795 GB Notification: Performance of selectInitializationVariablesDAE (initialization): time 0.0008182/2.671, allocations: 0.5857 MB / 0.9574 GB, free: 11.2 MB / 0.795 GB Notification: Performance of collectPreVariables (initialization): time 9.7e-05/2.672, allocations: 37.7 kB / 0.9575 GB, free: 11.16 MB / 0.795 GB Notification: Performance of collectInitialEqns (initialization): time 0.0003562/2.672, allocations: 419 kB / 0.9579 GB, free: 10.75 MB / 0.795 GB Notification: Performance of collectInitialBindings (initialization): time 0.0004121/2.672, allocations: 461.5 kB / 0.9583 GB, free: 10.3 MB / 0.795 GB Notification: Performance of simplifyInitialFunctions (initialization): time 0.0003534/2.673, allocations: 215.6 kB / 0.9585 GB, free: 10.08 MB / 0.795 GB Notification: Performance of setup shared object (initialization): time 0.0001441/2.673, allocations: 357.9 kB / 0.9589 GB, free: 9.727 MB / 0.795 GB Notification: Performance of preBalanceInitialSystem (initialization): time 0.0007201/2.674, allocations: 326.9 kB / 0.9592 GB, free: 9.406 MB / 0.795 GB Notification: Performance of partitionIndependentBlocks (initialization): time 0.0009316/2.674, allocations: 0.6323 MB / 0.9598 GB, free: 8.664 MB / 0.795 GB Notification: Performance of analyzeInitialSystem (initialization): time 0.001742/2.676, allocations: 1.033 MB / 0.9608 GB, free: 7.551 MB / 0.795 GB Notification: Performance of solveInitialSystemEqSystem (initialization): time 9.047e-06/2.676, allocations: 4 kB / 0.9608 GB, free: 7.547 MB / 0.795 GB Notification: Performance of matching and sorting (n=186) (initialization): time 0.002769/2.679, allocations: 1.443 MB / 0.9622 GB, free: 6.141 MB / 0.795 GB Notification: Performance of prepare postOptimizeDAE: time 2.325e-05/2.679, allocations: 9.562 kB / 0.9622 GB, free: 6.133 MB / 0.795 GB Notification: Performance of postOpt simplifyComplexFunction (initialization): time 1.536e-05/2.679, allocations: 12 kB / 0.9622 GB, free: 6.121 MB / 0.795 GB Notification: Performance of postOpt tearingSystem (initialization): time 0.003797/2.683, allocations: 1.439 MB / 0.9636 GB, free: 4.684 MB / 0.795 GB Notification: Performance of postOpt solveSimpleEquations (initialization): time 0.0002747/2.683, allocations: 70.19 kB / 0.9637 GB, free: 4.625 MB / 0.795 GB Notification: Performance of postOpt calculateStrongComponentJacobians (initialization): time 0.002798/2.686, allocations: 1.651 MB / 0.9653 GB, free: 2.957 MB / 0.795 GB Notification: Performance of postOpt simplifyAllExpressions (initialization): time 0.000764/2.687, allocations: 130.6 kB / 0.9654 GB, free: 2.828 MB / 0.795 GB Notification: Performance of postOpt collapseArrayExpressions (initialization): time 8.003e-05/2.687, allocations: 43.98 kB / 0.9655 GB, free: 2.785 MB / 0.795 GB Notification: Model statistics after passing the back-end for initialization: * Number of independent subsystems: 37 * Number of states: 0 () * Number of discrete variables: 40 ($PRE.idealCheckValve2.touvert,$whenCondition4,$PRE.idealCheckValve2.tferme,$whenCondition3,$PRE.idealCheckValve1.touvert,$whenCondition2,$PRE.idealCheckValve1.tferme,$whenCondition1,idealCheckValve2.tferme,idealCheckValve2.touvert,idealCheckValve2.ouvert,$PRE.idealCheckValve2.ouvert,idealCheckValve1.tferme,idealCheckValve1.touvert,idealCheckValve1.ouvert,$PRE.idealCheckValve1.ouvert,perteDP1.C2.b,perteDP1.C1.a,perteDP.C2.b,perteDP.C1.a,volumeC.Ce3.a,volumeC.Cs.b,volumeC.Ce2.a,volumeC.Ce1.a,idealCheckValve2.C1.a,idealCheckValve2.C2.b,idealCheckValve1.C1.a,idealCheckValve1.C2.b,volumeD.Cs3.b,volumeD.Cs2.b,volumeD.Cs1.b,volumeD.Ce.a,staticCentrifugalPump2.C2.b,staticCentrifugalPump2.C1.a,staticCentrifugalPump1.C2.b,staticCentrifugalPump1.C1.a,sourceP.C.b,puitsP.C.a,volumeC.Ce1.b,volumeD.Cs3.a) * Number of discrete states: 0 () * Number of clocked states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for initialization (67): * Single equations (assignments): 64 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 2 * 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 {(14,34)} Notification: Performance of prepare postOptimizeDAE: time 0.0004023/2.687, allocations: 253.3 kB / 0.9657 GB, free: 2.539 MB / 0.795 GB Notification: Performance of postOpt lateInlineFunction (simulation): time 0.0001696/2.687, allocations: 90.78 kB / 0.9658 GB, free: 2.449 MB / 0.795 GB Notification: Performance of postOpt wrapFunctionCalls (simulation): time 0.004221/2.692, allocations: 2.136 MB / 0.9679 GB, free: 280 kB / 0.795 GB Notification: Performance of postOpt simplifysemiLinear (simulation): time 1.222e-05/2.692, allocations: 7.984 kB / 0.9679 GB, free: 272 kB / 0.795 GB Notification: Performance of postOpt simplifyComplexFunction (simulation): time 4.629e-06/2.692, allocations: 0 / 0.9679 GB, free: 272 kB / 0.795 GB Notification: Performance of postOpt removeConstants (simulation): time 0.0004834/2.692, allocations: 273.7 kB / 0.9682 GB, free: 15.98 MB / 0.8106 GB Notification: Performance of postOpt simplifyTimeIndepFuncCalls (simulation): time 0.0001645/2.692, allocations: 21.2 kB / 0.9682 GB, free: 15.96 MB / 0.8106 GB Notification: Performance of postOpt simplifyAllExpressions (simulation): time 0.0005231/2.693, allocations: 30.59 kB / 0.9682 GB, free: 15.93 MB / 0.8106 GB Notification: Performance of postOpt findZeroCrossings (simulation): time 0.0001469/2.693, allocations: 52.58 kB / 0.9683 GB, free: 15.88 MB / 0.8106 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(perteDP1.T, perteDP1.rho, perteDP1.pro.u, perteDP1.pro.s, perteDP1.pro.cp, perteDP1.pro.ddhp, perteDP1.pro.ddph, perteDP1.pro.duph, perteDP1.pro.duhp, perteDP1.pro.x) = $cse1 Variables: 1: perteDP1.pro.ddhp:VARIABLE(unit = "kg.s2/m5" ) "Derivative of density wrt. specific enthalpy at constant pressure" type: Real 2: perteDP1.pro.ddph:VARIABLE(unit = "s2/m2" ) "Derivative of density wrt. pressure at constant specific enthalpy" type: Real 3: perteDP1.pro.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real 4: perteDP1.pro.x:VARIABLE(min = 0.0 max = 1.0 unit = "1" ) "Vapor mass fraction" type: Real 5: perteDP1.pro.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific heat capacity at constant presure" type: Real 6: $cse1.ddhp:VARIABLE(protected = true ) type: Real unreplaceable 7: $cse1.duhp:VARIABLE(protected = true ) type: Real unreplaceable 8: $cse1.u:VARIABLE(protected = true ) type: Real unreplaceable 9: $cse1.s:VARIABLE(protected = true ) type: Real unreplaceable 10: $cse1.cp:VARIABLE(protected = true ) type: Real unreplaceable [/var/lib/jenkins1/ws/OpenModelicaLibraryTestingWork/OpenModelica/OMCompiler/Compiler/BackEnd/DAEMode.mo:528:7-530:90:writable] Error: Internal error DAEMode.traverserStrongComponents failed on equation: 1/1 (1): 0.0 = if idealCheckValve1.ouvert then idealCheckValve1.deltaP else idealCheckValve1.Q - idealCheckValve1.Qmin 2/2 (1): idealCheckValve1.Q = staticCentrifugalPump1.Qv * staticCentrifugalPump1.rho 3/3 (1): staticCentrifugalPump1.rh = max(if noEvent(abs(staticCentrifugalPump1.R) > staticCentrifugalPump1.eps) then staticCentrifugalPump1.b1 * staticCentrifugalPump1.Qv * abs(staticCentrifugalPump1.Qv) / staticCentrifugalPump1.R ^ 2.0 + staticCentrifugalPump1.b2 * staticCentrifugalPump1.Qv / staticCentrifugalPump1.R + staticCentrifugalPump1.b3 else staticCentrifugalPump1.b3, staticCentrifugalPump1.rhmin) 4/4 (1): staticCentrifugalPump1.deltaH = 9.80665 * staticCentrifugalPump1.hn / staticCentrifugalPump1.rh 5/5 (1): staticCentrifugalPump1.deltaH = idealCheckValve1.C1.h - volumeD.Cs1.h 6/6 (1): 0.0 = if idealCheckValve1.Q > 0.0 then volumeD.Cs1.h - volumeD.h else idealCheckValve1.C1.h - staticCentrifugalPump1.C2.h_vol 7/7 (1): staticCentrifugalPump1.h = 0.5 * (volumeD.Cs1.h + idealCheckValve1.C1.h) 8/8 (10): $cse8 = ThermoSysPro.Properties.Fluid.Ph(staticCentrifugalPump1.Pm, staticCentrifugalPump1.h, staticCentrifugalPump1.mode, staticCentrifugalPump1.fluid) 9/18 (10): ThermoSysPro.Properties.WaterSteam.Common.ThermoProperties_ph(staticCentrifugalPump1.pro.T, staticCentrifugalPump1.rho, staticCentrifugalPump1.pro.u, staticCentrifugalPump1.pro.s, staticCentrifugalPump1.pro.cp, staticCentrifugalPump1.pro.ddhp, staticCentrifugalPump1.pro.ddph, staticCentrifugalPump1.pro.duph, staticCentrifugalPump1.pro.duhp, staticCentrifugalPump1.pro.x) = $cse8 10/28 (1): staticCentrifugalPump1.Pm = 0.5 * (volumeD.P + staticCentrifugalPump1.C2.P) 11/29 (1): staticCentrifugalPump1.deltaP = staticCentrifugalPump1.C2.P - volumeD.P 12/30 (1): staticCentrifugalPump1.deltaP = 9.80665 * staticCentrifugalPump1.rho * staticCentrifugalPump1.hn 13/31 (1): 0.0 = idealCheckValve1.deltaP + staticCentrifugalPump2.deltaP + (-idealCheckValve2.deltaP) - staticCentrifugalPump1.deltaP 14/32 (1): staticCentrifugalPump2.deltaP = staticCentrifugalPump2.C2.P - volumeD.P 15/33 (1): staticCentrifugalPump2.Pm = 0.5 * (volumeD.P + staticCentrifugalPump2.C2.P) 16/34 (10): $cse7 = ThermoSysPro.Properties.Fluid.Ph(staticCentrifugalPump2.Pm, staticCentrifugalPump2.h, staticCentrifugalPump2.mode, staticCentrifugalPump2.fluid) 17/44 (10): ThermoSysPro.Properties.WaterSteam.Common.ThermoProperties_ph(staticCentrifugalPump2.pro.T, staticCentrifugalPump2.rho, staticCentrifugalPump2.pro.u, staticCentrifugalPump2.pro.s, staticCentrifugalPump2.pro.cp, staticCentrifugalPump2.pro.ddhp, staticCentrifugalPump2.pro.ddph, staticCentrifugalPump2.pro.duph, staticCentrifugalPump2.pro.duhp, staticCentrifugalPump2.pro.x) = $cse7 18/54 (1): staticCentrifugalPump2.h = 0.5 * (volumeD.Cs2.h + idealCheckValve2.C1.h) 19/55 (1): staticCentrifugalPump2.deltaH = idealCheckValve2.C1.h - volumeD.Cs2.h 20/56 (1): staticCentrifugalPump2.deltaH = 9.80665 * staticCentrifugalPump2.hn / staticCentrifugalPump2.rh 21/57 (1): staticCentrifugalPump2.rh = max(if noEvent(abs(staticCentrifugalPump2.R) > staticCentrifugalPump2.eps) then staticCentrifugalPump2.b1 * staticCentrifugalPump2.Qv * abs(staticCentrifugalPump2.Qv) / staticCentrifugalPump2.R ^ 2.0 + staticCentrifugalPump2.b2 * staticCentrifugalPump2.Qv / staticCentrifugalPump2.R + staticCentrifugalPump2.b3 else staticCentrifugalPump2.b3, staticCentrifugalPump2.rhmin) 22/58 (1): idealCheckValve2.Q = staticCentrifugalPump2.Qv * staticCentrifugalPump2.rho 23/59 (1): 0.0 = if idealCheckValve2.Q > 0.0 then volumeD.Cs2.h - volumeD.h else idealCheckValve2.C1.h - staticCentrifugalPump2.C2.h_vol 24/60 (1): 0.0 = if idealCheckValve2.Q > 0.0 then idealCheckValve2.C1.h - staticCentrifugalPump2.C2.h_vol else idealCheckValve2.C1.h - volumeC.h 25/61 (1): 0.0 = perteDP.Q + (-idealCheckValve2.Q) - idealCheckValve1.Q 26/62 (1): $cse4 = ThermoSysPro.Functions.ThermoSquare(perteDP.Q, perteDP.eps) 27/63 (1): perteDP.deltaPf = 0.5 * perteDP.khi * $cse4 / (perteDP.A ^ 2.0 * perteDP.rho) 28/64 (1): perteDP.deltaP = perteDP.deltaPf + 9.80665 * perteDP.rho * (perteDP.z2 - perteDP.z1) 29/65 (10): $cse3 = ThermoSysPro.Properties.Fluid.Ph(perteDP.Pm, perteDP.h, perteDP.mode, perteDP.fluid) 30/75 (10): ThermoSysPro.Properties.WaterSteam.Common.ThermoProperties_ph(perteDP.T, perteDP.rho, perteDP.pro.u, perteDP.pro.s, perteDP.pro.cp, perteDP.pro.ddhp, perteDP.pro.ddph, perteDP.pro.duph, perteDP.pro.duhp, perteDP.pro.x) = $cse3 31/85 (1): perteDP.Pm = 0.5 * (sourceP.P0 + volumeD.P) 32/86 (1): sourceP.P0 - volumeD.P = perteDP.deltaP 33/87 (1): 0.0 = perteDP.Q - perteDP1.Q 34/88 (1): $cse2 = ThermoSysPro.Functions.ThermoSquare(perteDP1.Q, perteDP1.eps) 35/89 (1): perteDP1.deltaPf = 0.5 * perteDP1.khi * $cse2 / (perteDP1.A ^ 2.0 * perteDP1.rho) 36/90 (1): perteDP1.deltaP = perteDP1.deltaPf + 9.80665 * perteDP1.rho * (perteDP1.z2 - perteDP1.z1) 37/91 (10): $cse1 = ThermoSysPro.Properties.Fluid.Ph(perteDP1.Pm, perteDP1.h, perteDP1.mode, perteDP1.fluid) 38/101 (10): ThermoSysPro.Properties.WaterSteam.Common.ThermoProperties_ph(perteDP1.T, perteDP1.rho, perteDP1.pro.u, perteDP1.pro.s, perteDP1.pro.cp, perteDP1.pro.ddhp, perteDP1.pro.ddph, perteDP1.pro.duph, perteDP1.pro.duhp, perteDP1.pro.x) = $cse1 39/111 (1): perteDP1.Pm = 0.5 * (volumeC.P + puitsP.P0) 40/112 (1): idealCheckValve1.deltaP = staticCentrifugalPump1.C2.P - volumeC.P 41/113 (1): volumeC.P - puitsP.P0 = perteDP1.deltaP 42/114 (1): 0.0 = if perteDP1.Q > 0.0 then perteDP1.h - volumeC.h else perteDP1.h - puitsP.h 43/115 (1): 0.0 = if perteDP.Q > 0.0 then perteDP.h - sourceP.h else perteDP.h - volumeD.h 44/116 (1): 0.0 = if idealCheckValve2.ouvert then idealCheckValve2.deltaP else idealCheckValve2.Q - idealCheckValve2.Qmin 45/117 (1): staticCentrifugalPump2.hn = (staticCentrifugalPump2.a1 * abs(staticCentrifugalPump2.Qv) + staticCentrifugalPump2.a2 * staticCentrifugalPump2.R) * staticCentrifugalPump2.Qv + staticCentrifugalPump2.a3 * staticCentrifugalPump2.R ^ 2.0 46/118 (1): staticCentrifugalPump2.deltaP = 9.80665 * staticCentrifugalPump2.rho * staticCentrifugalPump2.hn 47/119 (1): 0.0 = if idealCheckValve1.Q > 0.0 then idealCheckValve1.C1.h - staticCentrifugalPump1.C2.h_vol else idealCheckValve1.C1.h - volumeC.h 48/120 (1): staticCentrifugalPump1.hn = (staticCentrifugalPump1.a1 * abs(staticCentrifugalPump1.Qv) + staticCentrifugalPump1.a2 * staticCentrifugalPump1.R) * staticCentrifugalPump1.Qv + staticCentrifugalPump1.a3 * staticCentrifugalPump1.R ^ 2.0 Variables: 1: staticCentrifugalPump1.hn:VARIABLE(min = 0.0 start = 10.0 unit = "m" ) "Pump head" type: Real 2: staticCentrifugalPump1.C2.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real 3: staticCentrifugalPump2.rho:VARIABLE(min = 1e-9 max = 1e5 start = 998.0 unit = "kg/m3" nominal = 998.0 ) "Fluid density" type: Real 4: staticCentrifugalPump2.hn:VARIABLE(min = 0.0 start = 10.0 unit = "m" ) "Pump head" type: Real 5: idealCheckValve2.deltaP:VARIABLE(unit = "Pa" ) "Pressure difference between the inlet and the outlet" type: Real 6: perteDP.h:VARIABLE(start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy" type: Real 7: perteDP1.h:VARIABLE(start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy" type: Real 8: perteDP1.deltaP:VARIABLE(unit = "Pa" ) "Total pressure loss" type: Real 9: idealCheckValve1.deltaP:VARIABLE(unit = "Pa" ) "Pressure difference between the inlet and the outlet" type: Real 10: volumeC.P:VARIABLE(min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure" type: Real 11: perteDP1.pro.ddhp:VARIABLE(unit = "kg.s2/m5" ) "Derivative of density wrt. specific enthalpy at constant pressure" type: Real 12: perteDP1.pro.ddph:VARIABLE(unit = "s2/m2" ) "Derivative of density wrt. pressure at constant specific enthalpy" type: Real 13: perteDP1.pro.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real 14: perteDP1.pro.x:VARIABLE(min = 0.0 max = 1.0 unit = "1" ) "Vapor mass fraction" type: Real 15: perteDP1.pro.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific heat capacity at constant presure" type: Real 16: $cse1.ddhp:VARIABLE(protected = true ) type: Real unreplaceable 17: $cse1.duhp:VARIABLE(protected = true ) type: Real unreplaceable 18: $cse1.u:VARIABLE(protected = true ) type: Real unreplaceable 19: $cse1.s:VARIABLE(protected = true ) type: Real unreplaceable 20: $cse1.cp:VARIABLE(protected = true ) type: Real unreplaceable 21: $cse1.T:VARIABLE(protected = true ) type: Real unreplaceable 22: $cse1.x:VARIABLE(protected = true ) type: Real unreplaceable 23: $cse1.d:VARIABLE(protected = true ) type: Real unreplaceable 24: $cse1.duph:VARIABLE(protected = true ) type: Real unreplaceable 25: perteDP1.Pm:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 ) "Fluid average pressure" type: Real 26: $cse1.ddph:VARIABLE(protected = true ) type: Real unreplaceable 27: perteDP1.pro.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific inner energy" type: Real 28: perteDP1.pro.duhp:VARIABLE(unit = "1" ) "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real 29: perteDP1.pro.duph:VARIABLE(unit = "m3/kg" ) "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real 30: perteDP1.T:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 300.0 ) "Fluid temperature" type: Real 31: perteDP1.deltaPf:VARIABLE(unit = "Pa" ) "Friction pressure loss" type: Real 32: perteDP1.rho:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 ) "Fluid density" type: Real 33: $cse2:VARIABLE(protected = true ) type: Real unreplaceable 34: perteDP1.Q:VARIABLE(start = 100.0 unit = "kg/s" ) "Mass flow rate" type: Real 35: perteDP.deltaP:VARIABLE(unit = "Pa" ) "Total pressure loss" type: Real 36: volumeD.P:VARIABLE(min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure" type: Real 37: perteDP.pro.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific inner energy" type: Real 38: perteDP.pro.duph:VARIABLE(unit = "m3/kg" ) "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real 39: perteDP.pro.x:VARIABLE(min = 0.0 max = 1.0 unit = "1" ) "Vapor mass fraction" type: Real 40: perteDP.pro.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real 41: perteDP.pro.ddhp:VARIABLE(unit = "kg.s2/m5" ) "Derivative of density wrt. specific enthalpy at constant pressure" type: Real 42: perteDP.T:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 300.0 ) "Fluid temperature" type: Real 43: perteDP.pro.ddph:VARIABLE(unit = "s2/m2" ) "Derivative of density wrt. pressure at constant specific enthalpy" type: Real 44: perteDP.pro.duhp:VARIABLE(unit = "1" ) "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real 45: perteDP.pro.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific heat capacity at constant presure" type: Real 46: $cse3.cp:VARIABLE(protected = true ) type: Real unreplaceable 47: $cse3.s:VARIABLE(protected = true ) type: Real unreplaceable 48: $cse3.duhp:VARIABLE(protected = true ) type: Real unreplaceable 49: $cse3.duph:VARIABLE(protected = true ) type: Real unreplaceable 50: $cse3.u:VARIABLE(protected = true ) type: Real unreplaceable 51: perteDP.Pm:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 ) "Fluid average pressure" type: Real 52: $cse3.x:VARIABLE(protected = true ) type: Real unreplaceable 53: $cse3.d:VARIABLE(protected = true ) type: Real unreplaceable 54: $cse3.ddph:VARIABLE(protected = true ) type: Real unreplaceable 55: $cse3.T:VARIABLE(protected = true ) type: Real unreplaceable 56: $cse3.ddhp:VARIABLE(protected = true ) type: Real unreplaceable 57: perteDP.rho:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 ) "Fluid density" type: Real 58: perteDP.deltaPf:VARIABLE(unit = "Pa" ) "Friction pressure loss" type: Real 59: $cse4:VARIABLE(protected = true ) type: Real unreplaceable 60: perteDP.Q:VARIABLE(start = 100.0 unit = "kg/s" ) "Mass flow rate" type: Real 61: staticCentrifugalPump2.C2.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real 62: idealCheckValve2.C1.h:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real 63: idealCheckValve2.Q:VARIABLE(start = 500.0 unit = "kg/s" ) "Mass flow rate" type: Real 64: staticCentrifugalPump2.Qv:VARIABLE(start = 0.5 unit = "m3/s" ) "Volume flow rate" type: Real 65: staticCentrifugalPump2.rh:VARIABLE() "Hydraulic efficiency" type: Real 66: staticCentrifugalPump2.deltaH:VARIABLE(unit = "J/kg" ) "Specific enthalpy variation between the outlet and the inlet" type: Real 67: volumeD.Cs2.h:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real 68: staticCentrifugalPump2.pro.x:VARIABLE(min = 0.0 max = 1.0 unit = "1" ) "Vapor mass fraction" type: Real 69: staticCentrifugalPump2.pro.ddph:VARIABLE(unit = "s2/m2" ) "Derivative of density wrt. pressure at constant specific enthalpy" type: Real 70: staticCentrifugalPump2.pro.duph:VARIABLE(unit = "m3/kg" ) "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real 71: $cse7.duhp:VARIABLE(protected = true ) type: Real unreplaceable 72: staticCentrifugalPump2.pro.T:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 320.0 ) "Temperature" type: Real 73: staticCentrifugalPump2.pro.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific inner energy" type: Real 74: staticCentrifugalPump2.pro.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real 75: staticCentrifugalPump2.pro.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific heat capacity at constant presure" type: Real 76: staticCentrifugalPump2.pro.ddhp:VARIABLE(unit = "kg.s2/m5" ) "Derivative of density wrt. specific enthalpy at constant pressure" type: Real 77: staticCentrifugalPump2.pro.duhp:VARIABLE(unit = "1" ) "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real 78: $cse7.cp:VARIABLE(protected = true ) type: Real unreplaceable 79: $cse7.u:VARIABLE(protected = true ) type: Real unreplaceable 80: $cse7.ddhp:VARIABLE(protected = true ) type: Real unreplaceable 81: $cse7.x:VARIABLE(protected = true ) type: Real unreplaceable 82: $cse7.T:VARIABLE(protected = true ) type: Real unreplaceable 83: staticCentrifugalPump2.h:VARIABLE(start = 1e5 unit = "J/kg" ) "Fluid average specific enthalpy" type: Real 84: $cse7.s:VARIABLE(protected = true ) type: Real unreplaceable 85: $cse7.d:VARIABLE(protected = true ) type: Real unreplaceable 86: $cse7.duph:VARIABLE(protected = true ) type: Real unreplaceable 87: $cse7.ddph:VARIABLE(protected = true ) type: Real unreplaceable 88: staticCentrifugalPump2.Pm:VARIABLE(min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid average pressure" type: Real 89: staticCentrifugalPump2.C2.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 90: staticCentrifugalPump2.deltaP:VARIABLE(unit = "Pa" ) "Pressure variation between the outlet and the inlet" type: Real 91: staticCentrifugalPump1.rho:VARIABLE(min = 1e-9 max = 1e5 start = 998.0 unit = "kg/m3" nominal = 998.0 ) "Fluid density" type: Real 92: staticCentrifugalPump1.deltaP:VARIABLE(unit = "Pa" ) "Pressure variation between the outlet and the inlet" type: Real 93: staticCentrifugalPump1.C2.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 94: staticCentrifugalPump1.pro.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific inner energy" type: Real 95: staticCentrifugalPump1.pro.duhp:VARIABLE(unit = "1" ) "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real 96: staticCentrifugalPump1.pro.T:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 320.0 ) "Temperature" type: Real 97: $cse8.d:VARIABLE(protected = true ) type: Real unreplaceable 98: staticCentrifugalPump1.pro.x:VARIABLE(min = 0.0 max = 1.0 unit = "1" ) "Vapor mass fraction" type: Real 99: staticCentrifugalPump1.pro.ddph:VARIABLE(unit = "s2/m2" ) "Derivative of density wrt. pressure at constant specific enthalpy" type: Real 100: staticCentrifugalPump1.pro.ddhp:VARIABLE(unit = "kg.s2/m5" ) "Derivative of density wrt. specific enthalpy at constant pressure" type: Real 101: staticCentrifugalPump1.pro.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real 102: staticCentrifugalPump1.pro.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific heat capacity at constant presure" type: Real 103: staticCentrifugalPump1.pro.duph:VARIABLE(unit = "m3/kg" ) "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real 104: $cse8.s:VARIABLE(protected = true ) type: Real unreplaceable 105: $cse8.ddhp:VARIABLE(protected = true ) type: Real unreplaceable 106: $cse8.ddph:VARIABLE(protected = true ) type: Real unreplaceable 107: $cse8.duph:VARIABLE(protected = true ) type: Real unreplaceable 108: staticCentrifugalPump1.Pm:VARIABLE(min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid average pressure" type: Real 109: $cse8.x:VARIABLE(protected = true ) type: Real unreplaceable 110: $cse8.T:VARIABLE(protected = true ) type: Real unreplaceable 111: $cse8.u:VARIABLE(protected = true ) type: Real unreplaceable 112: $cse8.cp:VARIABLE(protected = true ) type: Real unreplaceable 113: $cse8.duhp:VARIABLE(protected = true ) type: Real unreplaceable 114: staticCentrifugalPump1.h:VARIABLE(start = 1e5 unit = "J/kg" ) "Fluid average specific enthalpy" type: Real 115: volumeD.Cs1.h:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real 116: idealCheckValve1.C1.h:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real 117: staticCentrifugalPump1.deltaH:VARIABLE(unit = "J/kg" ) "Specific enthalpy variation between the outlet and the inlet" type: Real 118: staticCentrifugalPump1.rh:VARIABLE() "Hydraulic efficiency" type: Real 119: staticCentrifugalPump1.Qv:VARIABLE(start = 0.5 unit = "m3/s" ) "Volume flow rate" type: Real 120: idealCheckValve1.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 postOpt createDAEmodeBDAE (simulation): time 0.004084/2.697, allocations: 5.274 MB / 0.9734 GB, free: 9.395 MB / 0.8106 GB Error: post-optimization module createDAEmodeBDAE (simulation) failed. Error: Internal error SimCode DAEmode: The model ThermoSysPro.Properties.WaterSteamSimple.Validation.Bench.Test1_IF97 could not be translated