Running: ./testmodel.py --libraries=/home/hudson/saved_omc/libraries/.openmodelica/libraries --ompython_omhome=/usr ThermoSysPro_ThermoSysPro.Examples.SimpleExamples.TestDynamicReliefValve.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.TestDynamicReliefValve,tolerance=1e-06,outputFormat="empty",numberOfIntervals=1200,variableFilter="",fileNamePrefix="ThermoSysPro_ThermoSysPro.Examples.SimpleExamples.TestDynamicReliefValve")
translateModel(ThermoSysPro.Examples.SimpleExamples.TestDynamicReliefValve,tolerance=1e-06,outputFormat="empty",numberOfIntervals=1200,variableFilter="",fileNamePrefix="ThermoSysPro_ThermoSysPro.Examples.SimpleExamples.TestDynamicReliefValve")
Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermoSysPro 4.0.0-master/package.mo): time 0.8344/0.8344, allocations: 150.9 MB / 167.2 MB, free: 14.52 MB / 142.1 MB
Notification: Performance of FrontEnd - loaded program: time 0.0003357/0.0003357, allocations: 21.67 kB / 237.8 MB, free: 1.766 MB / 190.1 MB
Notification: Performance of FrontEnd - Absyn->SCode: time 0.05429/0.05464, allocations: 31.34 MB / 269.1 MB, free: 7.027 MB / 222.1 MB
Notification: Automatically loaded package Complex 4.0.0 due to uses annotation from Modelica.
Notification: Automatically loaded package ModelicaServices 4.0.0 due to uses annotation from Modelica.
Notification: Automatically loaded package Modelica 4.0.0 due to usage.
Notification: Performance of NFInst.instantiate(ThermoSysPro.Examples.SimpleExamples.TestDynamicReliefValve): time 1.605/1.66, allocations: 296.7 MB / 0.5526 GB, free: 11.18 MB / 446.1 MB
Notification: Performance of NFInst.instExpressions: time 0.502/2.162, allocations: 187.3 MB / 0.7355 GB, free: 0.7578 MB / 0.5919 GB
Notification: Performance of NFInst.updateImplicitVariability: time 0.0002935/2.162, allocations: 11.25 kB / 0.7355 GB, free: 0.7539 MB / 0.5919 GB
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermoSysPro 4.0.0-master/WaterSteam/PressureLosses/DynamicReliefValve.mo:73:3-75:16:writable] Warning: Connector C1 is not balanced: The number of potential variables (4) is not equal to the number of flow variables (0).
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermoSysPro 4.0.0-master/WaterSteam/PressureLosses/DynamicReliefValve.mo:76:3-78:33: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/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/PressureLosses/Bend.mo:55:3-57:42: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/Bend.mo:58:3-60:43: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/Diaphragm.mo:30:3-32:42: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/Diaphragm.mo:33:3-35:37: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 0.0006768/2.163, allocations: 411.2 kB / 0.7359 GB, free: 0.75 MB / 0.5919 GB
Notification: Performance of NFTyping.typeBindings: time 0.0008525/2.164, allocations: 0.5534 MB / 0.7365 GB, free: 0.7422 MB / 0.5919 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 0.0296/2.193, allocations: 11.52 MB / 0.7477 GB, free: 484 kB / 0.5919 GB
Notification: Performance of NFFlatten.flatten: time 0.001722/2.195, allocations: 1.19 MB / 0.7489 GB, free: 480 kB / 0.5919 GB
Notification: Performance of NFFlatten.resolveConnections: time 0.0005053/2.196, allocations: 460.8 kB / 0.7493 GB, free: 428 kB / 0.5919 GB
Notification: Performance of NFEvalConstants.evaluate: time 0.0005888/2.196, allocations: 0.5199 MB / 0.7498 GB, free: 424 kB / 0.5919 GB
Notification: Performance of NFSimplifyModel.simplify: time 0.0005859/2.197, allocations: 0.6204 MB / 0.7504 GB, free: 424 kB / 0.5919 GB
Notification: Performance of NFPackage.collectConstants: time 0.0001034/2.197, allocations: 66.69 kB / 0.7505 GB, free: 424 kB / 0.5919 GB
Notification: Performance of NFFlatten.collectFunctions: time 0.03469/2.232, allocations: 20.35 MB / 0.7704 GB, free: 13.96 MB / 0.6075 GB
Notification: Performance of NFScalarize.scalarize: time 0.0004074/2.232, allocations: 309.1 kB / 0.7707 GB, free: 13.91 MB / 0.6075 GB
Notification: Performance of NFVerifyModel.verify: time 0.0007296/2.233, allocations: 0.5463 MB / 0.7712 GB, free: 13.87 MB / 0.6075 GB
Notification: Performance of NFConvertDAE.convert: time 0.02438/2.257, allocations: 10.71 MB / 0.7817 GB, free: 9.914 MB / 0.6075 GB
Notification: Performance of FrontEnd - DAE generated: time 5.631e-06/2.257, allocations: 0 / 0.7817 GB, free: 9.914 MB / 0.6075 GB
Notification: Performance of FrontEnd: time 2.485e-06/2.257, allocations: 0 / 0.7817 GB, free: 9.914 MB / 0.6075 GB
Notification: Performance of Transformations before backend: time 1.273e-05/2.257, allocations: 1.203 kB / 0.7817 GB, free: 9.914 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: 206
 * Number of variables: 206
Notification: Performance of Generate backend data structure: time 0.006201/2.263, allocations: 2.623 MB / 0.7842 GB, free: 8.293 MB / 0.6075 GB
Notification: Performance of prepare preOptimizeDAE: time 4.134e-05/2.263, allocations: 10.22 kB / 0.7842 GB, free: 8.293 MB / 0.6075 GB
Notification: Performance of preOpt normalInlineFunction (simulation): time 0.0001877/2.264, allocations: 131.6 kB / 0.7844 GB, free: 8.223 MB / 0.6075 GB
Notification: Performance of preOpt evaluateParameters (simulation): time 0.0007962/2.264, allocations: 0.6789 MB / 0.785 GB, free: 7.801 MB / 0.6075 GB
Notification: Performance of preOpt simplifyIfEquations (simulation): time 7.058e-05/2.265, allocations: 76 kB / 0.7851 GB, free: 7.766 MB / 0.6075 GB
Notification: Performance of preOpt expandDerOperator (simulation): time 7.861e-05/2.265, allocations: 61.5 kB / 0.7851 GB, free: 7.766 MB / 0.6075 GB
Notification: Performance of preOpt clockPartitioning (simulation): time 0.001185/2.266, allocations: 0.9153 MB / 0.786 GB, free: 7.418 MB / 0.6075 GB
Notification: Performance of preOpt findStateOrder (simulation): time 2.194e-05/2.266, allocations: 9.719 kB / 0.786 GB, free: 7.418 MB / 0.6075 GB
Notification: Performance of preOpt replaceEdgeChange (simulation): time 5.636e-05/2.266, allocations: 25.22 kB / 0.7861 GB, free: 7.418 MB / 0.6075 GB
Notification: Performance of preOpt inlineArrayEqn (simulation): time 2.435e-05/2.266, allocations: 28.61 kB / 0.7861 GB, free: 7.414 MB / 0.6075 GB
Notification: Performance of preOpt removeEqualRHS (simulation): time 0.001129/2.267, allocations: 0.773 MB / 0.7869 GB, free: 7.297 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 0.02189/2.289, allocations: 12.73 MB / 0.7993 GB, free: 13.59 MB / 0.6231 GB
Notification: Performance of preOpt comSubExp (simulation): time 0.001581/2.291, allocations: 0.6408 MB / 0.7999 GB, free: 13.18 MB / 0.6231 GB
Notification: Performance of preOpt resolveLoops (simulation): time 0.0006146/2.291, allocations: 376.5 kB / 0.8003 GB, free: 12.96 MB / 0.6231 GB
Notification: Performance of preOpt evalFunc (simulation): time 0.3221/2.613, allocations: 159.8 MB / 0.9563 GB, free: 12.13 MB / 0.795 GB
Notification: Performance of preOpt encapsulateWhenConditions (simulation): time 0.0009432/2.614, allocations: 460.5 kB / 0.9568 GB, free: 11.66 MB / 0.795 GB
Notification: Performance of pre-optimization done (n=109): time 3.717e-06/2.614, allocations: 0 / 0.9568 GB, free: 11.66 MB / 0.795 GB
Notification: Performance of matching and sorting (n=109): time 0.007982/2.622, allocations: 2.168 MB / 0.9589 GB, free: 9.477 MB / 0.795 GB
Notification: Performance of inlineWhenForInitialization (initialization): time 7.364e-05/2.622, allocations: 166.7 kB / 0.9591 GB, free: 9.277 MB / 0.795 GB
Notification: Performance of selectInitializationVariablesDAE (initialization): time 0.001872/2.624, allocations: 1.276 MB / 0.9603 GB, free: 7.98 MB / 0.795 GB
Notification: Performance of collectPreVariables (initialization): time 5.356e-05/2.624, allocations: 37.7 kB / 0.9603 GB, free: 7.938 MB / 0.795 GB
Notification: Performance of collectInitialEqns (initialization): time 0.0003492/2.625, allocations: 470.2 kB / 0.9608 GB, free: 7.477 MB / 0.795 GB
Notification: Performance of collectInitialBindings (initialization): time 0.000266/2.625, allocations: 359 kB / 0.9611 GB, free: 7.129 MB / 0.795 GB
Notification: Performance of simplifyInitialFunctions (initialization): time 0.0002469/2.625, allocations: 154.2 kB / 0.9613 GB, free: 6.973 MB / 0.795 GB
Notification: Performance of setup shared object (initialization): time 0.0001222/2.625, allocations: 341.9 kB / 0.9616 GB, free: 6.633 MB / 0.795 GB
Notification: Performance of preBalanceInitialSystem (initialization): time 0.0006261/2.626, allocations: 359 kB / 0.9619 GB, free: 6.285 MB / 0.795 GB
Notification: Performance of partitionIndependentBlocks (initialization): time 0.0007472/2.627, allocations: 0.5201 MB / 0.9625 GB, free: 5.703 MB / 0.795 GB
Notification: Performance of analyzeInitialSystem (initialization): time 0.001351/2.628, allocations: 0.8345 MB / 0.9633 GB, free: 4.836 MB / 0.795 GB
Notification: Performance of solveInitialSystemEqSystem (initialization): time 5.139e-06/2.628, allocations: 0 / 0.9633 GB, free: 4.836 MB / 0.795 GB
Notification: Performance of matching and sorting (n=135) (initialization): time 0.00223/2.63, allocations: 1.239 MB / 0.9645 GB, free: 3.609 MB / 0.795 GB
Notification: Performance of prepare postOptimizeDAE: time 1.899e-05/2.63, allocations: 4 kB / 0.9645 GB, free: 3.605 MB / 0.795 GB
Notification: Performance of postOpt simplifyComplexFunction (initialization): time 1.162e-05/2.63, allocations: 4 kB / 0.9645 GB, free: 3.602 MB / 0.795 GB
Notification: Performance of postOpt tearingSystem (initialization): time 0.004362/2.635, allocations: 1.067 MB / 0.9655 GB, free: 2.531 MB / 0.795 GB
Notification: Performance of postOpt solveSimpleEquations (initialization): time 0.0005092/2.635, allocations: 102.3 kB / 0.9656 GB, free: 2.438 MB / 0.795 GB
Notification: Performance of postOpt calculateStrongComponentJacobians (initialization): time 0.001504/2.637, allocations: 1.13 MB / 0.9667 GB, free: 1.289 MB / 0.795 GB
Notification: Performance of postOpt simplifyAllExpressions (initialization): time 0.000727/2.638, allocations: 103 kB / 0.9668 GB, free: 1.188 MB / 0.795 GB
Notification: Performance of postOpt collapseArrayExpressions (initialization): time 6.816e-05/2.638, allocations: 37.88 kB / 0.9669 GB, free: 1.152 MB / 0.795 GB
Notification: Model statistics after passing the back-end for initialization:
 * Number of independent subsystems: 17
 * Number of states: 0 ()
 * Number of discrete variables: 13 (diaphragm.C2.b,diaphragm.C1.a,bend.C2.b,bend.C1.a,sourceP.C.b,sinkP.C.a,pipe.C2.b,pipe.C1.a,reliefValve.C2.b,reliefValve.C1.a,reliefValve.clapper_is_free,$whenCondition1,$whenCondition2)
 * Number of discrete states: 0 ()
 * Number of clocked states: 0 ()
 * Top-level inputs: 0
Notification: Strong component statistics for initialization (56):
 * Single equations (assignments): 53
 * 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
   {(7,19)}
Notification: Performance of prepare postOptimizeDAE: time 0.0004699/2.638, allocations: 339.1 kB / 0.9672 GB, free: 0.8203 MB / 0.795 GB
Notification: Performance of postOpt lateInlineFunction (simulation): time 0.0002162/2.638, allocations: 110.5 kB / 0.9673 GB, free: 0.7109 MB / 0.795 GB
Notification: Performance of postOpt wrapFunctionCalls (simulation): time 0.00305/2.641, allocations: 1.687 MB / 0.9689 GB, free: 14.99 MB / 0.8106 GB
Notification: Performance of postOpt simplifysemiLinear (simulation): time 9.418e-06/2.641, allocations: 1.781 kB / 0.9689 GB, free: 14.99 MB / 0.8106 GB
Notification: Performance of postOpt simplifyComplexFunction (simulation): time 4.569e-06/2.641, allocations: 0 / 0.9689 GB, free: 14.99 MB / 0.8106 GB
Notification: Performance of postOpt removeConstants (simulation): time 0.0004899/2.642, allocations: 287.1 kB / 0.9692 GB, free: 14.69 MB / 0.8106 GB
Notification: Performance of postOpt simplifyTimeIndepFuncCalls (simulation): time 0.0001417/2.642, allocations: 16 kB / 0.9692 GB, free: 14.68 MB / 0.8106 GB
Notification: Performance of postOpt simplifyAllExpressions (simulation): time 0.0005514/2.643, allocations: 39.95 kB / 0.9693 GB, free: 14.64 MB / 0.8106 GB
Notification: Performance of postOpt findZeroCrossings (simulation): time 0.0001314/2.643, allocations: 56.47 kB / 0.9693 GB, free: 14.58 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(diaphragm.T, diaphragm.rho, diaphragm.pro.u, diaphragm.pro.s, diaphragm.pro.cp, diaphragm.pro.ddhp, diaphragm.pro.ddph, diaphragm.pro.duph, diaphragm.pro.duhp, diaphragm.pro.x) = $cse2

Variables:
1: diaphragm.pro.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 )  "Specific inner energy" type: Real
2: diaphragm.pro.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific entropy" type: Real
3: diaphragm.pro.ddhp:VARIABLE(unit = "kg.s2/m5" )  "Derivative of density wrt. specific enthalpy at constant pressure" type: Real
4: diaphragm.T:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 300.0 )  "Fluid temperature" type: Real
5: diaphragm.pro.x:VARIABLE(min = 0.0 max = 1.0 unit = "1" )  "Vapor mass fraction" type: Real
6: diaphragm.pro.ddph:VARIABLE(unit = "s2/m2" )  "Derivative of density wrt. pressure at constant specific enthalpy" type: Real
7: diaphragm.pro.duhp:VARIABLE(unit = "1" )  "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real
8: $cse2.T:VARIABLE(protected = true )  type: Real unreplaceable
9: $cse2.x:VARIABLE(protected = true )  type: Real unreplaceable
10: $cse2.duhp: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): diaphragm.deltaP = 8.0 * diaphragm.khi * $cse3 / (9.869604401089358 * diaphragm.D ^ 4.0 * diaphragm.rho)
2/2 (1): reliefValve.C2.P - sinkP.P0 = diaphragm.deltaP
3/3 (1): reliefValve.deltaP = bend.C2.P - reliefValve.C2.P
4/4 (1): reliefValve.deltaP * reliefValve.Cv * abs(reliefValve.Cv) = 1.733e12 * $cse9 / (reliefValve.rho * 998.98)
5/5 (10): $cse8 = ThermoSysPro.Properties.WaterSteam.IF97.Water_Ph(reliefValve.Pm, diaphragm.h, reliefValve.mode)
6/15 (10): ThermoSysPro.Properties.WaterSteam.Common.ThermoProperties_ph(reliefValve.T, reliefValve.rho, reliefValve.pro.u, reliefValve.pro.s, reliefValve.pro.cp, reliefValve.pro.ddhp, reliefValve.pro.ddph, reliefValve.pro.duph, reliefValve.pro.duhp, reliefValve.pro.x) = $cse8
7/25 (1): reliefValve.Pm = 0.5 * (bend.C2.P + reliefValve.C2.P)
8/26 (1): pipe.C2.P - bend.C2.P = bend.deltaP
9/27 (1): bend.deltaP = 8.0 * bend.khi * $cse5 / (9.869604401089358 * bend.D ^ 4.0 * bend.rho)
10/28 (1): $cse5 = ThermoSysPro.Functions.ThermoSquare(diaphragm.Q, bend.eps)
11/29 (1): $cse3 = ThermoSysPro.Functions.ThermoSquare(diaphragm.Q, diaphragm.eps)
12/30 (1): $cse7 = ThermoSysPro.Functions.ThermoSquare(diaphragm.Q, pipe.eps)
13/31 (1): pipe.deltaPf = 0.5 * pipe.khi * $cse7 / (pipe.A ^ 2.0 * pipe.rho)
14/32 (1): pipe.deltaP = pipe.deltaPf + 9.80665 * pipe.rho * (pipe.z2 - pipe.z1)
15/33 (10): $cse6 = ThermoSysPro.Properties.Fluid.Ph(pipe.Pm, diaphragm.h, pipe.mode, pipe.fluid)
16/43 (10): ThermoSysPro.Properties.WaterSteam.Common.ThermoProperties_ph(pipe.T, pipe.rho, pipe.pro.u, pipe.pro.s, pipe.pro.cp, pipe.pro.ddhp, pipe.pro.ddph, pipe.pro.duph, pipe.pro.duhp, pipe.pro.x) = $cse6
17/53 (1): pipe.Pm = 0.5 * (sourceP.P + pipe.C2.P)
18/54 (1): sourceP.P - pipe.C2.P = pipe.deltaP
19/55 (1): bend.Pm = 0.5 * (pipe.C2.P + bend.C2.P)
20/56 (10): $cse4 = ThermoSysPro.Properties.Fluid.Ph(bend.Pm, diaphragm.h, bend.mode, bend.fluid)
21/66 (1): bend.mu = ThermoSysPro.Properties.WaterSteam.IF97.DynamicViscosity_rhoT(bend.rho, bend.T)
22/67 (1): bend.Re = 4.0 * abs(diaphragm.Q) / (3.141592653589793 * bend.D * bend.mu)
23/68 (1): bend.lambda = if noEvent(bend.Re > 0.0) then 1.0 / (1.8 * log10(bend.Re) - 1.64) ^ 2.0 else 0.0
24/69 (1): bend.khif = 0.0175 * bend.lambda * bend.R0 * bend.delta / bend.D
25/70 (1): bend.khi = bend.khim + bend.khif
26/71 (10): ThermoSysPro.Properties.WaterSteam.Common.ThermoProperties_ph(bend.T, bend.rho, bend.pro.u, bend.pro.s, bend.pro.cp, bend.pro.ddhp, bend.pro.ddph, bend.pro.duph, bend.pro.duhp, bend.pro.x) = $cse4
27/81 (1): $cse9 = ThermoSysPro.Functions.ThermoSquare(diaphragm.Q, reliefValve.eps)
28/82 (1): 0.0 = if diaphragm.Q > 0.0 then diaphragm.h - bend.C2.h_vol else diaphragm.h - reliefValve.C2.h_vol
29/83 (1): 0.0 = if diaphragm.Q > 0.0 then diaphragm.h - pipe.C2.h_vol else diaphragm.h - bend.C2.h_vol
30/84 (1): 0.0 = if diaphragm.Q > 0.0 then diaphragm.h - sourceP.h else diaphragm.h - pipe.C2.h_vol
31/85 (10): $cse2 = ThermoSysPro.Properties.Fluid.Ph(diaphragm.Pm, diaphragm.h, diaphragm.mode, diaphragm.fluid)
32/95 (10): ThermoSysPro.Properties.WaterSteam.Common.ThermoProperties_ph(diaphragm.T, diaphragm.rho, diaphragm.pro.u, diaphragm.pro.s, diaphragm.pro.cp, diaphragm.pro.ddhp, diaphragm.pro.ddph, diaphragm.pro.duph, diaphragm.pro.duhp, diaphragm.pro.x) = $cse2
33/105 (1): 0.0 = if diaphragm.Q > 0.0 then diaphragm.h - reliefValve.C2.h_vol else diaphragm.h - sinkP.h
34/106 (1): diaphragm.Pm = 0.5 * (reliefValve.C2.P + sinkP.P0)

Variables:
1: diaphragm.Pm:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 )  "Fluid average pressure" type: Real
2: reliefValve.C2.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" )  "Fluid specific enthalpy in the control volume" type: Real
3: diaphragm.pro.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 )  "Specific inner energy" type: Real
4: diaphragm.pro.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific entropy" type: Real
5: diaphragm.pro.ddhp:VARIABLE(unit = "kg.s2/m5" )  "Derivative of density wrt. specific enthalpy at constant pressure" type: Real
6: diaphragm.T:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 300.0 )  "Fluid temperature" type: Real
7: diaphragm.pro.x:VARIABLE(min = 0.0 max = 1.0 unit = "1" )  "Vapor mass fraction" type: Real
8: diaphragm.pro.ddph:VARIABLE(unit = "s2/m2" )  "Derivative of density wrt. pressure at constant specific enthalpy" type: Real
9: diaphragm.pro.duhp:VARIABLE(unit = "1" )  "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real
10: $cse2.T:VARIABLE(protected = true )  type: Real unreplaceable
11: $cse2.x:VARIABLE(protected = true )  type: Real unreplaceable
12: $cse2.duhp:VARIABLE(protected = true )  type: Real unreplaceable
13: $cse2.cp:VARIABLE(protected = true )  type: Real unreplaceable
14: $cse2.s:VARIABLE(protected = true )  type: Real unreplaceable
15: $cse2.u:VARIABLE(protected = true )  type: Real unreplaceable
16: $cse2.d:VARIABLE(protected = true )  type: Real unreplaceable
17: $cse2.duph:VARIABLE(protected = true )  type: Real unreplaceable
18: $cse2.ddph:VARIABLE(protected = true )  type: Real unreplaceable
19: $cse2.ddhp:VARIABLE(protected = true )  type: Real unreplaceable
20: diaphragm.h:VARIABLE(start = 1e5 unit = "J/kg" )  "Fluid specific enthalpy" type: Real
21: pipe.C2.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" )  "Fluid specific enthalpy in the control volume" type: Real
22: bend.C2.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" )  "Fluid specific enthalpy in the control volume" type: Real
23: $cse9:VARIABLE(protected = true )  type: Real unreplaceable
24: bend.rho:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 )  "Fluid density" type: Real
25: bend.pro.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific entropy" type: Real
26: bend.khi:VARIABLE()  "Hydraulic pressure loss coefficient" type: Real
27: bend.khif:VARIABLE()  "Friction pressure loss coefficient" type: Real
28: bend.lambda:VARIABLE()  "Friction pressure loss coefficient" type: Real
29: bend.Re:VARIABLE(unit = "1" )  "Reynolds number" type: Real
30: bend.mu:VARIABLE(min = 0.0 unit = "Pa.s" )  "Fluid dynamic viscosity" type: Real
31: bend.T:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 300.0 )  "Fluid temperature" type: Real
32: bend.pro.duhp:VARIABLE(unit = "1" )  "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real
33: bend.pro.ddhp:VARIABLE(unit = "kg.s2/m5" )  "Derivative of density wrt. specific enthalpy at constant pressure" type: Real
34: bend.pro.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 )  "Specific inner energy" type: Real
35: bend.pro.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific heat capacity at constant presure" type: Real
36: bend.pro.ddph:VARIABLE(unit = "s2/m2" )  "Derivative of density wrt. pressure at constant specific enthalpy" type: Real
37: bend.pro.duph:VARIABLE(unit = "m3/kg" )  "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real
38: bend.pro.x:VARIABLE(min = 0.0 max = 1.0 unit = "1" )  "Vapor mass fraction" type: Real
39: $cse4.duhp:VARIABLE(protected = true )  type: Real unreplaceable
40: $cse4.x:VARIABLE(protected = true )  type: Real unreplaceable
41: $cse4.cp:VARIABLE(protected = true )  type: Real unreplaceable
42: $cse4.duph:VARIABLE(protected = true )  type: Real unreplaceable
43: $cse4.s:VARIABLE(protected = true )  type: Real unreplaceable
44: $cse4.ddhp:VARIABLE(protected = true )  type: Real unreplaceable
45: $cse4.d:VARIABLE(protected = true )  type: Real unreplaceable
46: $cse4.T:VARIABLE(protected = true )  type: Real unreplaceable
47: $cse4.u:VARIABLE(protected = true )  type: Real unreplaceable
48: $cse4.ddph:VARIABLE(protected = true )  type: Real unreplaceable
49: bend.Pm:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 )  "Fluid average pressure" type: Real
50: pipe.deltaP:VARIABLE(unit = "Pa" )  "Total pressure loss" type: Real
51: pipe.C2.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 )  "Fluid pressure in the control volume" type: Real
52: pipe.pro.ddhp:VARIABLE(unit = "kg.s2/m5" )  "Derivative of density wrt. specific enthalpy at constant pressure" type: Real
53: pipe.pro.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific heat capacity at constant presure" type: Real
54: pipe.pro.duph:VARIABLE(unit = "m3/kg" )  "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real
55: pipe.T:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 300.0 )  "Fluid temperature" type: Real
56: pipe.pro.ddph:VARIABLE(unit = "s2/m2" )  "Derivative of density wrt. pressure at constant specific enthalpy" type: Real
57: pipe.pro.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 )  "Specific inner energy" type: Real
58: pipe.pro.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific entropy" type: Real
59: $cse6.s:VARIABLE(protected = true )  type: Real unreplaceable
60: $cse6.d:VARIABLE(protected = true )  type: Real unreplaceable
61: $cse6.x:VARIABLE(protected = true )  type: Real unreplaceable
62: $cse6.u:VARIABLE(protected = true )  type: Real unreplaceable
63: $cse6.ddph:VARIABLE(protected = true )  type: Real unreplaceable
64: $cse6.ddhp:VARIABLE(protected = true )  type: Real unreplaceable
65: $cse6.cp:VARIABLE(protected = true )  type: Real unreplaceable
66: pipe.Pm:VARIABLE(min = 0.0 start = Pinitial unit = "Pa" nominal = 1e5 )  "Fluid average pressure" type: Real
67: $cse6.duhp:VARIABLE(protected = true )  type: Real unreplaceable
68: $cse6.T:VARIABLE(protected = true )  type: Real unreplaceable
69: $cse6.duph:VARIABLE(protected = true )  type: Real unreplaceable
70: pipe.pro.x:VARIABLE(min = 0.0 max = 1.0 unit = "1" )  "Vapor mass fraction" type: Real
71: pipe.pro.duhp:VARIABLE(unit = "1" )  "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real
72: pipe.deltaPf:VARIABLE(unit = "Pa" )  "Friction pressure loss" type: Real
73: pipe.rho:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 )  "Fluid density" type: Real
74: $cse7:VARIABLE(protected = true )  type: Real unreplaceable
75: $cse3:VARIABLE(protected = true )  type: Real unreplaceable
76: diaphragm.Q:VARIABLE(start = 0.0 unit = "kg/s" )  "Mass flow rate" type: Real
77: $cse5:VARIABLE(protected = true )  type: Real unreplaceable
78: bend.deltaP:VARIABLE(unit = "Pa" )  "Presure loss" type: Real
79: bend.C2.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 )  "Fluid pressure in the control volume" type: Real
80: reliefValve.pro.duph:VARIABLE(unit = "m3/kg" protected = true )  "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real
81: reliefValve.pro.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 protected = true )  "Specific entropy" type: Real
82: reliefValve.pro.ddhp:VARIABLE(unit = "kg.s2/m5" protected = true )  "Derivative of density wrt. specific enthalpy at constant pressure" type: Real
83: reliefValve.pro.duhp:VARIABLE(unit = "1" protected = true )  "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real
84: reliefValve.pro.ddph:VARIABLE(unit = "s2/m2" protected = true )  "Derivative of density wrt. pressure at constant specific enthalpy" type: Real
85: $cse8.u:VARIABLE(protected = true )  type: Real unreplaceable
86: reliefValve.Pm:VARIABLE(min = 0.0 start = Pinitial unit = "Pa" nominal = 1e5 )  "Fluid average pressure" type: Real
87: $cse8.cp:VARIABLE(protected = true )  type: Real unreplaceable
88: $cse8.d:VARIABLE(protected = true )  type: Real unreplaceable
89: $cse8.x:VARIABLE(protected = true )  type: Real unreplaceable
90: $cse8.ddph:VARIABLE(protected = true )  type: Real unreplaceable
91: $cse8.s:VARIABLE(protected = true )  type: Real unreplaceable
92: $cse8.ddhp:VARIABLE(protected = true )  type: Real unreplaceable
93: $cse8.T:VARIABLE(protected = true )  type: Real unreplaceable
94: $cse8.duph:VARIABLE(protected = true )  type: Real unreplaceable
95: $cse8.duhp:VARIABLE(protected = true )  type: Real unreplaceable
96: reliefValve.pro.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 protected = true )  "Specific inner energy" type: Real
97: reliefValve.T:VARIABLE(min = 200.0 max = 6000.0 start = 290.0 unit = "K" nominal = 300.0 )  "Fluid temperature" type: Real
98: reliefValve.pro.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 protected = true )  "Specific heat capacity at constant presure" type: Real
99: reliefValve.pro.x:VARIABLE(min = 0.0 max = 1.0 unit = "1" protected = true )  "Vapor mass fraction" type: Real
100: reliefValve.rho:VARIABLE(min = 1e-9 max = 1e5 start = 998.0 unit = "kg/m3" nominal = 998.0 )  "Fluid density" type: Real
101: reliefValve.deltaP:VARIABLE(unit = "Pa" )  "Singular pressure loss" type: Real
102: reliefValve.C2.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 )  "Fluid pressure in the control volume" type: Real
103: diaphragm.deltaP:VARIABLE(unit = "Pa" )  "Pressure loss" type: Real
104: diaphragm.rho:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 )  "Fluid density" type: Real
105: diaphragm.pro.duph:VARIABLE(unit = "m3/kg" )  "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real
106: diaphragm.pro.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific heat capacity at constant presure" 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 0.003013/2.646, allocations: 3.484 MB / 0.9727 GB, free: 10.36 MB / 0.8106 GB
Error: post-optimization module createDAEmodeBDAE (simulation) failed.
Error: Internal error SimCode DAEmode: The model ThermoSysPro.Examples.SimpleExamples.TestDynamicReliefValve could not be translated