Running: ./testmodel.py --libraries=/home/hudson/saved_omc/libraries/.openmodelica/libraries --ompython_omhome=/usr ThermoSysPro_ThermoSysPro.Examples.SimpleExamples.TestThreeWayValve.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.TestThreeWayValve,tolerance=1e-06,outputFormat="empty",numberOfIntervals=5000,variableFilter="",fileNamePrefix="ThermoSysPro_ThermoSysPro.Examples.SimpleExamples.TestThreeWayValve")
translateModel(ThermoSysPro.Examples.SimpleExamples.TestThreeWayValve,tolerance=1e-06,outputFormat="empty",numberOfIntervals=5000,variableFilter="",fileNamePrefix="ThermoSysPro_ThermoSysPro.Examples.SimpleExamples.TestThreeWayValve")
Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermoSysPro 4.0.0-master/package.mo): time 0.8221/0.8221, allocations: 150.9 MB / 167.2 MB, free: 14.53 MB / 142.1 MB
Notification: Performance of FrontEnd - loaded program: time 0.0003834/0.0003835, allocations: 18.33 kB / 237.8 MB, free: 1.773 MB / 190.1 MB
Notification: Performance of FrontEnd - Absyn->SCode: time 0.05486/0.05526, allocations: 31.35 MB / 269.1 MB, free: 7.047 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.TestThreeWayValve): time 1.659/1.714, allocations: 296.8 MB / 0.5527 GB, free: 10.91 MB / 446.1 MB
Notification: Performance of NFInst.instExpressions: time 0.04119/1.755, allocations: 35.31 MB / 0.5872 GB, free: 7.457 MB / 478.1 MB
Notification: Performance of NFInst.updateImplicitVariability: time 0.000394/1.756, allocations: 8 kB / 0.5872 GB, free: 7.449 MB / 478.1 MB
[/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/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/ThreeWayValve.mo:25:3-27:68: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/ThreeWayValve.mo:28:3-30:66: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/ThreeWayValve.mo:43:3-44:54:writable] Warning: Connector C3 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/Volumes/VolumeA.mo:25:3-27:42:writable] Warning: Connector Ce1 is not balanced: The number of potential variables (4) is not equal to the number of flow variables (0).
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermoSysPro 4.0.0-master/WaterSteam/Volumes/VolumeA.mo:28:3-30:37:writable] Warning: Connector Ce2 is not balanced: The number of potential variables (4) is not equal to the number of flow variables (0).
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermoSysPro 4.0.0-master/WaterSteam/Volumes/VolumeA.mo:31:3-33:37:writable] Warning: Connector Cs1 is not balanced: The number of potential variables (4) is not equal to the number of flow variables (0).
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermoSysPro 4.0.0-master/WaterSteam/Volumes/VolumeA.mo:38:3-40:43:writable] Warning: Connector Cs2 is not balanced: The number of potential variables (4) is not equal to the number of flow variables (0).
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermoSysPro 4.0.0-master/WaterSteam/PressureLosses/PipePressureLoss.mo:35:3-37:42: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/PipePressureLoss.mo:38:3-40:37: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).
Notification: Performance of NFTyping.typeComponents: time 0.0006343/1.756, allocations: 213 kB / 0.5874 GB, free: 7.242 MB / 478.1 MB
Notification: Performance of NFTyping.typeBindings: time 0.000495/1.757, allocations: 305.5 kB / 0.5877 GB, free: 6.941 MB / 478.1 MB
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermoSysPro 4.0.0-master/Properties/WaterSteam/IF97_packages.mo:783:9-783:27:writable] Warning: cv was used before it was defined (given a value). Additional such uses may exist for the variable, but some messages were suppressed.
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermoSysPro 4.0.0-master/Properties/WaterSteam/IF97_packages.mo:850:9-850:27:writable] Warning: cv was used before it was defined (given a value). Additional such uses may exist for the variable, but some messages were suppressed.
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermoSysPro 4.0.0-master/Properties/WaterSteam/IF97_packages.mo:1088:9-1088:27:writable] Warning: cv was used before it was defined (given a value). Additional such uses may exist for the variable, but some messages were suppressed.
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermoSysPro 4.0.0-master/Properties/WaterSteamSimple/prop4_Ph.mo:69:3-69:60:writable] Warning: dh1satp was used before it was defined (given a value). Additional such uses may exist for the variable, but some messages were suppressed.
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermoSysPro 4.0.0-master/Properties/WaterSteamSimple/prop4_Ph.mo:69:3-69:60:writable] Warning: dh2satp was used before it was defined (given a value). Additional such uses may exist for the variable, but some messages were suppressed.
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermoSysPro 4.0.0-master/Properties/WaterSteamSimple/prop4_Ph_der.mo:167:3-170:49:writable] Warning: du1satp_der was used before it was defined (given a value). Additional such uses may exist for the variable, but some messages were suppressed.
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermoSysPro 4.0.0-master/Properties/WaterSteamSimple/prop4_Ph_der.mo:167:3-170:49:writable] Warning: du2satp_der was used before it was defined (given a value). Additional such uses may exist for the variable, but some messages were suppressed.
Notification: Performance of NFTyping.typeClassSections: time 0.02477/1.782, allocations: 9.922 MB / 0.5974 GB, free: 13 MB / 494.1 MB
Notification: Performance of NFFlatten.flatten: time 0.001445/1.783, allocations: 1.066 MB / 0.5984 GB, free: 11.93 MB / 494.1 MB
Notification: Performance of NFFlatten.resolveConnections: time 0.000542/1.784, allocations: 461.2 kB / 0.5989 GB, free: 11.46 MB / 494.1 MB
Notification: Performance of NFEvalConstants.evaluate: time 0.000493/1.784, allocations: 434.3 kB / 0.5993 GB, free: 11.04 MB / 494.1 MB
Notification: Performance of NFSimplifyModel.simplify: time 0.0003692/1.785, allocations: 378.2 kB / 0.5996 GB, free: 10.67 MB / 494.1 MB
Notification: Performance of NFPackage.collectConstants: time 9.471e-05/1.785, allocations: 76 kB / 0.5997 GB, free: 10.59 MB / 494.1 MB
Notification: Performance of NFFlatten.collectFunctions: time 0.03021/1.815, allocations: 17.95 MB / 0.6172 GB, free: 8.625 MB / 0.4981 GB
Notification: Performance of NFScalarize.scalarize: time 0.0002664/1.815, allocations: 183.3 kB / 0.6174 GB, free: 8.445 MB / 0.4981 GB
Notification: Performance of NFVerifyModel.verify: time 0.0005626/1.816, allocations: 453.7 kB / 0.6178 GB, free: 8 MB / 0.4981 GB
Notification: Performance of NFConvertDAE.convert: time 0.02282/1.839, allocations: 9.169 MB / 0.6268 GB, free: 14.8 MB / 0.5137 GB
Notification: Performance of FrontEnd - DAE generated: time 5.28e-06/1.839, allocations: 0 / 0.6268 GB, free: 14.8 MB / 0.5137 GB
Notification: Performance of FrontEnd: time 1.663e-06/1.839, allocations: 0 / 0.6268 GB, free: 14.8 MB / 0.5137 GB
Notification: Performance of Transformations before backend: time 1.356e-05/1.839, allocations: 0 / 0.6268 GB, free: 14.8 MB / 0.5137 GB
Notification: Model statistics after passing the front-end and creating the data structures used by the back-end:
 * Number of equations: 223
 * Number of variables: 223
Notification: Performance of Generate backend data structure: time 0.005331/1.844, allocations: 1.98 MB / 0.6287 GB, free: 12.78 MB / 0.5137 GB
Notification: Performance of prepare preOptimizeDAE: time 4.136e-05/1.844, allocations: 8.031 kB / 0.6287 GB, free: 12.77 MB / 0.5137 GB
Notification: Performance of preOpt normalInlineFunction (simulation): time 0.0001394/1.844, allocations: 98.81 kB / 0.6288 GB, free: 12.67 MB / 0.5137 GB
Notification: Performance of preOpt evaluateParameters (simulation): time 0.0005325/1.845, allocations: 448.1 kB / 0.6292 GB, free: 12.2 MB / 0.5137 GB
Notification: Performance of preOpt simplifyIfEquations (simulation): time 5.238e-05/1.845, allocations: 53.25 kB / 0.6293 GB, free: 12.14 MB / 0.5137 GB
Notification: Performance of preOpt expandDerOperator (simulation): time 8.362e-05/1.845, allocations: 60 kB / 0.6294 GB, free: 12.09 MB / 0.5137 GB
Notification: Performance of preOpt clockPartitioning (simulation): time 0.001241/1.846, allocations: 0.8606 MB / 0.6302 GB, free: 11.16 MB / 0.5137 GB
Notification: Performance of preOpt findStateOrder (simulation): time 1.981e-05/1.846, allocations: 3.938 kB / 0.6302 GB, free: 11.15 MB / 0.5137 GB
Notification: Performance of preOpt replaceEdgeChange (simulation): time 5.101e-05/1.846, allocations: 28 kB / 0.6302 GB, free: 11.12 MB / 0.5137 GB
Notification: Performance of preOpt inlineArrayEqn (simulation): time 3.3e-05/1.846, allocations: 35.97 kB / 0.6303 GB, free: 11.09 MB / 0.5137 GB
Notification: Performance of preOpt removeEqualRHS (simulation): time 0.0009054/1.847, allocations: 0.5513 MB / 0.6308 GB, free: 10.54 MB / 0.5137 GB
Warning: The model contains alias variables with redundant start and/or conflicting nominal values. It is recommended to resolve the conflicts, because otherwise the system could be hard to solve. To print the conflicting alias sets and the chosen candidates please use -d=aliasConflicts.
Notification: Performance of preOpt removeSimpleEquations (simulation): time 0.05817/1.905, allocations: 29.72 MB / 0.6598 GB, free: 9.742 MB / 0.545 GB
Notification: Performance of preOpt comSubExp (simulation): time 0.0007057/1.906, allocations: 384.1 kB / 0.6602 GB, free: 9.359 MB / 0.545 GB
Notification: Performance of preOpt resolveLoops (simulation): time 0.0003893/1.906, allocations: 275 kB / 0.6605 GB, free: 9.086 MB / 0.545 GB
Notification: Performance of preOpt evalFunc (simulation): time 0.3311/2.238, allocations: 77.73 MB / 0.7364 GB, free: 194.1 MB / 0.5919 GB
Notification: Performance of preOpt encapsulateWhenConditions (simulation): time 2.619e-05/2.238, allocations: 36.14 kB / 0.7364 GB, free: 194.1 MB / 0.5919 GB
Notification: Performance of pre-optimization done (n=91): time 3.016e-06/2.238, allocations: 0 / 0.7364 GB, free: 194.1 MB / 0.5919 GB
Notification: Performance of matching and sorting (n=91): time 0.003226/2.241, allocations: 1.27 MB / 0.7376 GB, free: 193.9 MB / 0.5919 GB
Notification: Performance of inlineWhenForInitialization (initialization): time 2.724e-05/2.241, allocations: 82.66 kB / 0.7377 GB, free: 193.8 MB / 0.5919 GB
Notification: Performance of selectInitializationVariablesDAE (initialization): time 0.0005739/2.242, allocations: 0.51 MB / 0.7382 GB, free: 193.7 MB / 0.5919 GB
Notification: Performance of collectPreVariables (initialization): time 2.989e-05/2.242, allocations: 29.64 kB / 0.7382 GB, free: 193.6 MB / 0.5919 GB
Notification: Performance of collectInitialEqns (initialization): time 0.0002044/2.242, allocations: 337.3 kB / 0.7386 GB, free: 193.5 MB / 0.5919 GB
Notification: Performance of collectInitialBindings (initialization): time 0.0001573/2.242, allocations: 300.2 kB / 0.7389 GB, free: 193.3 MB / 0.5919 GB
Notification: Performance of simplifyInitialFunctions (initialization): time 0.0001582/2.242, allocations: 121.2 kB / 0.739 GB, free: 193.3 MB / 0.5919 GB
Notification: Performance of setup shared object (initialization): time 9.549e-05/2.242, allocations: 386.3 kB / 0.7393 GB, free: 193 MB / 0.5919 GB
Notification: Performance of preBalanceInitialSystem (initialization): time 0.0003367/2.243, allocations: 205 kB / 0.7395 GB, free: 193 MB / 0.5919 GB
Notification: Performance of partitionIndependentBlocks (initialization): time 0.0004274/2.243, allocations: 363.1 kB / 0.7399 GB, free: 192.8 MB / 0.5919 GB
Notification: Performance of analyzeInitialSystem (initialization): time 0.0008318/2.244, allocations: 0.6304 MB / 0.7405 GB, free: 192.6 MB / 0.5919 GB
Notification: Performance of solveInitialSystemEqSystem (initialization): time 7.554e-06/2.244, allocations: 6.875 kB / 0.7405 GB, free: 192.6 MB / 0.5919 GB
Notification: Performance of matching and sorting (n=112) (initialization): time 0.001467/2.245, allocations: 0.8896 MB / 0.7414 GB, free: 192.5 MB / 0.5919 GB
Notification: Performance of prepare postOptimizeDAE: time 1.968e-05/2.245, allocations: 5.844 kB / 0.7414 GB, free: 192.5 MB / 0.5919 GB
Notification: Performance of postOpt simplifyComplexFunction (initialization): time 1.206e-05/2.245, allocations: 6.688 kB / 0.7414 GB, free: 192.5 MB / 0.5919 GB
Notification: Performance of postOpt tearingSystem (initialization): time 0.002867/2.248, allocations: 0.8972 MB / 0.7423 GB, free: 192.5 MB / 0.5919 GB
Notification: Performance of postOpt solveSimpleEquations (initialization): time 0.0001273/2.248, allocations: 34.5 kB / 0.7423 GB, free: 192.5 MB / 0.5919 GB
Notification: Performance of postOpt calculateStrongComponentJacobians (initialization): time 0.001227/2.25, allocations: 1.094 MB / 0.7434 GB, free: 192 MB / 0.5919 GB
Notification: Performance of postOpt simplifyAllExpressions (initialization): time 0.0003299/2.25, allocations: 72.31 kB / 0.7434 GB, free: 191.9 MB / 0.5919 GB
Notification: Performance of postOpt collapseArrayExpressions (initialization): time 3.637e-05/2.25, allocations: 22.09 kB / 0.7435 GB, free: 191.9 MB / 0.5919 GB
Notification: Model statistics after passing the back-end for initialization:
 * Number of independent subsystems: 18
 * Number of states: 0 ()
 * Number of discrete variables: 14 (PuitsP2.C.a,threeWayValve.PerteDP1.C2.b,threeWayValve.PerteDP1.C1.a,threeWayValve.VolumeA1.Cs2.b,threeWayValve.VolumeA1.Cs1.b,threeWayValve.VolumeA1.Ce2.a,threeWayValve.VolumeA1.Ce1.a,threeWayValve.Valve2.C2.b,threeWayValve.Valve2.C1.a,threeWayValve.Valve1.C2.b,threeWayValve.Valve1.C1.a,PuitsP1.C.a,SourceP1.C.b,threeWayValve.VolumeA1.Ce2.b)
 * Number of discrete states: 0 ()
 * Number of clocked states: 0 ()
 * Top-level inputs: 0
Notification: Strong component statistics for initialization (29):
 * Single equations (assignments): 25
 * Array equations: 0
 * Algorithm blocks: 0
 * Record equations: 3
 * 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
   {(7,14)}
Notification: Performance of prepare postOptimizeDAE: time 0.0002646/2.25, allocations: 233.1 kB / 0.7437 GB, free: 191.8 MB / 0.5919 GB
Notification: Performance of postOpt lateInlineFunction (simulation): time 0.0001001/2.25, allocations: 65.81 kB / 0.7437 GB, free: 191.8 MB / 0.5919 GB
Notification: Performance of postOpt wrapFunctionCalls (simulation): time 0.002126/2.252, allocations: 2.14 MB / 0.7458 GB, free: 191.4 MB / 0.5919 GB
Notification: Performance of postOpt simplifysemiLinear (simulation): time 6.563e-06/2.253, allocations: 1.125 kB / 0.7458 GB, free: 191.4 MB / 0.5919 GB
Notification: Performance of postOpt simplifyComplexFunction (simulation): time 2.154e-06/2.253, allocations: 0 / 0.7458 GB, free: 191.4 MB / 0.5919 GB
Notification: Performance of postOpt removeConstants (simulation): time 0.0002365/2.253, allocations: 189.4 kB / 0.746 GB, free: 191.2 MB / 0.5919 GB
Notification: Performance of postOpt simplifyTimeIndepFuncCalls (simulation): time 0.0001016/2.253, allocations: 26.72 kB / 0.746 GB, free: 191.2 MB / 0.5919 GB
Notification: Performance of postOpt simplifyAllExpressions (simulation): time 0.0002421/2.253, allocations: 14.36 kB / 0.746 GB, free: 191.2 MB / 0.5919 GB
Notification: Performance of postOpt findZeroCrossings (simulation): time 7.633e-05/2.253, allocations: 19.38 kB / 0.7461 GB, free: 191.2 MB / 0.5919 GB
[/var/lib/jenkins1/ws/OpenModelicaLibraryTestingWork/OpenModelica/OMCompiler/Compiler/BackEnd/DAEMode.mo:528:7-530:90:writable] Error: Internal error DAEMode.traverserStrongComponents failed on equation:
1/1 (10): ThermoSysPro.Properties.WaterSteam.Common.ThermoProperties_ph(threeWayValve.Valve1.T, threeWayValve.Valve1.rho, threeWayValve.Valve1.pro.u, threeWayValve.Valve1.pro.s, threeWayValve.Valve1.pro.cp, threeWayValve.Valve1.pro.ddhp, threeWayValve.Valve1.pro.ddph, threeWayValve.Valve1.pro.duph, threeWayValve.Valve1.pro.duhp, threeWayValve.Valve1.pro.x) = $cse6

Variables:
1: threeWayValve.Valve1.pro.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific heat capacity at constant presure" type: Real
2: threeWayValve.Valve1.pro.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 )  "Specific inner energy" type: Real
3: threeWayValve.Valve1.pro.ddhp:VARIABLE(unit = "kg.s2/m5" )  "Derivative of density wrt. specific enthalpy at constant pressure" type: Real
4: threeWayValve.Valve1.pro.x:VARIABLE(min = 0.0 max = 1.0 unit = "1" )  "Vapor mass fraction" type: Real
5: threeWayValve.Valve1.pro.duph:VARIABLE(unit = "m3/kg" )  "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real
6: threeWayValve.Valve1.pro.ddph:VARIABLE(unit = "s2/m2" )  "Derivative of density wrt. pressure at constant specific enthalpy" type: Real
7: threeWayValve.Valve1.T:VARIABLE(min = 200.0 max = 6000.0 start = 290.0 unit = "K" nominal = 300.0 )  "Fluid temperature" type: Real
8: threeWayValve.Valve1.pro.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific entropy" type: Real
9: threeWayValve.Valve1.rho:VARIABLE(min = 1e-9 max = 1e5 start = 998.0 unit = "kg/m3" nominal = 998.0 )  "Fluid density" type: Real
10: threeWayValve.Valve1.pro.duhp:VARIABLE(unit = "1" )  "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real
[/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): threeWayValve.Valve2.deltaP * threeWayValve.Valve2.Cv * abs(threeWayValve.Valve2.Cv) = 1.733e12 * $cse5 / threeWayValve.Valve2.rho ^ 2.0
2/2 (1): $cse5 = ThermoSysPro.Functions.ThermoSquare(PuitsP1.Q, threeWayValve.Valve2.eps)
3/3 (1): 0.0 = if PuitsP1.Q > 0.0 then threeWayValve.Valve2.h - threeWayValve.VolumeA1.h else threeWayValve.Valve2.h - PuitsP1.h
4/4 (10): $cse4 = ThermoSysPro.Properties.Fluid.Ph(threeWayValve.Valve2.Pm, threeWayValve.Valve2.h, threeWayValve.Valve2.mode, threeWayValve.Valve2.fluid)
5/14 (10): ThermoSysPro.Properties.WaterSteam.Common.ThermoProperties_ph(threeWayValve.Valve2.T, threeWayValve.Valve2.rho, threeWayValve.Valve2.pro.u, threeWayValve.Valve2.pro.s, threeWayValve.Valve2.pro.cp, threeWayValve.Valve2.pro.ddhp, threeWayValve.Valve2.pro.ddph, threeWayValve.Valve2.pro.duph, threeWayValve.Valve2.pro.duhp, threeWayValve.Valve2.pro.x) = $cse4
6/24 (1): 0.0 = SourceP1.Q + (-PuitsP1.Q) - PuitsP2.Q
7/25 (1): $cse2 = ThermoSysPro.Functions.ThermoSquare(SourceP1.Q, threeWayValve.PerteDP1.eps)
8/26 (1): threeWayValve.PerteDP1.deltaPf = threeWayValve.PerteDP1.K * $cse2 / threeWayValve.PerteDP1.rho
9/27 (1): threeWayValve.PerteDP1.deltaP = threeWayValve.PerteDP1.deltaPf + threeWayValve.PerteDP1.deltaPg
10/28 (1): threeWayValve.PerteDP1.deltaPg = 9.80665 * threeWayValve.PerteDP1.rho * (threeWayValve.PerteDP1.z2 - threeWayValve.PerteDP1.z1)
11/29 (10): $cse1 = ThermoSysPro.Properties.Fluid.Ph(threeWayValve.PerteDP1.Pm, threeWayValve.PerteDP1.h, threeWayValve.PerteDP1.mode, threeWayValve.PerteDP1.fluid)
12/39 (10): ThermoSysPro.Properties.WaterSteam.Common.ThermoProperties_ph(threeWayValve.PerteDP1.T, threeWayValve.PerteDP1.rho, threeWayValve.PerteDP1.pro.u, threeWayValve.PerteDP1.pro.s, threeWayValve.PerteDP1.pro.cp, threeWayValve.PerteDP1.pro.ddhp, threeWayValve.PerteDP1.pro.ddph, threeWayValve.PerteDP1.pro.duph, threeWayValve.PerteDP1.pro.duhp, threeWayValve.PerteDP1.pro.x) = $cse1
13/49 (1): threeWayValve.PerteDP1.Pm = 0.5 * (SourceP1.P0 + threeWayValve.VolumeA1.P)
14/50 (1): threeWayValve.Valve1.deltaP = threeWayValve.VolumeA1.P - PuitsP2.P0
15/51 (1): threeWayValve.Valve1.deltaP * threeWayValve.Valve1.Cv * abs(threeWayValve.Valve1.Cv) = 1.733e12 * $cse7 / threeWayValve.Valve1.rho ^ 2.0
16/52 (1): $cse7 = ThermoSysPro.Functions.ThermoSquare(PuitsP2.Q, threeWayValve.Valve1.eps)
17/53 (1): 0.0 = if PuitsP2.Q > 0.0 then threeWayValve.Valve1.h - threeWayValve.VolumeA1.h else threeWayValve.Valve1.h - PuitsP2.h
18/54 (10): $cse6 = ThermoSysPro.Properties.Fluid.Ph(threeWayValve.Valve1.Pm, threeWayValve.Valve1.h, threeWayValve.Valve1.mode, threeWayValve.Valve1.fluid)
19/64 (10): ThermoSysPro.Properties.WaterSteam.Common.ThermoProperties_ph(threeWayValve.Valve1.T, threeWayValve.Valve1.rho, threeWayValve.Valve1.pro.u, threeWayValve.Valve1.pro.s, threeWayValve.Valve1.pro.cp, threeWayValve.Valve1.pro.ddhp, threeWayValve.Valve1.pro.ddph, threeWayValve.Valve1.pro.duph, threeWayValve.Valve1.pro.duhp, threeWayValve.Valve1.pro.x) = $cse6
20/74 (1): threeWayValve.Valve1.Pm = 0.5 * (threeWayValve.VolumeA1.P + PuitsP2.P0)
21/75 (1): threeWayValve.Valve2.deltaP = threeWayValve.VolumeA1.P - PuitsP1.P0
22/76 (1): threeWayValve.Valve2.Pm = 0.5 * (threeWayValve.VolumeA1.P + PuitsP1.P0)
23/77 (1): SourceP1.P0 - threeWayValve.VolumeA1.P = threeWayValve.PerteDP1.deltaP
24/78 (1): 0.0 = if SourceP1.Q > 0.0 then threeWayValve.PerteDP1.h - SourceP1.h else threeWayValve.PerteDP1.h - threeWayValve.VolumeA1.h

Variables:
1: threeWayValve.PerteDP1.h:VARIABLE(start = 1e5 unit = "J/kg" )  "Fluid specific enthalpy" type: Real
2: threeWayValve.PerteDP1.deltaP:VARIABLE(unit = "Pa" )  "Total pressure loss" type: Real
3: threeWayValve.Valve2.Pm:VARIABLE(min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 )  "Fluid average pressure" type: Real
4: threeWayValve.Valve2.deltaP:VARIABLE(unit = "Pa" )  "Singular pressure loss" type: Real
5: threeWayValve.Valve1.Pm:VARIABLE(min = 0.0 start = 2e5 unit = "Pa" nominal = 1e5 )  "Fluid average pressure" type: Real
6: threeWayValve.Valve1.pro.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific heat capacity at constant presure" type: Real
7: threeWayValve.Valve1.pro.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 )  "Specific inner energy" type: Real
8: threeWayValve.Valve1.pro.ddhp:VARIABLE(unit = "kg.s2/m5" )  "Derivative of density wrt. specific enthalpy at constant pressure" type: Real
9: threeWayValve.Valve1.pro.x:VARIABLE(min = 0.0 max = 1.0 unit = "1" )  "Vapor mass fraction" type: Real
10: threeWayValve.Valve1.pro.duph:VARIABLE(unit = "m3/kg" )  "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real
11: threeWayValve.Valve1.pro.ddph:VARIABLE(unit = "s2/m2" )  "Derivative of density wrt. pressure at constant specific enthalpy" type: Real
12: threeWayValve.Valve1.T:VARIABLE(min = 200.0 max = 6000.0 start = 290.0 unit = "K" nominal = 300.0 )  "Fluid temperature" type: Real
13: threeWayValve.Valve1.pro.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific entropy" type: Real
14: threeWayValve.Valve1.rho:VARIABLE(min = 1e-9 max = 1e5 start = 998.0 unit = "kg/m3" nominal = 998.0 )  "Fluid density" type: Real
15: threeWayValve.Valve1.pro.duhp:VARIABLE(unit = "1" )  "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real
16: $cse6.x:VARIABLE(protected = true )  type: Real unreplaceable
17: $cse6.ddhp:VARIABLE(protected = true )  type: Real unreplaceable
18: $cse6.duph:VARIABLE(protected = true )  type: Real unreplaceable
19: $cse6.u:VARIABLE(protected = true )  type: Real unreplaceable
20: $cse6.d:VARIABLE(protected = true )  type: Real unreplaceable
21: $cse6.duhp:VARIABLE(protected = true )  type: Real unreplaceable
22: $cse6.ddph:VARIABLE(protected = true )  type: Real unreplaceable
23: $cse6.T:VARIABLE(protected = true )  type: Real unreplaceable
24: $cse6.cp:VARIABLE(protected = true )  type: Real unreplaceable
25: $cse6.s:VARIABLE(protected = true )  type: Real unreplaceable
26: threeWayValve.Valve1.h:VARIABLE(start = 1e5 unit = "J/kg" )  "Fluid specific enthalpy" type: Real
27: PuitsP2.Q:VARIABLE(start = 500.0 unit = "kg/s" )  "Mass flow rate" type: Real
28: $cse7:VARIABLE(protected = true )  type: Real unreplaceable
29: threeWayValve.Valve1.deltaP:VARIABLE(unit = "Pa" )  "Singular pressure loss" type: Real
30: threeWayValve.VolumeA1.P:VARIABLE(min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 )  "Fluid pressure" type: Real
31: threeWayValve.PerteDP1.pro.x:VARIABLE(min = 0.0 max = 1.0 unit = "1" )  "Vapor mass fraction" type: Real
32: threeWayValve.PerteDP1.pro.ddhp:VARIABLE(unit = "kg.s2/m5" )  "Derivative of density wrt. specific enthalpy at constant pressure" type: Real
33: threeWayValve.PerteDP1.pro.duph:VARIABLE(unit = "m3/kg" )  "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real
34: $cse1.duhp:VARIABLE(protected = true )  type: Real unreplaceable
35: $cse1.x:VARIABLE(protected = true )  type: Real unreplaceable
36: threeWayValve.PerteDP1.Pm:VARIABLE(min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 )  "Average fluid pressure" type: Real
37: $cse1.u:VARIABLE(protected = true )  type: Real unreplaceable
38: $cse1.T:VARIABLE(protected = true )  type: Real unreplaceable
39: $cse1.d:VARIABLE(protected = true )  type: Real unreplaceable
40: $cse1.duph:VARIABLE(protected = true )  type: Real unreplaceable
41: $cse1.ddhp:VARIABLE(protected = true )  type: Real unreplaceable
42: $cse1.s:VARIABLE(protected = true )  type: Real unreplaceable
43: $cse1.cp:VARIABLE(protected = true )  type: Real unreplaceable
44: $cse1.ddph:VARIABLE(protected = true )  type: Real unreplaceable
45: threeWayValve.PerteDP1.pro.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 )  "Specific inner energy" type: Real
46: threeWayValve.PerteDP1.pro.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific heat capacity at constant presure" type: Real
47: threeWayValve.PerteDP1.pro.ddph:VARIABLE(unit = "s2/m2" )  "Derivative of density wrt. pressure at constant specific enthalpy" type: Real
48: threeWayValve.PerteDP1.pro.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific entropy" type: Real
49: threeWayValve.PerteDP1.pro.duhp:VARIABLE(unit = "1" )  "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real
50: threeWayValve.PerteDP1.T:VARIABLE(min = 200.0 max = 6000.0 start = 290.0 unit = "K" nominal = 300.0 )  "Fluid temperature" type: Real
51: threeWayValve.PerteDP1.rho:VARIABLE(min = 1e-9 max = 1e5 start = 998.0 unit = "kg/m3" nominal = 998.0 )  "Fluid density" type: Real
52: threeWayValve.PerteDP1.deltaPg:VARIABLE(unit = "Pa" )  "Gravity pressure loss" type: Real
53: threeWayValve.PerteDP1.deltaPf:VARIABLE(unit = "Pa" )  "Friction pressure loss" type: Real
54: $cse2:VARIABLE(protected = true )  type: Real unreplaceable
55: SourceP1.Q:VARIABLE(start = 100.0 unit = "kg/s" )  "Mass flow rate" type: Real
56: threeWayValve.Valve2.pro.ddph:VARIABLE(unit = "s2/m2" )  "Derivative of density wrt. pressure at constant specific enthalpy" type: Real
57: threeWayValve.Valve2.pro.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific heat capacity at constant presure" type: Real
58: threeWayValve.Valve2.pro.duhp:VARIABLE(unit = "1" )  "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real
59: threeWayValve.Valve2.pro.x:VARIABLE(min = 0.0 max = 1.0 unit = "1" )  "Vapor mass fraction" type: Real
60: threeWayValve.Valve2.rho:VARIABLE(min = 1e-9 max = 1e5 start = 998.0 unit = "kg/m3" nominal = 998.0 )  "Fluid density" type: Real
61: threeWayValve.Valve2.pro.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 )  "Specific inner energy" type: Real
62: threeWayValve.Valve2.pro.duph:VARIABLE(unit = "m3/kg" )  "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real
63: threeWayValve.Valve2.T:VARIABLE(min = 200.0 max = 6000.0 start = 290.0 unit = "K" nominal = 300.0 )  "Fluid temperature" type: Real
64: threeWayValve.Valve2.pro.ddhp:VARIABLE(unit = "kg.s2/m5" )  "Derivative of density wrt. specific enthalpy at constant pressure" type: Real
65: threeWayValve.Valve2.pro.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific entropy" type: Real
66: $cse4.u:VARIABLE(protected = true )  type: Real unreplaceable
67: $cse4.duhp:VARIABLE(protected = true )  type: Real unreplaceable
68: $cse4.ddph:VARIABLE(protected = true )  type: Real unreplaceable
69: $cse4.ddhp:VARIABLE(protected = true )  type: Real unreplaceable
70: $cse4.d:VARIABLE(protected = true )  type: Real unreplaceable
71: $cse4.x:VARIABLE(protected = true )  type: Real unreplaceable
72: $cse4.s:VARIABLE(protected = true )  type: Real unreplaceable
73: $cse4.duph:VARIABLE(protected = true )  type: Real unreplaceable
74: $cse4.cp:VARIABLE(protected = true )  type: Real unreplaceable
75: $cse4.T:VARIABLE(protected = true )  type: Real unreplaceable
76: threeWayValve.Valve2.h:VARIABLE(start = 1e5 unit = "J/kg" )  "Fluid specific enthalpy" type: Real
77: PuitsP1.Q:VARIABLE(start = 500.0 unit = "kg/s" )  "Mass flow rate" type: Real
78: $cse5:VARIABLE(protected = true )  type: Real unreplaceable
[/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 0.001761/2.255, allocations: 2.364 MB / 0.7484 GB, free: 189 MB / 0.5919 GB
Error: post-optimization module createDAEmodeBDAE (simulation) failed.
Error: Internal error SimCode DAEmode: The model ThermoSysPro.Examples.SimpleExamples.TestThreeWayValve could not be translated