Running: ./testmodel.py --libraries=/home/hudson/saved_omc/libraries/.openmodelica/libraries --ompython_omhome=/usr ThermoSysPro_ThermoSysPro.Fluid.Examples.SimpleExamples.TestDynamicCondenser.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.Fluid.Examples.SimpleExamples.TestDynamicCondenser,tolerance=1e-06,outputFormat="empty",numberOfIntervals=5000,variableFilter="",fileNamePrefix="ThermoSysPro_ThermoSysPro.Fluid.Examples.SimpleExamples.TestDynamicCondenser")
translateModel(ThermoSysPro.Fluid.Examples.SimpleExamples.TestDynamicCondenser,tolerance=1e-06,outputFormat="empty",numberOfIntervals=5000,variableFilter="",fileNamePrefix="ThermoSysPro_ThermoSysPro.Fluid.Examples.SimpleExamples.TestDynamicCondenser")
Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermoSysPro 4.0.0-master/package.mo): time 0.8095/0.8095, allocations: 150.9 MB / 167.2 MB, free: 14.54 MB / 142.1 MB
Notification: Performance of FrontEnd - loaded program: time 0.0003307/0.0003307, allocations: 18.78 kB / 237.8 MB, free: 1.777 MB / 190.1 MB
Notification: Performance of FrontEnd - Absyn->SCode: time 0.05816/0.0585, allocations: 31.35 MB / 269.1 MB, free: 7.039 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.Fluid.Examples.SimpleExamples.TestDynamicCondenser): time 1.668/1.726, allocations: 302.7 MB / 0.5584 GB, free: 5.047 MB / 446.1 MB
Notification: Performance of NFInst.instExpressions: time 0.5489/2.275, allocations: 212.1 MB / 0.7656 GB, free: 15.34 MB / 0.6075 GB
Notification: Performance of NFInst.updateImplicitVariability: time 0.001617/2.277, allocations: 42.06 kB / 0.7656 GB, free: 15.34 MB / 0.6075 GB
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermoSysPro 4.0.0-master/Fluid/Machines/StaticCentrifugalPump.mo:63:3-64:67:writable] Warning: Connector C1 is not balanced: The number of potential variables (9) is not equal to the number of flow variables (0).
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermoSysPro 4.0.0-master/Fluid/Machines/StaticCentrifugalPump.mo:65:3-66:65:writable] Warning: Connector C2 is not balanced: The number of potential variables (9) is not equal to the number of flow variables (0).
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermoSysPro 4.0.0-master/Fluid/Machines/StodolaTurbine.mo:65:3-66:54:writable] Warning: Connector Ce is not balanced: The number of potential variables (9) is not equal to the number of flow variables (0).
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermoSysPro 4.0.0-master/Fluid/Machines/StodolaTurbine.mo:67:3-68:52:writable] Warning: Connector Cs is not balanced: The number of potential variables (9) is not equal to the number of flow variables (0).
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermoSysPro 4.0.0-master/Fluid/Machines/StodolaTurbine.mo:72:3-76:23:writable] Warning: Connector M is not balanced: The number of potential variables (2) is not equal to the number of flow variables (0).
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermoSysPro 4.0.0-master/Fluid/Volumes/TwoPhaseCavityOnePipe.mo:144:3-145:65:writable] Warning: Connector CvBP is not balanced: The number of potential variables (9) is not equal to the number of flow variables (0).
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermoSysPro 4.0.0-master/Fluid/Volumes/TwoPhaseCavityOnePipe.mo:146:3-147:69:writable] Warning: Connector Cl is not balanced: The number of potential variables (9) is not equal to the number of flow variables (0).
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermoSysPro 4.0.0-master/Fluid/Volumes/TwoPhaseCavityOnePipe.mo:158:3-159:67:writable] Warning: Connector Ce is not balanced: The number of potential variables (9) is not equal to the number of flow variables (0).
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermoSysPro 4.0.0-master/Fluid/Volumes/TwoPhaseCavityOnePipe.mo:166:3-167:67:writable] Warning: Connector CvGCT is not balanced: The number of potential variables (9) is not equal to the number of flow variables (0).
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermoSysPro 4.0.0-master/Fluid/HeatExchangers/DynamicOnePhaseFlowPipe.mo:150:3-151:67:writable] Warning: Connector C1 is not balanced: The number of potential variables (9) is not equal to the number of flow variables (0).
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermoSysPro 4.0.0-master/Fluid/HeatExchangers/DynamicOnePhaseFlowPipe.mo:152:3-153:65:writable] Warning: Connector C2 is not balanced: The number of potential variables (9) is not equal to the number of flow variables (0).
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermoSysPro 4.0.0-master/Fluid/HeatExchangers/DynamicCondenser.mo:83:3-84:65:writable] Warning: Connector C1vap is not balanced: The number of potential variables (9) is not equal to the number of flow variables (0).
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermoSysPro 4.0.0-master/Fluid/HeatExchangers/DynamicCondenser.mo:85:3-87:16:writable] Warning: Connector C2ex is not balanced: The number of potential variables (9) is not equal to the number of flow variables (0).
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermoSysPro 4.0.0-master/Fluid/HeatExchangers/DynamicCondenser.mo:88:3-89:74:writable] Warning: Connector Ce1 is not balanced: The number of potential variables (9) is not equal to the number of flow variables (0).
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermoSysPro 4.0.0-master/Fluid/HeatExchangers/DynamicCondenser.mo:90:3-91:72:writable] Warning: Connector Ce2 is not balanced: The number of potential variables (9) is not equal to the number of flow variables (0).
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermoSysPro 4.0.0-master/Fluid/HeatExchangers/DynamicCondenser.mo:96:3-98:57:writable] Warning: Connector C1 is not balanced: The number of potential variables (9) is not equal to the number of flow variables (0).
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermoSysPro 4.0.0-master/Fluid/HeatExchangers/DynamicCondenser.mo:111:3-113:58:writable] Warning: Connector C2vap is not balanced: The number of potential variables (9) is not equal to the number of flow variables (0).
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermoSysPro 4.0.0-master/Fluid/BoundaryConditions/SinkP.mo:46:3-47:67:writable] Warning: Connector C is not balanced: The number of potential variables (9) is not equal to the number of flow variables (0).
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermoSysPro 4.0.0-master/Fluid/BoundaryConditions/SourceQ.mo:62:3-63:65:writable] Warning: Connector C is not balanced: The number of potential variables (9) is not equal to the number of flow variables (0).
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermoSysPro 4.0.0-master/Fluid/Volumes/VolumeATh.mo:104:3-105:67:writable] Warning: Connector Ce1 is not balanced: The number of potential variables (9) is not equal to the number of flow variables (0).
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermoSysPro 4.0.0-master/Fluid/Volumes/VolumeATh.mo:106:3-108:57:writable] Warning: Connector Ce2 is not balanced: The number of potential variables (9) is not equal to the number of flow variables (0).
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermoSysPro 4.0.0-master/Fluid/Volumes/VolumeATh.mo:109:3-110:73:writable] Warning: Connector Cs1 is not balanced: The number of potential variables (9) is not equal to the number of flow variables (0).
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermoSysPro 4.0.0-master/Fluid/Volumes/VolumeATh.mo:111:3-112:75:writable] Warning: Connector Cs2 is not balanced: The number of potential variables (9) is not equal to the number of flow variables (0).
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermoSysPro 4.0.0-master/Fluid/BoundaryConditions/SourceQ.mo:62:3-63:65:writable] Warning: Connector C is not balanced: The number of potential variables (9) is not equal to the number of flow variables (0).
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermoSysPro 4.0.0-master/Fluid/PressureLosses/SingularPressureLoss.mo:27:3-28:67:writable] Warning: Connector C1 is not balanced: The number of potential variables (9) is not equal to the number of flow variables (0).
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermoSysPro 4.0.0-master/Fluid/PressureLosses/SingularPressureLoss.mo:29:3-30:65:writable] Warning: Connector C2 is not balanced: The number of potential variables (9) is not equal to the number of flow variables (0).
Notification: Performance of NFTyping.typeComponents: time 0.001713/2.278, allocations: 0.5949 MB / 0.7662 GB, free: 15.33 MB / 0.6075 GB
Notification: Performance of NFTyping.typeBindings: time 0.003016/2.281, allocations: 1.165 MB / 0.7674 GB, free: 15.29 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.
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermoSysPro 4.0.0-master/Properties/Fluid/derDensity_derP_derh.mo:63:5-63:84:writable] Warning: T 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:1445:9-1445:35:writable] Warning: h 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_Ps.mo:71:3-71:60: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_Ps.mo:71:3-71:60: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.
Notification: Performance of NFTyping.typeClassSections: time 0.05853/2.34, allocations: 18.79 MB / 0.7857 GB, free: 10.94 MB / 0.6075 GB
Notification: Performance of NFFlatten.flatten: time 0.01026/2.35, allocations: 9.525 MB / 0.795 GB, free: 8.766 MB / 0.6075 GB
Notification: Performance of NFFlatten.resolveConnections: time 0.005505/2.356, allocations: 3.493 MB / 0.7984 GB, free: 6.863 MB / 0.6075 GB
Notification: Performance of NFEvalConstants.evaluate: time 0.005423/2.361, allocations: 2.997 MB / 0.8014 GB, free: 5.434 MB / 0.6075 GB
Notification: Performance of NFSimplifyModel.simplify: time 0.005571/2.367, allocations: 3.373 MB / 0.8046 GB, free: 3.352 MB / 0.6075 GB
Notification: Performance of NFPackage.collectConstants: time 0.002434/2.369, allocations: 0.8056 MB / 0.8054 GB, free: 3.352 MB / 0.6075 GB
Notification: Performance of NFFlatten.collectFunctions: time 0.06264/2.432, allocations: 31.14 MB / 0.8358 GB, free: 8.422 MB / 0.6387 GB
Notification: Performance of NFScalarize.scalarize: time 0.003451/2.435, allocations: 2.306 MB / 0.8381 GB, free: 6.145 MB / 0.6387 GB
Notification: Performance of NFVerifyModel.verify: time 0.005929/2.441, allocations: 3.187 MB / 0.8412 GB, free: 2.977 MB / 0.6387 GB
Notification: Performance of NFConvertDAE.convert: time 0.05191/2.493, allocations: 22.67 MB / 0.8633 GB, free: 13.35 MB / 0.67 GB
Notification: Performance of FrontEnd - DAE generated: time 6.773e-06/2.493, allocations: 0 / 0.8633 GB, free: 13.35 MB / 0.67 GB
Notification: Performance of FrontEnd: time 2.775e-06/2.493, allocations: 0 / 0.8633 GB, free: 13.35 MB / 0.67 GB
Notification: Performance of Transformations before backend: time 0.0002809/2.494, allocations: 0 / 0.8633 GB, free: 13.35 MB / 0.67 GB
Notification: Model statistics after passing the front-end and creating the data structures used by the back-end:
 * Number of equations: 1245
 * Number of variables: 1245
Notification: Performance of Generate backend data structure: time 0.02602/2.52, allocations: 7.656 MB / 0.8708 GB, free: 5.637 MB / 0.67 GB
Notification: Performance of prepare preOptimizeDAE: time 6.111e-05/2.52, allocations: 12.03 kB / 0.8708 GB, free: 5.625 MB / 0.67 GB
Notification: Performance of preOpt normalInlineFunction (simulation): time 0.002882/2.523, allocations: 0.5253 MB / 0.8713 GB, free: 5.094 MB / 0.67 GB
Notification: Performance of preOpt evaluateParameters (simulation): time 0.00573/2.528, allocations: 2.538 MB / 0.8738 GB, free: 2.527 MB / 0.67 GB
Notification: Performance of preOpt simplifyIfEquations (simulation): time 0.0008564/2.529, allocations: 0.7049 MB / 0.8745 GB, free: 1.746 MB / 0.67 GB
Notification: Performance of preOpt expandDerOperator (simulation): time 0.001902/2.531, allocations: 475.8 kB / 0.875 GB, free: 1.281 MB / 0.67 GB
Notification: Performance of preOpt clockPartitioning (simulation): time 0.01912/2.55, allocations: 7.843 MB / 0.8826 GB, free: 8.984 MB / 0.6856 GB
Notification: Performance of preOpt findStateOrder (simulation): time 0.0002306/2.551, allocations: 19.81 kB / 0.8826 GB, free: 8.965 MB / 0.6856 GB
Notification: Performance of preOpt replaceEdgeChange (simulation): time 0.00183/2.553, allocations: 192 kB / 0.8828 GB, free: 8.777 MB / 0.6856 GB
Notification: Performance of preOpt inlineArrayEqn (simulation): time 0.0001802/2.553, allocations: 147.9 kB / 0.883 GB, free: 8.633 MB / 0.6856 GB
Notification: Performance of preOpt removeEqualRHS (simulation): time 0.02662/2.579, allocations: 14.89 MB / 0.8975 GB, free: 9.727 MB / 0.7012 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 0.066/2.645, allocations: 41.13 MB / 0.9377 GB, free: 14.18 MB / 0.7481 GB
Notification: Performance of preOpt comSubExp (simulation): time 0.02386/2.669, allocations: 7.243 MB / 0.9448 GB, free: 6.941 MB / 0.7481 GB
Notification: Performance of preOpt resolveLoops (simulation): time 0.00766/2.677, allocations: 3.628 MB / 0.9483 GB, free: 3.301 MB / 0.7481 GB
Notification: Performance of preOpt evalFunc (simulation): time 1.834/4.511, allocations: 0.7362 GB / 1.685 GB, free: 142.7 MB / 0.92 GB
Notification: Performance of preOpt encapsulateWhenConditions (simulation): time 0.0001139/4.511, allocations: 79.05 kB / 1.685 GB, free: 142.7 MB / 0.92 GB
Notification: Performance of pre-optimization done (n=519): time 6.432e-06/4.511, allocations: 0 / 1.685 GB, free: 142.7 MB / 0.92 GB
Notification: Performance of matching and sorting (n=521): time 0.05695/4.568, allocations: 24.56 MB / 1.709 GB, free: 117.5 MB / 0.92 GB
Notification: Performance of inlineWhenForInitialization (initialization): time 3.835e-05/4.568, allocations: 94.78 kB / 1.709 GB, free: 117.4 MB / 0.92 GB
Notification: Performance of selectInitializationVariablesDAE (initialization): time 0.002735/4.571, allocations: 2.193 MB / 1.711 GB, free: 115.2 MB / 0.92 GB
Notification: Performance of collectPreVariables (initialization): time 0.001665/4.572, allocations: 101.7 kB / 1.711 GB, free: 115.1 MB / 0.92 GB
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermoSysPro 4.0.0-master/Thermal/BoundaryConditions/HeatSource.mo:5:3-6:72:writable] Warning: The parameter heatSource.W0[1] has fixed = false and a binding equation heatSource.W0[1] = 2e6, which is probably redundant.
Setting fixed = false usually means there is an additional initial equation to determine the parameter value. The binding was ignored by old Modelica tools, but this is not according to the Modelica specification. Please remove the parameter binding, or bind the parameter to another parameter with fixed = false and no binding.
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermoSysPro 4.0.0-master/Fluid/Machines/StaticCentrifugalPump.mo:24:3-25:69:writable] Warning: The parameter staticCentrifugalPump.a1 has fixed = false and a binding equation staticCentrifugalPump.a1 = -88.67, which is probably redundant.
Setting fixed = false usually means there is an additional initial equation to determine the parameter value. The binding was ignored by old Modelica tools, but this is not according to the Modelica specification. Please remove the parameter binding, or bind the parameter to another parameter with fixed = false and no binding.
Notification: Performance of collectInitialEqns (initialization): time 0.001057/4.574, allocations: 1.648 MB / 1.713 GB, free: 113.5 MB / 0.92 GB
Notification: Performance of collectInitialBindings (initialization): time 0.002655/4.576, allocations: 1.836 MB / 1.714 GB, free: 111.6 MB / 0.92 GB
Notification: Performance of simplifyInitialFunctions (initialization): time 0.00207/4.578, allocations: 1.128 MB / 1.715 GB, free: 110.5 MB / 0.92 GB
Notification: Performance of setup shared object (initialization): time 5.971e-05/4.578, allocations: 309.1 kB / 1.716 GB, free: 110.2 MB / 0.92 GB
Notification: Performance of preBalanceInitialSystem (initialization): time 0.005732/4.584, allocations: 3.729 MB / 1.719 GB, free: 106.5 MB / 0.92 GB
Notification: Performance of partitionIndependentBlocks (initialization): time 0.006814/4.591, allocations: 5.221 MB / 1.724 GB, free: 100.6 MB / 0.92 GB
Notification: It was not possible to check the given initialization system for consistency symbolically, because the relevant equations are part of an algebraic loop. This is not supported yet.
Notification: Performance of analyzeInitialSystem (initialization): time 0.1352/4.726, allocations: 39.13 MB / 1.763 GB, free: 61.59 MB / 0.92 GB
Notification: Performance of solveInitialSystemEqSystem (initialization): time 3.374e-05/4.726, allocations: 12 kB / 1.763 GB, free: 61.57 MB / 0.92 GB
Notification: Performance of matching and sorting (n=781) (initialization): time 0.02538/4.752, allocations: 12.84 MB / 1.775 GB, free: 48.89 MB / 0.92 GB
Notification: Performance of prepare postOptimizeDAE: time 5.067e-05/4.752, allocations: 24.66 kB / 1.775 GB, free: 48.87 MB / 0.92 GB
Notification: Performance of postOpt simplifyComplexFunction (initialization): time 7.144e-05/4.752, allocations: 44.88 kB / 1.775 GB, free: 48.83 MB / 0.92 GB
Notification: Performance of postOpt tearingSystem (initialization): time 0.05716/4.809, allocations: 12.69 MB / 1.788 GB, free: 36.18 MB / 0.92 GB
Notification: Performance of postOpt solveSimpleEquations (initialization): time 0.003142/4.812, allocations: 0.693 MB / 1.788 GB, free: 35.54 MB / 0.92 GB
Notification: Performance of postOpt calculateStrongComponentJacobians (initialization): time 0.0298/4.842, allocations: 30.35 MB / 1.818 GB, free: 3.547 MB / 0.92 GB
Notification: Performance of postOpt simplifyAllExpressions (initialization): time 0.005264/4.847, allocations: 248.5 kB / 1.818 GB, free: 3.305 MB / 0.92 GB
Notification: Performance of postOpt collapseArrayExpressions (initialization): time 0.001456/4.849, allocations: 287.9 kB / 1.818 GB, free: 3.023 MB / 0.92 GB
Warning: The initial conditions are over specified. The following 3 initial equations are redundant, so they are removed from the initialization system:
         $DER.Condenseur.pipe_3.Q[1] = 0.0
         volumeA.P = $START.volumeA.P
         stodolaTurbine.proe.x = $START.stodolaTurbine.proe.x.
Notification: Model statistics after passing the back-end for initialization:
 * Number of independent subsystems: 199
 * Number of states: 0 ()
 * Number of discrete variables: 36 (Source_Vsup1.C.ftype,volumeA.Cs2.ftype,volumeA.Cs1.ftype,volumeA.Ce1.ftype,Condenseur.DynamicCondenser.Cl.ftype,volumeA.fluids[1],sourcePCaloporteur.C.ftype,Condenseur.C1.ftype,Condenseur.DynamicCondenser.fluids[1],staticCentrifugalPump.fluid,stodolaTurbine.fluid,Condenseur.pipe_3.fluid,puitsPCaloporteur.fluid,PressureLoss_VapeurIn_in4.fluid,Source_Vsup1.fluid1,volumeA.fluid1,sourcePCaloporteur.fluid1,Condenseur.DynamicCondenser.CvGCT.diff_on_2,Source_Vsup1.C.diff_on_2,PressureLoss_VapeurIn_in4.C2.diff_on_1,volumeA.Cs2.diff_on_1,stodolaTurbine.Cs.diff_on_1,volumeA.Cs1.diff_on_1,volumeA.Ce2.diff_on_2,Condenseur.C2ex.diff_on_2,volumeA.Ce1.diff_on_2,volumeA.Cs1.diff_on_2,volumeA.Ce1.diff_on_1,Condenseur.C1.diff_on_1,Condenseur.pipe_3.C1.diff_on_2,Condenseur.pipe_3.C2.diff_on_1,Condenseur.DynamicCondenser.Cl.diff_on_1,staticCentrifugalPump.C2.diff_on_1,Condenseur.DynamicCondenser.CvBP.diff_on_2,volumeA.Cs2.diff_on_2,Condenseur.DynamicCondenser.Ce.diff_on_2)
 * Number of discrete states: 0 ()
 * Number of clocked states: 0 ()
 * Top-level inputs: 0
Notification: Strong component statistics for initialization (393):
 * Single equations (assignments): 371
 * Array equations: 0
 * Algorithm blocks: 0
 * Record equations: 6
 * When equations: 0
 * If-equations: 0
 * Equation systems (not torn): 0
 * Torn equation systems: 16
 * Mixed (continuous/discrete) equation systems: 0
Notification: Torn system details for strict tearing set:
 * Linear torn systems (#iteration vars, #inner vars, density): 11 systems
   {(4,1,62.5%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%)}
 * Non-linear torn systems (#iteration vars, #inner vars): 5 systems
   {(1,2), (1,2), (5,12), (1,3), (21,239)}
Notification: Performance of prepare postOptimizeDAE: time 0.003235/4.852, allocations: 1.147 MB / 1.82 GB, free: 1.922 MB / 0.92 GB
Notification: Performance of postOpt lateInlineFunction (simulation): time 0.0009687/4.853, allocations: 359.6 kB / 1.82 GB, free: 1.566 MB / 0.92 GB
Notification: Performance of postOpt wrapFunctionCalls (simulation): time 0.2967/5.15, allocations: 10.84 MB / 1.831 GB, free: 0.5025 GB / 0.92 GB
Notification: Performance of postOpt simplifysemiLinear (simulation): time 0.0001383/5.15, allocations: 21.09 kB / 1.831 GB, free: 0.5025 GB / 0.92 GB
Notification: Performance of postOpt simplifyComplexFunction (simulation): time 2.298e-05/5.15, allocations: 3.375 kB / 1.831 GB, free: 0.5025 GB / 0.92 GB
Notification: Performance of postOpt removeConstants (simulation): time 0.003523/5.153, allocations: 1.217 MB / 1.832 GB, free: 0.5024 GB / 0.92 GB
Notification: Performance of postOpt simplifyTimeIndepFuncCalls (simulation): time 0.001202/5.155, allocations: 115.8 kB / 1.832 GB, free: 0.5024 GB / 0.92 GB
Notification: Performance of postOpt simplifyAllExpressions (simulation): time 0.003337/5.158, allocations: 162.2 kB / 1.832 GB, free: 0.5024 GB / 0.92 GB
Notification: Performance of postOpt findZeroCrossings (simulation): time 0.001032/5.159, allocations: 413.6 kB / 1.832 GB, free: 0.5024 GB / 0.92 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(stodolaTurbine.Te, stodolaTurbine.proe.d, stodolaTurbine.proe.u, stodolaTurbine.proe.s, stodolaTurbine.proe.cp, stodolaTurbine.proe.ddhp, stodolaTurbine.proe.ddph, stodolaTurbine.proe.duph, stodolaTurbine.proe.duhp, stodolaTurbine.proe.x) = $cse11

Variables:
1: stodolaTurbine.proe.duhp:VARIABLE(unit = "1" )  "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real
2: stodolaTurbine.proe.ddph:VARIABLE(unit = "s2/m2" )  "Derivative of density wrt. pressure at constant specific enthalpy" type: Real
3: stodolaTurbine.proe.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific heat capacity at constant presure" type: Real
4: $cse11.cp:VARIABLE(protected = true )  type: Real unreplaceable
5: stodolaTurbine.proe.ddhp:VARIABLE(unit = "kg.s2/m5" )  "Derivative of density wrt. specific enthalpy at constant pressure" type: Real
6: stodolaTurbine.proe.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 )  "Specific inner energy" type: Real
7: stodolaTurbine.proe.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific entropy" type: Real
8: stodolaTurbine.proe.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 )  "Density" type: Real
9: stodolaTurbine.proe.duph:VARIABLE(unit = "m3/kg" )  "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real
10: stodolaTurbine.Te:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 300.0 )  "Temperature at the inlet" 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): staticCentrifugalPump.deltaP = volumeA.P - Condenseur.DynamicCondenser.Pfond
2/2 (1): staticCentrifugalPump.deltaP = 9.80665 * staticCentrifugalPump.rho * staticCentrifugalPump.hn
3/3 (1): staticCentrifugalPump.hn = (staticCentrifugalPump.a1 * abs(staticCentrifugalPump.Qv) + staticCentrifugalPump.a2 * staticCentrifugalPump.R) * staticCentrifugalPump.Qv + staticCentrifugalPump.a3 * staticCentrifugalPump.R ^ 2.0
4/4 (1): staticCentrifugalPump.rh = max(if noEvent(abs(staticCentrifugalPump.R) > staticCentrifugalPump.eps) then staticCentrifugalPump.b1 * staticCentrifugalPump.Qv * abs(staticCentrifugalPump.Qv) / staticCentrifugalPump.R ^ 2.0 + staticCentrifugalPump.b2 * staticCentrifugalPump.Qv / staticCentrifugalPump.R + staticCentrifugalPump.b3 else staticCentrifugalPump.b3, staticCentrifugalPump.rhmin)
5/5 (1): staticCentrifugalPump.deltaH = 9.80665 * staticCentrifugalPump.hn / staticCentrifugalPump.rh
6/6 (1): staticCentrifugalPump.deltaH = staticCentrifugalPump.C2.h - Condenseur.C2ex.h
7/7 (1): 0.0 = staticCentrifugalPump.Q * (-2.501569e6 + staticCentrifugalPump.C2.h) + heatSource.W0[1] - staticCentrifugalPump.Q * volumeA.Cs2.h
8/8 (10): $cse11 = ThermoSysPro.Properties.Fluid.Ph(volumeA.P, volumeA.Cs2.h, stodolaTurbine.mode_e, stodolaTurbine.fluid)
9/18 (10): ThermoSysPro.Properties.WaterSteam.Common.ThermoProperties_ph(stodolaTurbine.Te, stodolaTurbine.proe.d, stodolaTurbine.proe.u, stodolaTurbine.proe.s, stodolaTurbine.proe.cp, stodolaTurbine.proe.ddhp, stodolaTurbine.proe.ddph, stodolaTurbine.proe.duph, stodolaTurbine.proe.duhp, stodolaTurbine.proe.x) = $cse11
10/28 (1): staticCentrifugalPump.Q = if noEvent(volumeA.P > stodolaTurbine.pcrit) or noEvent(stodolaTurbine.Te > stodolaTurbine.Tcrit) then sqrt((volumeA.P ^ 2.0 - Condenseur.DynamicCondenser.P ^ 2.0) / (stodolaTurbine.Cst * stodolaTurbine.Te)) else sqrt((volumeA.P ^ 2.0 - Condenseur.DynamicCondenser.P ^ 2.0) / (stodolaTurbine.Cst * stodolaTurbine.Te * stodolaTurbine.proe.x))
11/29 (1): staticCentrifugalPump.Pm = 0.5 * (Condenseur.DynamicCondenser.Pfond + volumeA.P)
12/30 (1): staticCentrifugalPump.rho = ThermoSysPro.Properties.Fluid.Density_Ph(staticCentrifugalPump.Pm, staticCentrifugalPump.h, staticCentrifugalPump.fluid, staticCentrifugalPump.mode, 0.0, 1.0, 0.0, 0.0)
13/31 (1): staticCentrifugalPump.Q = staticCentrifugalPump.Qv * staticCentrifugalPump.rho
14/32 (1): volumeA.Cs2.h = if staticCentrifugalPump.Q > 0.0 then volumeA.h else Condenseur.DynamicCondenser.hv
15/33 (1): Condenseur.C2ex.h = if staticCentrifugalPump.Q > 0.0 then Condenseur.DynamicCondenser.hl else volumeA.h
16/34 (10): Condenseur.DynamicCondenser.prod = ThermoSysPro.Properties.Fluid.Ph(Condenseur.DynamicCondenser.Pfond, Condenseur.C2ex.h, 0, Condenseur.DynamicCondenser.fluid)
17/44 (1): Condenseur.DynamicCondenser.Pfond = Condenseur.DynamicCondenser.P + 9.80665 * Condenseur.DynamicCondenser.prod.d * Condenseur.DynamicCondenser.zl
18/45 (1): staticCentrifugalPump.h = 0.5 * (Condenseur.C2ex.h + staticCentrifugalPump.C2.h)

Variables:
1: staticCentrifugalPump.h:VARIABLE(start = 193554.9971298399 unit = "J/kg" )  "Fluid average specific enthalpy" type: Real
2: Condenseur.DynamicCondenser.prod.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 )  "Density" type: Real
3: Condenseur.DynamicCondenser.prod.T:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 320.0 )  "Temperature" type: Real
4: Condenseur.DynamicCondenser.prod.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 )  "Specific inner energy" type: Real
5: Condenseur.DynamicCondenser.prod.ddph:VARIABLE(unit = "s2/m2" )  "Derivative of density wrt. pressure at constant specific enthalpy" type: Real
6: Condenseur.DynamicCondenser.prod.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific entropy" type: Real
7: Condenseur.DynamicCondenser.prod.duhp:VARIABLE(unit = "1" )  "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real
8: Condenseur.DynamicCondenser.prod.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific heat capacity at constant presure" type: Real
9: Condenseur.DynamicCondenser.prod.duph:VARIABLE(unit = "m3/kg" )  "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real
10: Condenseur.DynamicCondenser.Pfond:VARIABLE(start = 11000.0 unit = "Pa" )  "Fluid pressure at the bottom of the cavity" type: Real
11: Condenseur.DynamicCondenser.prod.ddhp:VARIABLE(unit = "kg.s2/m5" )  "Derivative of density wrt. specific enthalpy at constant pressure" type: Real
12: Condenseur.DynamicCondenser.prod.x:VARIABLE(min = 0.0 max = 1.0 unit = "1" )  "Vapor mass fraction" type: Real
13: Condenseur.C2ex.h:VARIABLE(flow=false start = 1e5 unit = "J/kg" )  "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real
14: volumeA.h:VARIABLE(start = 2e6 unit = "J/kg" )  "Fluid specific enthalpy" type: Real
15: staticCentrifugalPump.Q:VARIABLE(start = 500.0 unit = "kg/s" fixed = false )  "Mass flow rate" type: Real
16: staticCentrifugalPump.rho:VARIABLE(min = 0.0 start = 998.0 unit = "kg/m3" )  "Fluid density" type: Real
17: staticCentrifugalPump.Pm:VARIABLE(min = 0.0 start = 355000.00000015664 unit = "Pa" nominal = 1e5 )  "Fluid average pressure" type: Real
18: stodolaTurbine.proe.x:VARIABLE(min = 0.0 max = 1.0 start = 1.0 unit = "1" fixed = true )  "Vapor mass fraction" type: Real
19: stodolaTurbine.proe.duhp:VARIABLE(unit = "1" )  "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real
20: stodolaTurbine.proe.ddph:VARIABLE(unit = "s2/m2" )  "Derivative of density wrt. pressure at constant specific enthalpy" type: Real
21: stodolaTurbine.proe.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific heat capacity at constant presure" type: Real
22: $cse11.cp:VARIABLE(protected = true )  type: Real unreplaceable
23: stodolaTurbine.proe.ddhp:VARIABLE(unit = "kg.s2/m5" )  "Derivative of density wrt. specific enthalpy at constant pressure" type: Real
24: stodolaTurbine.proe.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 )  "Specific inner energy" type: Real
25: stodolaTurbine.proe.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific entropy" type: Real
26: stodolaTurbine.proe.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 )  "Density" type: Real
27: stodolaTurbine.proe.duph:VARIABLE(unit = "m3/kg" )  "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real
28: stodolaTurbine.Te:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 300.0 )  "Temperature at the inlet" type: Real
29: $cse11.d:VARIABLE(protected = true )  type: Real unreplaceable
30: $cse11.ddhp:VARIABLE(protected = true )  type: Real unreplaceable
31: $cse11.duph:VARIABLE(protected = true )  type: Real unreplaceable
32: $cse11.x:VARIABLE(protected = true )  type: Real unreplaceable
33: $cse11.s:VARIABLE(protected = true )  type: Real unreplaceable
34: $cse11.duhp:VARIABLE(protected = true )  type: Real unreplaceable
35: $cse11.T:VARIABLE(protected = true )  type: Real unreplaceable
36: volumeA.P:VARIABLE(min = 0.0 start = 7e5 unit = "Pa" fixed = true nominal = 1e5 )  "Fluid pressure" type: Real
37: $cse11.ddph:VARIABLE(protected = true )  type: Real unreplaceable
38: $cse11.u:VARIABLE(protected = true )  type: Real unreplaceable
39: volumeA.Cs2.h:VARIABLE(flow=false start = 1e5 unit = "J/kg" )  "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real
40: staticCentrifugalPump.C2.h:VARIABLE(flow=false start = 195297.69906611618 unit = "J/kg" )  "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real
41: staticCentrifugalPump.deltaH:VARIABLE(unit = "J/kg" )  "Specific enthalpy variation between the outlet and the inlet" type: Real
42: staticCentrifugalPump.rh:VARIABLE()  "Hydraulic efficiency" type: Real
43: staticCentrifugalPump.Qv:VARIABLE(start = 0.009081311621074862 unit = "m3/s" )  "Volume flow rate" type: Real
44: staticCentrifugalPump.hn:VARIABLE(min = 0.0 start = 71.08245675235786 unit = "m" fixed = false )  "Pump head" type: Real
45: staticCentrifugalPump.deltaP:VARIABLE(unit = "Pa" )  "Pressure variation between the outlet and the inlet" 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 0.008839/5.168, allocations: 2.958 MB / 1.835 GB, free: 0.5011 GB / 0.92 GB
Error: post-optimization module createDAEmodeBDAE (simulation) failed.
Error: Internal error SimCode DAEmode: The model ThermoSysPro.Fluid.Examples.SimpleExamples.TestDynamicCondenser could not be translated