Running: ./testmodel.py --libraries=/home/hudson/saved_omc/libraries/.openmodelica/libraries --ompython_omhome=/usr ThermoSysPro_ThermoSysPro.Examples.Book.SimpleExamples.HeatExchanger.TestStaticCondenser.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.Book.SimpleExamples.HeatExchanger.TestStaticCondenser,tolerance=1e-06,outputFormat="empty",numberOfIntervals=5000,variableFilter="",fileNamePrefix="ThermoSysPro_ThermoSysPro.Examples.Book.SimpleExamples.HeatExchanger.TestStaticCondenser")
translateModel(ThermoSysPro.Examples.Book.SimpleExamples.HeatExchanger.TestStaticCondenser,tolerance=1e-06,outputFormat="empty",numberOfIntervals=5000,variableFilter="",fileNamePrefix="ThermoSysPro_ThermoSysPro.Examples.Book.SimpleExamples.HeatExchanger.TestStaticCondenser")
Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermoSysPro 4.0.0-master/package.mo): time 0.8047/0.8047, allocations: 150.9 MB / 167.2 MB, free: 14.54 MB / 142.1 MB
Notification: Performance of FrontEnd - loaded program: time 0.0003386/0.0003387, allocations: 16.97 kB / 237.7 MB, free: 1.809 MB / 190.1 MB
Notification: Performance of FrontEnd - Absyn->SCode: time 0.05035/0.0507, allocations: 31.34 MB / 269.1 MB, free: 7.098 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.Book.SimpleExamples.HeatExchanger.TestStaticCondenser): time 1.557/1.607, allocations: 298.7 MB / 0.5545 GB, free: 8.922 MB / 446.1 MB
Notification: Performance of NFInst.instExpressions: time 0.04164/1.649, allocations: 37.05 MB / 0.5907 GB, free: 3.719 MB / 478.1 MB
Notification: Performance of NFInst.updateImplicitVariability: time 0.0006958/1.65, allocations: 8 kB / 0.5907 GB, free: 3.711 MB / 478.1 MB
[/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/SingularPressureLoss.mo:25:3-27:16: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/SingularPressureLoss.mo:28:3-29:52: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/SingularPressureLoss.mo:25:3-27:16: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/SingularPressureLoss.mo:28:3-29:52: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/SingularPressureLoss.mo:25:3-27:16: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/SingularPressureLoss.mo:28:3-29:52: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/Sink.mo:17:3-19:16: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/SingularPressureLoss.mo:25:3-27:16: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/SingularPressureLoss.mo:28:3-29:52: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/SingularPressureLoss.mo:25:3-27:16: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/SingularPressureLoss.mo:28:3-29:52: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/HeatExchangers/StaticCondenser.mo:78:3-80:24:writable] Warning: Connector Cee 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/HeatExchangers/StaticCondenser.mo:81:3-83:17:writable] Warning: Connector Cse 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/HeatExchangers/StaticCondenser.mo:84:3-86:16:writable] Warning: Connector Cex 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/HeatExchangers/StaticCondenser.mo:87:3-88:83:writable] Warning: Connector Cvt 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/HeatExchangers/StaticCondenser.mo:108:3-109:83:writable] Warning: Connector Cep 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/HeatExchangers/StaticCondenser.mo:111:3-113:17:writable] Warning: Connector Cev 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/SourceQ.mo:24:3-25:52: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/SingularPressureLoss.mo:25:3-27:16: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/SingularPressureLoss.mo:28:3-29:52: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 0.0008773/1.651, allocations: 306.1 kB / 0.591 GB, free: 3.414 MB / 478.1 MB
Notification: Performance of NFTyping.typeBindings: time 0.001236/1.652, allocations: 479.9 kB / 0.5914 GB, free: 2.941 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 0.02331/1.675, allocations: 10.25 MB / 0.6015 GB, free: 8.668 MB / 494.1 MB
Notification: Performance of NFFlatten.flatten: time 0.001789/1.677, allocations: 1.669 MB / 0.6031 GB, free: 6.992 MB / 494.1 MB
Notification: Performance of NFFlatten.resolveConnections: time 0.0006135/1.678, allocations: 0.5972 MB / 0.6037 GB, free: 6.375 MB / 494.1 MB
Notification: Performance of NFEvalConstants.evaluate: time 0.0006363/1.678, allocations: 0.6304 MB / 0.6043 GB, free: 5.742 MB / 494.1 MB
Notification: Performance of NFSimplifyModel.simplify: time 0.0005017/1.679, allocations: 0.5714 MB / 0.6048 GB, free: 5.168 MB / 494.1 MB
Notification: Performance of NFPackage.collectConstants: time 0.0001127/1.679, allocations: 96 kB / 0.6049 GB, free: 5.074 MB / 494.1 MB
Notification: Performance of NFFlatten.collectFunctions: time 0.02831/1.707, allocations: 18.88 MB / 0.6234 GB, free: 2.176 MB / 0.4981 GB
Notification: Performance of NFScalarize.scalarize: time 0.0002333/1.708, allocations: 227.1 kB / 0.6236 GB, free: 1.953 MB / 0.4981 GB
Notification: Performance of NFVerifyModel.verify: time 0.000697/1.708, allocations: 0.6646 MB / 0.6242 GB, free: 1.285 MB / 0.4981 GB
Notification: Performance of NFConvertDAE.convert: time 0.01746/1.726, allocations: 9.874 MB / 0.6339 GB, free: 7.387 MB / 0.5137 GB
Notification: Performance of FrontEnd - DAE generated: time 4.869e-06/1.726, allocations: 3.938 kB / 0.6339 GB, free: 7.383 MB / 0.5137 GB
Notification: Performance of FrontEnd: time 2.615e-06/1.726, allocations: 4 kB / 0.6339 GB, free: 7.379 MB / 0.5137 GB
Notification: Performance of Transformations before backend: time 1.257e-05/1.726, allocations: 0 / 0.6339 GB, free: 7.379 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: 389
 * Number of variables: 389
Notification: Performance of Generate backend data structure: time 0.004847/1.731, allocations: 2.396 MB / 0.6362 GB, free: 4.926 MB / 0.5137 GB
Notification: Performance of prepare preOptimizeDAE: time 4.504e-05/1.731, allocations: 15.89 kB / 0.6362 GB, free: 4.91 MB / 0.5137 GB
Notification: Performance of preOpt normalInlineFunction (simulation): time 0.0001776/1.731, allocations: 150.1 kB / 0.6364 GB, free: 4.762 MB / 0.5137 GB
Notification: Performance of preOpt evaluateParameters (simulation): time 0.0005134/1.731, allocations: 0.4956 MB / 0.6369 GB, free: 4.227 MB / 0.5137 GB
Notification: Performance of preOpt simplifyIfEquations (simulation): time 5.955e-05/1.731, allocations: 78.05 kB / 0.6369 GB, free: 4.148 MB / 0.5137 GB
Notification: Performance of preOpt expandDerOperator (simulation): time 9.823e-05/1.732, allocations: 100 kB / 0.637 GB, free: 4.051 MB / 0.5137 GB
Notification: Performance of preOpt clockPartitioning (simulation): time 0.0016/1.733, allocations: 1.36 MB / 0.6384 GB, free: 2.578 MB / 0.5137 GB
Notification: Performance of preOpt findStateOrder (simulation): time 2.513e-05/1.733, allocations: 4 kB / 0.6384 GB, free: 2.574 MB / 0.5137 GB
Notification: Performance of preOpt replaceEdgeChange (simulation): time 7.09e-05/1.733, allocations: 40 kB / 0.6384 GB, free: 2.535 MB / 0.5137 GB
Notification: Performance of preOpt inlineArrayEqn (simulation): time 4.392e-05/1.733, allocations: 59.95 kB / 0.6385 GB, free: 2.477 MB / 0.5137 GB
Notification: Performance of preOpt removeEqualRHS (simulation): time 0.001193/1.735, allocations: 0.8709 MB / 0.6393 GB, free: 1.602 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 0.004917/1.739, allocations: 7.325 MB / 0.6465 GB, free: 9.562 MB / 0.5294 GB
Notification: Performance of preOpt comSubExp (simulation): time 0.00102/1.74, allocations: 0.6309 MB / 0.6471 GB, free: 8.926 MB / 0.5294 GB
Notification: Performance of preOpt resolveLoops (simulation): time 0.0005458/1.741, allocations: 457.2 kB / 0.6475 GB, free: 8.477 MB / 0.5294 GB
Notification: Performance of preOpt evalFunc (simulation): time 0.3416/2.083, allocations: 89.37 MB / 0.7348 GB, free: 198.7 MB / 0.5919 GB
Notification: Performance of preOpt encapsulateWhenConditions (simulation): time 3.796e-05/2.083, allocations: 36.88 kB / 0.7348 GB, free: 198.6 MB / 0.5919 GB
Notification: Performance of pre-optimization done (n=182): time 3.066e-06/2.083, allocations: 0 / 0.7348 GB, free: 198.6 MB / 0.5919 GB
Notification: Performance of matching and sorting (n=182): time 0.009753/2.093, allocations: 3.313 MB / 0.7381 GB, free: 198 MB / 0.5919 GB
Notification: Performance of inlineWhenForInitialization (initialization): time 2.46e-05/2.093, allocations: 59.19 kB / 0.7381 GB, free: 198 MB / 0.5919 GB
Notification: Performance of selectInitializationVariablesDAE (initialization): time 0.0006035/2.093, allocations: 0.6058 MB / 0.7387 GB, free: 197.8 MB / 0.5919 GB
Notification: Performance of collectPreVariables (initialization): time 3.48e-05/2.093, allocations: 32.45 kB / 0.7387 GB, free: 197.8 MB / 0.5919 GB
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermoSysPro 4.0.0-master/WaterSteam/BoundaryConditions/SinkP.mo:3:3-3:64:writable] Warning: The parameter Puit_condenseur.P0 has fixed = false and a binding equation Puit_condenseur.P0 = 1e5, 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 0.0002378/2.093, allocations: 402.6 kB / 0.7391 GB, free: 197.7 MB / 0.5919 GB
Notification: Performance of collectInitialBindings (initialization): time 0.0002937/2.094, allocations: 0.5842 MB / 0.7397 GB, free: 197.3 MB / 0.5919 GB
Notification: Performance of simplifyInitialFunctions (initialization): time 0.0002629/2.094, allocations: 240.1 kB / 0.7399 GB, free: 197.2 MB / 0.5919 GB
Notification: Performance of setup shared object (initialization): time 7.559e-05/2.094, allocations: 343.2 kB / 0.7402 GB, free: 196.9 MB / 0.5919 GB
Notification: Performance of preBalanceInitialSystem (initialization): time 0.0004684/2.095, allocations: 353 kB / 0.7406 GB, free: 196.9 MB / 0.5919 GB
Notification: Performance of partitionIndependentBlocks (initialization): time 0.0005948/2.095, allocations: 0.5718 MB / 0.7411 GB, free: 196.7 MB / 0.5919 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 0.00742/2.103, allocations: 3.002 MB / 0.7441 GB, free: 196.3 MB / 0.5919 GB
Notification: Performance of solveInitialSystemEqSystem (initialization): time 9.198e-06/2.103, allocations: 3.969 kB / 0.7441 GB, free: 196.3 MB / 0.5919 GB
Notification: Performance of matching and sorting (n=230) (initialization): time 0.002418/2.105, allocations: 1.628 MB / 0.7457 GB, free: 196.1 MB / 0.5919 GB
Notification: Performance of prepare postOptimizeDAE: time 2.07e-05/2.105, allocations: 7.906 kB / 0.7457 GB, free: 196.1 MB / 0.5919 GB
Notification: Performance of postOpt simplifyComplexFunction (initialization): time 2.06e-05/2.105, allocations: 7.875 kB / 0.7457 GB, free: 196.1 MB / 0.5919 GB
Notification: Performance of postOpt tearingSystem (initialization): time 0.003114/2.108, allocations: 1.497 MB / 0.7471 GB, free: 195.9 MB / 0.5919 GB
Notification: Performance of postOpt solveSimpleEquations (initialization): time 0.0002331/2.109, allocations: 76.94 kB / 0.7472 GB, free: 195.9 MB / 0.5919 GB
Notification: Performance of postOpt calculateStrongComponentJacobians (initialization): time 0.003534/2.112, allocations: 5.656 MB / 0.7527 GB, free: 191.2 MB / 0.5919 GB
Notification: Performance of postOpt simplifyAllExpressions (initialization): time 0.0005492/2.113, allocations: 136.5 kB / 0.7529 GB, free: 191.1 MB / 0.5919 GB
Notification: Performance of postOpt collapseArrayExpressions (initialization): time 5.333e-05/2.113, allocations: 39.11 kB / 0.7529 GB, free: 191.1 MB / 0.5919 GB
Warning: The initial conditions are over specified. The following 1 initial equations are redundant, so they are removed from the initialization system:
         Source_condenseur.P = $START.Source_condenseur.P.
Notification: Model statistics after passing the back-end for initialization:
 * Number of independent subsystems: 25
 * Number of states: 0 ()
 * Number of discrete variables: 24 (singularPressureLoss2.C2.b,singularPressureLoss2.C1.a,Source_condenseur.C.b,condenseur.Cev.a,condenseur.Cep.a,condenseur.Cvt.a,condenseur.Cex.b,condenseur.Cse.b,condenseur.Cee.a,singularPressureLoss5.C2.b,singularPressureLoss5.C1.a,singularPressureLoss4.C2.b,singularPressureLoss4.C1.a,Puit_condenseur1.C.a,singularPressureLoss3.C2.b,singularPressureLoss3.C1.a,singularPressureLoss1.C2.b,singularPressureLoss1.C1.a,singularPressureLoss.C2.b,singularPressureLoss.C1.a,sourceP2.C.b,sourceP1.C.b,sourceP.C.b,Puit_condenseur.C.a)
 * Number of discrete states: 0 ()
 * Number of clocked states: 0 ()
 * Top-level inputs: 0
Notification: Strong component statistics for initialization (64):
 * Single equations (assignments): 52
 * Array equations: 0
 * Algorithm blocks: 0
 * Record equations: 4
 * When equations: 0
 * If-equations: 0
 * Equation systems (not torn): 0
 * Torn equation systems: 8
 * Mixed (continuous/discrete) equation systems: 0
Notification: Torn system details for strict tearing set:
 * Linear torn systems (#iteration vars, #inner vars, density): 1 system
   {(1,3,100.0%)}
 * Non-linear torn systems (#iteration vars, #inner vars): 7 systems
   {(1,3), (10,2), (1,3), (1,3), (1,3), (1,3), (5,12)}
Notification: Performance of prepare postOptimizeDAE: time 0.0003543/2.113, allocations: 260 kB / 0.7532 GB, free: 191 MB / 0.5919 GB
Notification: Performance of postOpt lateInlineFunction (simulation): time 0.0001072/2.113, allocations: 97.31 kB / 0.7533 GB, free: 191 MB / 0.5919 GB
Notification: Performance of postOpt wrapFunctionCalls (simulation): time 0.002753/2.116, allocations: 2.847 MB / 0.756 GB, free: 190.4 MB / 0.5919 GB
Notification: Performance of postOpt simplifysemiLinear (simulation): time 9.518e-06/2.116, allocations: 3.188 kB / 0.756 GB, free: 190.4 MB / 0.5919 GB
Notification: Performance of postOpt simplifyComplexFunction (simulation): time 7.254e-06/2.116, allocations: 0 / 0.756 GB, free: 190.4 MB / 0.5919 GB
Notification: Performance of postOpt removeConstants (simulation): time 0.0003126/2.116, allocations: 321.5 kB / 0.7563 GB, free: 190.2 MB / 0.5919 GB
Notification: Performance of postOpt simplifyTimeIndepFuncCalls (simulation): time 7.002e-05/2.116, allocations: 11.78 kB / 0.7564 GB, free: 190.2 MB / 0.5919 GB
Notification: Performance of postOpt simplifyAllExpressions (simulation): time 0.0003318/2.117, allocations: 16.16 kB / 0.7564 GB, free: 190.2 MB / 0.5919 GB
Notification: Performance of postOpt findZeroCrossings (simulation): time 8.742e-05/2.117, allocations: 40.06 kB / 0.7564 GB, free: 190.2 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(singularPressureLoss3.T, singularPressureLoss3.rho, singularPressureLoss3.pro.u, singularPressureLoss3.pro.s, singularPressureLoss3.pro.cp, singularPressureLoss3.pro.ddhp, singularPressureLoss3.pro.ddph, singularPressureLoss3.pro.duph, singularPressureLoss3.pro.duhp, singularPressureLoss3.pro.x) = $cse12

Variables:
1: singularPressureLoss3.pro.ddph:VARIABLE(unit = "s2/m2" )  "Derivative of density wrt. pressure at constant specific enthalpy" type: Real
2: singularPressureLoss3.pro.x:VARIABLE(min = 0.0 max = 1.0 unit = "1" )  "Vapor mass fraction" type: Real
3: singularPressureLoss3.pro.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific heat capacity at constant presure" type: Real
4: $cse12.duhp:VARIABLE(protected = true )  type: Real unreplaceable
5: $cse12.u:VARIABLE(protected = true )  type: Real unreplaceable
6: $cse12.cp:VARIABLE(protected = true )  type: Real unreplaceable
7: $cse12.duph:VARIABLE(protected = true )  type: Real unreplaceable
8: $cse12.T:VARIABLE(protected = true )  type: Real unreplaceable
9: $cse12.ddph:VARIABLE(protected = true )  type: Real unreplaceable
10: $cse12.x:VARIABLE(protected = true )  type: Real unreplaceable
[/var/lib/jenkins1/ws/OpenModelicaLibraryTestingWork/OpenModelica/OMCompiler/Compiler/BackEnd/DAEMode.mo:528:7-530:90:writable] Error: Internal error DAEMode.traverserStrongComponents failed on equation:
1/1 (1): 0.0 = if Source_condenseur.Q0 > 0.0 then singularPressureLoss2.h - Source_condenseur.h0 else singularPressureLoss2.h - singularPressureLoss2.C2.h_vol
2/2 (1): 0.0 = if Source_condenseur.Q0 > 0.0 then singularPressureLoss2.h - singularPressureLoss2.C2.h_vol else condenseur.Hse - condenseur.Cse.h_vol
3/3 (10): $cse5 = ThermoSysPro.Properties.WaterSteam.IF97.Water_Ph(condenseur.Pee, singularPressureLoss2.h, condenseur.mode_ee)
4/13 (1): $cse6 = exp(condenseur.XKCO * condenseur.SCO * (condenseur.Tee - condenseur.Tse) / condenseur.W)
5/14 (1): condenseur.W = Source_condenseur.Q0 * (condenseur.Hse - singularPressureLoss2.h)
6/15 (10): $cse3 = ThermoSysPro.Properties.WaterSteam.IF97.Water_Ph(condenseur.Pse, condenseur.Hse, condenseur.mode_se)
7/25 (1): 0.0 = condenseur.Tsat + (condenseur.Tee - condenseur.Tsat) * $cse6 - condenseur.Tse
8/26 (10): ThermoSysPro.Properties.WaterSteam.Common.ThermoProperties_ph(condenseur.Tse, condenseur.prose.d, condenseur.prose.u, condenseur.prose.s, condenseur.prose.cp, condenseur.prose.ddhp, condenseur.prose.ddph, condenseur.prose.duph, condenseur.prose.duhp, condenseur.prose.x) = $cse3
9/36 (10): $cse10 = ThermoSysPro.Properties.Fluid.Ph(singularPressureLoss4.Pm, condenseur.Hse, singularPressureLoss4.mode, singularPressureLoss4.fluid)
10/46 (10): ThermoSysPro.Properties.WaterSteam.Common.ThermoProperties_ph(singularPressureLoss4.T, singularPressureLoss4.rho, singularPressureLoss4.pro.u, singularPressureLoss4.pro.s, singularPressureLoss4.pro.cp, singularPressureLoss4.pro.ddhp, singularPressureLoss4.pro.ddph, singularPressureLoss4.pro.duph, singularPressureLoss4.pro.duhp, singularPressureLoss4.pro.x) = $cse10
11/56 (1): singularPressureLoss4.Pm = 0.5 * (condenseur.Pse + Puit_condenseur.P0)
12/57 (1): condenseur.Pse - Puit_condenseur.P0 = singularPressureLoss4.deltaP
13/58 (1): singularPressureLoss4.deltaP = singularPressureLoss4.K * $cse11 / singularPressureLoss4.rho
14/59 (1): condenseur.Pse = if noEvent(condenseur.rho_ee > 0.0) then condenseur.Pee - condenseur.CPCE * ThermoSysPro.Functions.ThermoSquare(Source_condenseur.Q0, condenseur.eps) / condenseur.rho_ee else condenseur.Pee
15/60 (10): ThermoSysPro.Properties.WaterSteam.Common.ThermoProperties_ph(condenseur.Tee, condenseur.rho_ee, condenseur.proee.u, condenseur.proee.s, condenseur.proee.cp, condenseur.proee.ddhp, condenseur.proee.ddph, condenseur.proee.duph, condenseur.proee.duhp, condenseur.proee.x) = $cse5
16/70 (1): 0.0 = if Source_condenseur.Q0 > 0.0 then condenseur.Hse - condenseur.Cse.h_vol else condenseur.Hse - Puit_condenseur.h
17/71 (1): condenseur.W = condenseur.Qvt * (condenseur.Hvt - condenseur.Hsate) + condenseur.Qep * (condenseur.Hep - condenseur.Hsate) + condenseur.Qev * (condenseur.Hev - condenseur.Hsate)
18/72 (10): $cse14 = ThermoSysPro.Properties.Fluid.Ph(singularPressureLoss1.Pm, condenseur.Hep, singularPressureLoss1.mode, singularPressureLoss1.fluid)
19/82 (10): ThermoSysPro.Properties.WaterSteam.Common.ThermoProperties_ph(singularPressureLoss1.T, singularPressureLoss1.rho, singularPressureLoss1.pro.u, singularPressureLoss1.pro.s, singularPressureLoss1.pro.cp, singularPressureLoss1.pro.ddhp, singularPressureLoss1.pro.ddph, singularPressureLoss1.pro.duph, singularPressureLoss1.pro.duhp, singularPressureLoss1.pro.x) = $cse14
20/92 (1): singularPressureLoss1.Pm = 0.5 * (sourceP2.P0 + condenseur.Pcond)
21/93 (14): (ThermoSysPro.Properties.WaterSteam.Common.PropThermoSat(condenseur.lsat1.P, condenseur.lsat1.T, condenseur.lsat1.rho, condenseur.Hsate, condenseur.lsat1.cp, condenseur.lsat1.pt, condenseur.lsat1.cv), condenseur.vsat1) = ThermoSysPro.Properties.WaterSteam.IF97.Water_sat_P(condenseur.Pcond)
22/107 (1): condenseur.Pcond = ThermoSysPro.Properties.WaterSteam.BaseIF97.Basic.psat(condenseur.Tsat)
23/108 (1): sourceP1.P0 - condenseur.Pcond = singularPressureLoss.deltaP
24/109 (1): singularPressureLoss.deltaP = singularPressureLoss.K * $cse17 / singularPressureLoss.rho
25/110 (1): $cse17 = ThermoSysPro.Functions.ThermoSquare(condenseur.Qev, singularPressureLoss.eps)
26/111 (1): 0.0 = if condenseur.Qev > 0.0 then condenseur.Hev - sourceP1.h0 else condenseur.Hev - condenseur.Hmv
27/112 (10): $cse16 = ThermoSysPro.Properties.Fluid.Ph(singularPressureLoss.Pm, condenseur.Hev, singularPressureLoss.mode, singularPressureLoss.fluid)
28/122 (10): ThermoSysPro.Properties.WaterSteam.Common.ThermoProperties_ph(singularPressureLoss.T, singularPressureLoss.rho, singularPressureLoss.pro.u, singularPressureLoss.pro.s, singularPressureLoss.pro.cp, singularPressureLoss.pro.ddhp, singularPressureLoss.pro.ddph, singularPressureLoss.pro.duph, singularPressureLoss.pro.duhp, singularPressureLoss.pro.x) = $cse16
29/132 (1): condenseur.Hmv = (condenseur.Hvt * condenseur.Qvt + condenseur.Hev * condenseur.Qev + condenseur.Hep * condenseur.Qep) / condenseur.Qex
30/133 (1): condenseur.Qex = condenseur.Qvt + condenseur.Qep + condenseur.Qev
31/134 (1): $cse15 = ThermoSysPro.Functions.ThermoSquare(condenseur.Qep, singularPressureLoss1.eps)
32/135 (1): singularPressureLoss1.deltaP = singularPressureLoss1.K * $cse15 / singularPressureLoss1.rho
33/136 (1): 0.0 = if condenseur.Qep > 0.0 then condenseur.Hep - sourceP2.h0 else condenseur.Hep - condenseur.Hmv
34/137 (1): 0.0 = if condenseur.Qvt > 0.0 then condenseur.Hvt - sourceP.h0 else condenseur.Hvt - condenseur.Hmv
35/138 (10): $cse12 = ThermoSysPro.Properties.Fluid.Ph(singularPressureLoss3.Pm, condenseur.Hvt, singularPressureLoss3.mode, singularPressureLoss3.fluid)
36/148 (1): singularPressureLoss3.deltaP = singularPressureLoss3.K * $cse13 / singularPressureLoss3.rho
37/149 (1): $cse13 = ThermoSysPro.Functions.ThermoSquare(condenseur.Qvt, singularPressureLoss3.eps)
38/150 (10): ThermoSysPro.Properties.WaterSteam.Common.ThermoProperties_ph(singularPressureLoss3.T, singularPressureLoss3.rho, singularPressureLoss3.pro.u, singularPressureLoss3.pro.s, singularPressureLoss3.pro.cp, singularPressureLoss3.pro.ddhp, singularPressureLoss3.pro.ddph, singularPressureLoss3.pro.duph, singularPressureLoss3.pro.duhp, singularPressureLoss3.pro.x) = $cse12
39/160 (1): singularPressureLoss.Pm = 0.5 * (sourceP1.P0 + condenseur.Pcond)
40/161 (1): sourceP2.P0 - condenseur.Pcond = singularPressureLoss1.deltaP
41/162 (1): sourceP.P0 - condenseur.Pcond = singularPressureLoss3.deltaP
42/163 (1): singularPressureLoss3.Pm = 0.5 * (sourceP.P0 + condenseur.Pcond)
43/164 (1): condenseur.KT2 = 52.0 + 3.3 * (-273.16 + condenseur.Tee) + (-0.05) * (-273.16 + condenseur.Tee) ^ 2.0
44/165 (1): condenseur.XKCO = condenseur.KCO * condenseur.COP * condenseur.KT2 * $cse7 / (condenseur.COPR * condenseur.KT1)

Variables:
1: condenseur.XKCO:VARIABLE(start = 200.0 unit = "W/(m2.K)" )  "Heat transfer coefficient" type: Real
2: condenseur.KT2:VARIABLE(start = 50.0 unit = "W/(m2.K)" )  "Second reference value for the exchange coefficient" type: Real
3: singularPressureLoss3.Pm:VARIABLE(min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 )  "Average fluid pressure" type: Real
4: singularPressureLoss3.deltaP:VARIABLE(unit = "Pa" )  "Singular pressure loss" type: Real
5: singularPressureLoss1.deltaP:VARIABLE(unit = "Pa" )  "Singular pressure loss" type: Real
6: singularPressureLoss.Pm:VARIABLE(min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 )  "Average fluid pressure" type: Real
7: singularPressureLoss3.T:VARIABLE(min = 200.0 max = 6000.0 start = 290.0 unit = "K" nominal = 300.0 )  "Fluid temperature" type: Real
8: singularPressureLoss3.pro.duph:VARIABLE(unit = "m3/kg" )  "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real
9: singularPressureLoss3.pro.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific entropy" type: Real
10: singularPressureLoss3.pro.duhp:VARIABLE(unit = "1" )  "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real
11: singularPressureLoss3.pro.ddhp:VARIABLE(unit = "kg.s2/m5" )  "Derivative of density wrt. specific enthalpy at constant pressure" type: Real
12: condenseur.Qvt:VARIABLE(start = 832.66 unit = "kg/s" fixed = true )  "Vapor mass flow rate leaving the turbine" type: Real
13: $cse13:VARIABLE(protected = true )  type: Real unreplaceable
14: singularPressureLoss3.rho:VARIABLE(min = 1e-9 max = 1e5 start = 998.0 unit = "kg/m3" nominal = 998.0 )  "Fluid density" type: Real
15: singularPressureLoss3.pro.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 )  "Specific inner energy" type: Real
16: singularPressureLoss3.pro.ddph:VARIABLE(unit = "s2/m2" )  "Derivative of density wrt. pressure at constant specific enthalpy" type: Real
17: singularPressureLoss3.pro.x:VARIABLE(min = 0.0 max = 1.0 unit = "1" )  "Vapor mass fraction" type: Real
18: singularPressureLoss3.pro.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific heat capacity at constant presure" type: Real
19: $cse12.duhp:VARIABLE(protected = true )  type: Real unreplaceable
20: $cse12.u:VARIABLE(protected = true )  type: Real unreplaceable
21: $cse12.cp:VARIABLE(protected = true )  type: Real unreplaceable
22: $cse12.duph:VARIABLE(protected = true )  type: Real unreplaceable
23: $cse12.T:VARIABLE(protected = true )  type: Real unreplaceable
24: $cse12.ddph:VARIABLE(protected = true )  type: Real unreplaceable
25: $cse12.x:VARIABLE(protected = true )  type: Real unreplaceable
26: $cse12.ddhp:VARIABLE(protected = true )  type: Real unreplaceable
27: $cse12.d:VARIABLE(protected = true )  type: Real unreplaceable
28: $cse12.s:VARIABLE(protected = true )  type: Real unreplaceable
29: condenseur.Hvt:VARIABLE(start = 2.5e6 unit = "J/kg" )  "Vapor specific enthalpy leaving the turbine" type: Real
30: condenseur.Hmv:VARIABLE(start = 2.5e6 unit = "J/kg" )  "Fluid input average specific enthalpy" type: Real
31: singularPressureLoss1.rho:VARIABLE(min = 1e-9 max = 1e5 start = 998.0 unit = "kg/m3" nominal = 998.0 )  "Fluid density" type: Real
32: $cse15:VARIABLE(protected = true )  type: Real unreplaceable
33: condenseur.Qep:VARIABLE(start = 1e-5 unit = "kg/s" fixed = true )  "Drain mass flow rate at the inlet" type: Real
34: condenseur.Qex:VARIABLE(start = 10.0 unit = "kg/s" )  "Drain mass flow rate at the outlet" type: Real
35: singularPressureLoss.pro.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific entropy" type: Real
36: singularPressureLoss.pro.duph:VARIABLE(unit = "m3/kg" )  "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real
37: singularPressureLoss.rho:VARIABLE(min = 1e-9 max = 1e5 start = 998.0 unit = "kg/m3" nominal = 998.0 )  "Fluid density" type: Real
38: singularPressureLoss.pro.duhp:VARIABLE(unit = "1" )  "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real
39: singularPressureLoss.pro.x:VARIABLE(min = 0.0 max = 1.0 unit = "1" )  "Vapor mass fraction" type: Real
40: singularPressureLoss.T:VARIABLE(min = 200.0 max = 6000.0 start = 290.0 unit = "K" nominal = 300.0 )  "Fluid temperature" type: Real
41: singularPressureLoss.pro.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 )  "Specific inner energy" type: Real
42: singularPressureLoss.pro.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific heat capacity at constant presure" type: Real
43: singularPressureLoss.pro.ddph:VARIABLE(unit = "s2/m2" )  "Derivative of density wrt. pressure at constant specific enthalpy" type: Real
44: singularPressureLoss.pro.ddhp:VARIABLE(unit = "kg.s2/m5" )  "Derivative of density wrt. specific enthalpy at constant pressure" type: Real
45: $cse16.cp:VARIABLE(protected = true )  type: Real unreplaceable
46: $cse16.x:VARIABLE(protected = true )  type: Real unreplaceable
47: $cse16.ddhp:VARIABLE(protected = true )  type: Real unreplaceable
48: $cse16.d:VARIABLE(protected = true )  type: Real unreplaceable
49: $cse16.ddph:VARIABLE(protected = true )  type: Real unreplaceable
50: $cse16.duph:VARIABLE(protected = true )  type: Real unreplaceable
51: $cse16.u:VARIABLE(protected = true )  type: Real unreplaceable
52: $cse16.T:VARIABLE(protected = true )  type: Real unreplaceable
53: $cse16.duhp:VARIABLE(protected = true )  type: Real unreplaceable
54: $cse16.s:VARIABLE(protected = true )  type: Real unreplaceable
55: condenseur.Hev:VARIABLE(start = 2.5e6 unit = "J/kg" )  "Vapor specific enthalpy at the inlet" type: Real
56: condenseur.Qev:VARIABLE(start = 1e-5 unit = "kg/s" fixed = true )  "Vapor mass flow rate at the inlet" type: Real
57: $cse17:VARIABLE(protected = true )  type: Real unreplaceable
58: singularPressureLoss.deltaP:VARIABLE(unit = "Pa" )  "Singular pressure loss" type: Real
59: condenseur.Tsat:VARIABLE(min = 0.0 start = 500.0 unit = "K" nominal = 300.0 )  "Water temperature at the saturation point" type: Real
60: condenseur.vsat1.P:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 )  "Pressure" type: Real
61: condenseur.Hsate:VARIABLE(start = 2e5 unit = "J/kg" )  "Water specific enthalpy at the saturation point" type: Real
62: condenseur.lsat1.P:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 )  "Pressure" type: Real
63: condenseur.vsat1.T:VARIABLE(min = 0.0 start = 288.15 unit = "K" nominal = 300.0 )  "Temperature" type: Real
64: condenseur.vsat1.h:VARIABLE(unit = "J/kg" )  "Specific enthalpy" type: Real
65: condenseur.lsat1.T:VARIABLE(min = 0.0 start = 288.15 unit = "K" nominal = 300.0 )  "Temperature" type: Real
66: condenseur.vsat1.cv:VARIABLE(unit = "J/(kg.K)" )  "Specific heat capacity at constant volume" type: Real
67: condenseur.lsat1.rho:VARIABLE(min = 0.0 unit = "kg/m3" )  "Density" type: Real
68: condenseur.vsat1.cp:VARIABLE(unit = "J/(kg.K)" )  "Specific heat capacity at constant pressure" type: Real
69: condenseur.vsat1.pt:VARIABLE()  "Derivative of pressure wrt. temperature" type: Real
70: condenseur.vsat1.rho:VARIABLE(min = 0.0 unit = "kg/m3" )  "Density" type: Real
71: condenseur.lsat1.cp:VARIABLE(unit = "J/(kg.K)" )  "Specific heat capacity at constant pressure" type: Real
72: condenseur.lsat1.cv:VARIABLE(unit = "J/(kg.K)" )  "Specific heat capacity at constant volume" type: Real
73: condenseur.lsat1.pt:VARIABLE()  "Derivative of pressure wrt. temperature" type: Real
74: condenseur.Pcond:VARIABLE(min = 0.0 start = 17000.0 unit = "Pa" nominal = 1e5 )  "Vapor pressure inside the condenser" type: Real
75: singularPressureLoss1.pro.duhp:VARIABLE(unit = "1" )  "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real
76: singularPressureLoss1.pro.x:VARIABLE(min = 0.0 max = 1.0 unit = "1" )  "Vapor mass fraction" type: Real
77: singularPressureLoss1.T:VARIABLE(min = 200.0 max = 6000.0 start = 290.0 unit = "K" nominal = 300.0 )  "Fluid temperature" type: Real
78: singularPressureLoss1.pro.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific heat capacity at constant presure" type: Real
79: singularPressureLoss1.pro.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 )  "Specific inner energy" type: Real
80: singularPressureLoss1.pro.duph:VARIABLE(unit = "m3/kg" )  "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real
81: $cse14.x:VARIABLE(protected = true )  type: Real unreplaceable
82: singularPressureLoss1.pro.ddhp:VARIABLE(unit = "kg.s2/m5" )  "Derivative of density wrt. specific enthalpy at constant pressure" type: Real
83: singularPressureLoss1.pro.ddph:VARIABLE(unit = "s2/m2" )  "Derivative of density wrt. pressure at constant specific enthalpy" type: Real
84: singularPressureLoss1.pro.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific entropy" type: Real
85: $cse14.cp:VARIABLE(protected = true )  type: Real unreplaceable
86: $cse14.T:VARIABLE(protected = true )  type: Real unreplaceable
87: $cse14.ddhp:VARIABLE(protected = true )  type: Real unreplaceable
88: $cse14.s:VARIABLE(protected = true )  type: Real unreplaceable
89: $cse14.duph:VARIABLE(protected = true )  type: Real unreplaceable
90: $cse14.u:VARIABLE(protected = true )  type: Real unreplaceable
91: $cse14.duhp:VARIABLE(protected = true )  type: Real unreplaceable
92: $cse14.ddph:VARIABLE(protected = true )  type: Real unreplaceable
93: singularPressureLoss1.Pm:VARIABLE(min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 )  "Average fluid pressure" type: Real
94: $cse14.d:VARIABLE(protected = true )  type: Real unreplaceable
95: condenseur.Hep:VARIABLE(start = 1e6 unit = "J/kg" )  "Drain specific enthalpy at the inlet" type: Real
96: condenseur.Cse.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" )  "Fluid specific enthalpy in the control volume" type: Real
97: condenseur.proee.x:VARIABLE(min = 0.0 max = 1.0 unit = "1" )  "Vapor mass fraction" type: Real
98: condenseur.proee.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific heat capacity at constant presure" type: Real
99: condenseur.proee.duhp:VARIABLE(unit = "1" )  "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real
100: $cse5.ddph:VARIABLE(protected = true )  type: Real unreplaceable
101: condenseur.proee.ddph:VARIABLE(unit = "s2/m2" )  "Derivative of density wrt. pressure at constant specific enthalpy" type: Real
102: condenseur.proee.duph:VARIABLE(unit = "m3/kg" )  "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real
103: condenseur.rho_ee:VARIABLE(min = 1e-9 max = 1e5 start = 900.0 unit = "kg/m3" nominal = 998.0 )  "Cooling water density at the inlet" type: Real
104: singularPressureLoss4.rho:VARIABLE(min = 1e-9 max = 1e5 start = 998.0 unit = "kg/m3" nominal = 998.0 )  "Fluid density" type: Real
105: singularPressureLoss4.deltaP:VARIABLE(unit = "Pa" )  "Singular pressure loss" type: Real
106: condenseur.Pse:VARIABLE(min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 )  "Cooling water pressure at the outlet" type: Real
107: singularPressureLoss4.pro.ddph:VARIABLE(unit = "s2/m2" )  "Derivative of density wrt. pressure at constant specific enthalpy" type: Real
108: singularPressureLoss4.pro.ddhp:VARIABLE(unit = "kg.s2/m5" )  "Derivative of density wrt. specific enthalpy at constant pressure" type: Real
109: singularPressureLoss4.pro.x:VARIABLE(min = 0.0 max = 1.0 unit = "1" )  "Vapor mass fraction" type: Real
110: singularPressureLoss4.T:VARIABLE(min = 200.0 max = 6000.0 start = 290.0 unit = "K" nominal = 300.0 )  "Fluid temperature" type: Real
111: singularPressureLoss4.pro.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 )  "Specific inner energy" type: Real
112: singularPressureLoss4.pro.duph:VARIABLE(unit = "m3/kg" )  "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real
113: singularPressureLoss4.pro.duhp:VARIABLE(unit = "1" )  "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real
114: singularPressureLoss4.pro.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific entropy" type: Real
115: singularPressureLoss4.pro.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific heat capacity at constant presure" type: Real
116: $cse10.duhp:VARIABLE(protected = true )  type: Real unreplaceable
117: $cse10.u:VARIABLE(protected = true )  type: Real unreplaceable
118: singularPressureLoss4.Pm:VARIABLE(min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 )  "Average fluid pressure" type: Real
119: $cse10.cp:VARIABLE(protected = true )  type: Real unreplaceable
120: $cse10.d:VARIABLE(protected = true )  type: Real unreplaceable
121: $cse10.ddhp:VARIABLE(protected = true )  type: Real unreplaceable
122: $cse10.s:VARIABLE(protected = true )  type: Real unreplaceable
123: $cse10.ddph:VARIABLE(protected = true )  type: Real unreplaceable
124: $cse10.duph:VARIABLE(protected = true )  type: Real unreplaceable
125: $cse10.x:VARIABLE(protected = true )  type: Real unreplaceable
126: $cse10.T:VARIABLE(protected = true )  type: Real unreplaceable
127: condenseur.prose.duhp:VARIABLE(unit = "1" )  "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real
128: condenseur.prose.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific heat capacity at constant presure" type: Real
129: condenseur.prose.ddph:VARIABLE(unit = "s2/m2" )  "Derivative of density wrt. pressure at constant specific enthalpy" type: Real
130: condenseur.prose.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 )  "Density" type: Real
131: condenseur.prose.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 )  "Specific inner energy" type: Real
132: $cse6:VARIABLE(protected = true )  type: Real unreplaceable
133: condenseur.Tse:VARIABLE(min = 200.0 max = 6000.0 start = 400.0 unit = "K" nominal = 300.0 )  "Cooling water temperature at the outlet" type: Real
134: condenseur.prose.x:VARIABLE(min = 0.0 max = 1.0 unit = "1" )  "Vapor mass fraction" type: Real
135: condenseur.prose.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific entropy" type: Real
136: condenseur.prose.ddhp:VARIABLE(unit = "kg.s2/m5" )  "Derivative of density wrt. specific enthalpy at constant pressure" type: Real
137: condenseur.prose.duph:VARIABLE(unit = "m3/kg" )  "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real
138: $cse3.u:VARIABLE(protected = true )  type: Real unreplaceable
139: $cse3.s:VARIABLE(protected = true )  type: Real unreplaceable
140: $cse3.duph:VARIABLE(protected = true )  type: Real unreplaceable
141: $cse3.cp:VARIABLE(protected = true )  type: Real unreplaceable
142: $cse3.duhp:VARIABLE(protected = true )  type: Real unreplaceable
143: $cse3.d:VARIABLE(protected = true )  type: Real unreplaceable
144: $cse3.ddph:VARIABLE(protected = true )  type: Real unreplaceable
145: $cse3.x:VARIABLE(protected = true )  type: Real unreplaceable
146: $cse3.T:VARIABLE(protected = true )  type: Real unreplaceable
147: $cse3.ddhp:VARIABLE(protected = true )  type: Real unreplaceable
148: condenseur.Hse:VARIABLE(start = 5e5 unit = "J/kg" )  "Cooling water specific enthalpy at the outlet" type: Real
149: condenseur.W:VARIABLE(unit = "W" )  "Heat power released to the cold source" type: Real
150: condenseur.Tee:VARIABLE(min = 200.0 max = 6000.0 start = 300.0 unit = "K" nominal = 300.0 )  "Cooling water temperature at the inlet" type: Real
151: condenseur.proee.ddhp:VARIABLE(unit = "kg.s2/m5" )  "Derivative of density wrt. specific enthalpy at constant pressure" type: Real
152: condenseur.proee.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 )  "Specific inner energy" type: Real
153: condenseur.proee.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific entropy" type: Real
154: $cse5.duhp:VARIABLE(protected = true )  type: Real unreplaceable
155: $cse5.s:VARIABLE(protected = true )  type: Real unreplaceable
156: $cse5.ddhp:VARIABLE(protected = true )  type: Real unreplaceable
157: $cse5.x:VARIABLE(protected = true )  type: Real unreplaceable
158: condenseur.Pee:VARIABLE(min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 )  "Cooling water pressure at the inlet" type: Real
159: $cse5.duph:VARIABLE(protected = true )  type: Real unreplaceable
160: $cse5.cp:VARIABLE(protected = true )  type: Real unreplaceable
161: $cse5.u:VARIABLE(protected = true )  type: Real unreplaceable
162: $cse5.d:VARIABLE(protected = true )  type: Real unreplaceable
163: $cse5.T:VARIABLE(protected = true )  type: Real unreplaceable
164: singularPressureLoss2.h:VARIABLE(start = 1e5 unit = "J/kg" )  "Fluid specific enthalpy" type: Real
165: singularPressureLoss2.C2.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" )  "Fluid specific enthalpy in the control volume" 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 0.003067/2.12, allocations: 8.179 MB / 0.7644 GB, free: 181.3 MB / 0.5919 GB
Error: post-optimization module createDAEmodeBDAE (simulation) failed.
Error: Internal error SimCode DAEmode: The model ThermoSysPro.Examples.Book.SimpleExamples.HeatExchanger.TestStaticCondenser could not be translated