Running: ./testmodel.py --libraries=/home/hudson/saved_omc/libraries/.openmodelica/libraries --ompython_omhome=/usr ThermoSysPro_ThermoSysPro.Fluid.Examples.SimpleExamples.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.Fluid.Examples.SimpleExamples.TestStaticCondenser,tolerance=1e-06,outputFormat="empty",numberOfIntervals=5000,variableFilter="",fileNamePrefix="ThermoSysPro_ThermoSysPro.Fluid.Examples.SimpleExamples.TestStaticCondenser")
translateModel(ThermoSysPro.Fluid.Examples.SimpleExamples.TestStaticCondenser,tolerance=1e-06,outputFormat="empty",numberOfIntervals=5000,variableFilter="",fileNamePrefix="ThermoSysPro_ThermoSysPro.Fluid.Examples.SimpleExamples.TestStaticCondenser")
Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermoSysPro 4.0.0-master/package.mo): time 0.8053/0.8053, allocations: 150.9 MB / 167.2 MB, free: 14.52 MB / 142.1 MB
Notification: Performance of FrontEnd - loaded program: time 0.0003311/0.0003311, allocations: 17.34 kB / 237.8 MB, free: 1.766 MB / 190.1 MB
Notification: Performance of FrontEnd - Absyn->SCode: time 0.05401/0.05436, allocations: 31.35 MB / 269.1 MB, free: 7.035 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.TestStaticCondenser): time 1.592/1.647, allocations: 300.1 MB / 0.5559 GB, free: 7.586 MB / 446.1 MB
Notification: Performance of NFInst.instExpressions: time 0.5101/2.157, allocations: 192.6 MB / 0.744 GB, free: 1.746 MB / 0.5919 GB
Notification: Performance of NFInst.updateImplicitVariability: time 0.0008692/2.158, allocations: 33.56 kB / 0.744 GB, free: 1.746 MB / 0.5919 GB
[/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/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/HeatExchangers/StaticCondenser.mo:100:3-102:24:writable] Warning: Connector Cee 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/StaticCondenser.mo:103:3-105:38:writable] Warning: Connector Cse 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/StaticCondenser.mo:106:3-108:66:writable] Warning: Connector Cex 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/StaticCondenser.mo:109:3-110:83:writable] Warning: Connector Cvt 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/StaticCondenser.mo:130:3-131:83:writable] Warning: Connector Cep 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/StaticCondenser.mo:133:3-135:17:writable] Warning: Connector Cev 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/SourceP.mo:58:3-59:65: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).
[/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).
[/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).
[/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).
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermoSysPro 4.0.0-master/Fluid/BoundaryConditions/Sink.mo:39:3-40:67: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/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).
[/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 0.000817/2.159, allocations: 328.4 kB / 0.7444 GB, free: 1.742 MB / 0.5919 GB
Notification: Performance of NFTyping.typeBindings: time 0.001162/2.16, allocations: 0.6298 MB / 0.745 GB, free: 1.738 MB / 0.5919 GB
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermoSysPro 4.0.0-master/Properties/WaterSteam/IF97_packages.mo:783:9-783:27:writable] Warning: cv was used before it was defined (given a value). Additional such uses may exist for the variable, but some messages were suppressed.
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermoSysPro 4.0.0-master/Properties/WaterSteam/IF97_packages.mo:850:9-850:27:writable] Warning: cv was used before it was defined (given a value). Additional such uses may exist for the variable, but some messages were suppressed.
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermoSysPro 4.0.0-master/Properties/WaterSteam/IF97_packages.mo:1088:9-1088:27:writable] Warning: cv was used before it was defined (given a value). Additional such uses may exist for the variable, but some messages were suppressed.
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermoSysPro 4.0.0-master/Properties/WaterSteamSimple/prop4_Ph.mo:69:3-69:60:writable] Warning: dh1satp was used before it was defined (given a value). Additional such uses may exist for the variable, but some messages were suppressed.
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermoSysPro 4.0.0-master/Properties/WaterSteamSimple/prop4_Ph.mo:69:3-69:60:writable] Warning: dh2satp was used before it was defined (given a value). Additional such uses may exist for the variable, but some messages were suppressed.
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermoSysPro 4.0.0-master/Properties/WaterSteamSimple/prop4_Ph_der.mo:167:3-170:49:writable] Warning: du1satp_der was used before it was defined (given a value). Additional such uses may exist for the variable, but some messages were suppressed.
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermoSysPro 4.0.0-master/Properties/WaterSteamSimple/prop4_Ph_der.mo:167:3-170:49:writable] Warning: du2satp_der was used before it was defined (given a value). Additional such uses may exist for the variable, but some messages were suppressed.
[/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.
Notification: Performance of NFTyping.typeClassSections: time 0.03277/2.193, allocations: 12.62 MB / 0.7573 GB, free: 1.465 MB / 0.5919 GB
Notification: Performance of NFFlatten.flatten: time 0.003758/2.196, allocations: 2.181 MB / 0.7594 GB, free: 1.457 MB / 0.5919 GB
Notification: Performance of NFFlatten.resolveConnections: time 0.001795/2.198, allocations: 1.177 MB / 0.7606 GB, free: 17.29 MB / 0.6075 GB
Notification: Performance of NFEvalConstants.evaluate: time 0.001308/2.2, allocations: 0.896 MB / 0.7615 GB, free: 17.29 MB / 0.6075 GB
Notification: Performance of NFSimplifyModel.simplify: time 0.0008487/2.2, allocations: 0.939 MB / 0.7624 GB, free: 17.27 MB / 0.6075 GB
Notification: Performance of NFPackage.collectConstants: time 0.0002075/2.201, allocations: 190.6 kB / 0.7626 GB, free: 17.27 MB / 0.6075 GB
Notification: Performance of NFFlatten.collectFunctions: time 0.04136/2.242, allocations: 21.48 MB / 0.7835 GB, free: 14.44 MB / 0.6075 GB
Notification: Performance of NFScalarize.scalarize: time 0.0005539/2.243, allocations: 432.4 kB / 0.7839 GB, free: 14.3 MB / 0.6075 GB
Notification: Performance of NFVerifyModel.verify: time 0.001612/2.244, allocations: 1.023 MB / 0.7849 GB, free: 13.95 MB / 0.6075 GB
Notification: Performance of NFConvertDAE.convert: time 0.03007/2.274, allocations: 12.23 MB / 0.7969 GB, free: 8.16 MB / 0.6075 GB
Notification: Performance of FrontEnd - DAE generated: time 6.222e-06/2.274, allocations: 0 / 0.7969 GB, free: 8.16 MB / 0.6075 GB
Notification: Performance of FrontEnd: time 3.817e-06/2.274, allocations: 0.6562 kB / 0.7969 GB, free: 8.16 MB / 0.6075 GB
Notification: Performance of Transformations before backend: time 3.223e-05/2.274, allocations: 3.938 kB / 0.7969 GB, free: 8.156 MB / 0.6075 GB
Notification: Model statistics after passing the front-end and creating the data structures used by the back-end:
 * Number of equations: 528
 * Number of variables: 528
Notification: Performance of Generate backend data structure: time 0.009098/2.283, allocations: 3.265 MB / 0.8001 GB, free: 5.809 MB / 0.6075 GB
Notification: Performance of prepare preOptimizeDAE: time 4.831e-05/2.284, allocations: 9 kB / 0.8001 GB, free: 5.801 MB / 0.6075 GB
Notification: Performance of preOpt normalInlineFunction (simulation): time 0.000383/2.284, allocations: 229.4 kB / 0.8003 GB, free: 5.574 MB / 0.6075 GB
Notification: Performance of preOpt evaluateParameters (simulation): time 0.001256/2.285, allocations: 0.8504 MB / 0.8011 GB, free: 4.742 MB / 0.6075 GB
Notification: Performance of preOpt simplifyIfEquations (simulation): time 0.0001079/2.285, allocations: 139.8 kB / 0.8013 GB, free: 4.605 MB / 0.6075 GB
Notification: Performance of preOpt expandDerOperator (simulation): time 0.0001825/2.285, allocations: 187.9 kB / 0.8015 GB, free: 4.426 MB / 0.6075 GB
Notification: Performance of preOpt clockPartitioning (simulation): time 0.002826/2.288, allocations: 1.928 MB / 0.8033 GB, free: 2.383 MB / 0.6075 GB
Notification: Performance of preOpt findStateOrder (simulation): time 3.968e-05/2.288, allocations: 8.031 kB / 0.8033 GB, free: 2.379 MB / 0.6075 GB
Notification: Performance of preOpt replaceEdgeChange (simulation): time 0.000138/2.289, allocations: 79.98 kB / 0.8034 GB, free: 2.301 MB / 0.6075 GB
Notification: Performance of preOpt inlineArrayEqn (simulation): time 5.749e-05/2.289, allocations: 59.98 kB / 0.8035 GB, free: 2.242 MB / 0.6075 GB
Notification: Performance of preOpt removeEqualRHS (simulation): time 0.002252/2.291, allocations: 1.31 MB / 0.8048 GB, free: 0.9609 MB / 0.6075 GB
Warning: The model contains alias variables with redundant start and/or conflicting nominal values. It is recommended to resolve the conflicts, because otherwise the system could be hard to solve. To print the conflicting alias sets and the chosen candidates please use -d=aliasConflicts.
Notification: Performance of preOpt removeSimpleEquations (simulation): time 0.2271/2.518, allocations: 106.8 MB / 0.9091 GB, free: 13.02 MB / 0.7325 GB
Notification: Performance of preOpt comSubExp (simulation): time 0.001213/2.519, allocations: 0.646 MB / 0.9097 GB, free: 12.34 MB / 0.7325 GB
Notification: Performance of preOpt resolveLoops (simulation): time 0.0004637/2.52, allocations: 332.3 kB / 0.91 GB, free: 12 MB / 0.7325 GB
Notification: Performance of preOpt evalFunc (simulation): time 0.779/3.299, allocations: 236.9 MB / 1.141 GB, free: 117.6 MB / 0.8262 GB
Notification: Performance of preOpt encapsulateWhenConditions (simulation): time 4.456e-05/3.299, allocations: 46.03 kB / 1.141 GB, free: 117.6 MB / 0.8262 GB
Notification: Performance of pre-optimization done (n=96): time 5.37e-06/3.299, allocations: 1.359 kB / 1.141 GB, free: 117.6 MB / 0.8262 GB
Notification: Performance of matching and sorting (n=96): time 0.008046/3.307, allocations: 2.528 MB / 1.144 GB, free: 115.4 MB / 0.8262 GB
Notification: Performance of inlineWhenForInitialization (initialization): time 3.058e-05/3.307, allocations: 161.3 kB / 1.144 GB, free: 115.2 MB / 0.8262 GB
Notification: Performance of selectInitializationVariablesDAE (initialization): time 0.001205/3.308, allocations: 0.956 MB / 1.145 GB, free: 114.5 MB / 0.8262 GB
Notification: Performance of collectPreVariables (initialization): time 4.276e-05/3.308, allocations: 32.7 kB / 1.145 GB, free: 114.5 MB / 0.8262 GB
Notification: Performance of collectInitialEqns (initialization): time 0.0003954/3.309, allocations: 0.8532 MB / 1.146 GB, free: 113.9 MB / 0.8262 GB
Notification: Performance of collectInitialBindings (initialization): time 0.0002006/3.309, allocations: 339.7 kB / 1.146 GB, free: 113.7 MB / 0.8262 GB
Notification: Performance of simplifyInitialFunctions (initialization): time 0.000376/3.309, allocations: 326.2 kB / 1.146 GB, free: 113.4 MB / 0.8262 GB
Notification: Performance of setup shared object (initialization): time 9.169e-05/3.309, allocations: 354.9 kB / 1.147 GB, free: 113.1 MB / 0.8262 GB
Notification: Performance of preBalanceInitialSystem (initialization): time 0.0005763/3.31, allocations: 329.8 kB / 1.147 GB, free: 112.9 MB / 0.8262 GB
Notification: Performance of partitionIndependentBlocks (initialization): time 0.0007294/3.311, allocations: 0.8697 MB / 1.148 GB, free: 112 MB / 0.8262 GB
Notification: Performance of analyzeInitialSystem (initialization): time 0.001343/3.312, allocations: 1.264 MB / 1.149 GB, free: 110.8 MB / 0.8262 GB
Notification: Performance of solveInitialSystemEqSystem (initialization): time 1.738e-05/3.312, allocations: 4 kB / 1.149 GB, free: 110.8 MB / 0.8262 GB
Notification: Performance of matching and sorting (n=207) (initialization): time 0.003103/3.315, allocations: 1.776 MB / 1.151 GB, free: 109.6 MB / 0.8262 GB
Notification: Performance of prepare postOptimizeDAE: time 2.918e-05/3.315, allocations: 12.94 kB / 1.151 GB, free: 109.6 MB / 0.8262 GB
Notification: Performance of postOpt simplifyComplexFunction (initialization): time 3.913e-05/3.315, allocations: 20 kB / 1.151 GB, free: 109.6 MB / 0.8262 GB
Notification: Performance of postOpt tearingSystem (initialization): time 0.002922/3.318, allocations: 1.037 MB / 1.152 GB, free: 108.7 MB / 0.8262 GB
Notification: Performance of postOpt solveSimpleEquations (initialization): time 0.0005419/3.319, allocations: 206.1 kB / 1.152 GB, free: 108.5 MB / 0.8262 GB
Notification: Performance of postOpt calculateStrongComponentJacobians (initialization): time 0.002383/3.321, allocations: 4.393 MB / 1.156 GB, free: 104.3 MB / 0.8262 GB
Notification: Performance of postOpt simplifyAllExpressions (initialization): time 0.001045/3.322, allocations: 184.9 kB / 1.157 GB, free: 104.1 MB / 0.8262 GB
Notification: Performance of postOpt collapseArrayExpressions (initialization): time 9.86e-05/3.322, allocations: 72.23 kB / 1.157 GB, free: 104 MB / 0.8262 GB
Notification: Model statistics after passing the back-end for initialization:
 * Number of independent subsystems: 80
 * Number of states: 0 ()
 * Number of discrete variables: 35 (condenseur.Cex.ftype,Source_condenseur.C.ftype,sourceP.C.ftype,sourceP2.C.ftype,sourceP1.C.ftype,condenseur.fluids[1],Puit_condenseur.fluid,condenseur.fluid_p,singularPressureLoss.fluid,singularPressureLoss1.fluid,singularPressureLoss2.fluid,singularPressureLoss3.fluid,Puit_condenseur1.fluid,singularPressureLoss4.fluid,singularPressureLoss5.fluid,sourceP2.fluid1,sourceP1.fluid1,sourceP.fluid1,Source_condenseur.fluid1,singularPressureLoss5.C1.diff_on_2,condenseur.Cex.diff_on_1,singularPressureLoss5.C2.diff_on_1,condenseur.Cee.diff_on_2,Source_condenseur.C.diff_on_2,condenseur.Cse.diff_on_1,singularPressureLoss4.C2.diff_on_1,condenseur.Cvt.diff_on_2,sourceP.C.diff_on_2,singularPressureLoss3.C2.diff_on_1,condenseur.Cep.diff_on_2,sourceP2.C.diff_on_2,singularPressureLoss1.C2.diff_on_1,condenseur.Cev.diff_on_2,sourceP1.C.diff_on_2,singularPressureLoss.C2.diff_on_1)
 * Number of discrete states: 0 ()
 * Number of clocked states: 0 ()
 * Top-level inputs: 0
Notification: Strong component statistics for initialization (134):
 * Single equations (assignments): 127
 * Array equations: 0
 * Algorithm blocks: 0
 * Record equations: 0
 * When equations: 0
 * If-equations: 0
 * Equation systems (not torn): 0
 * Torn equation systems: 7
 * 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): 7 systems
   {(1,3), (1,1), (1,3), (1,3), (1,3), (1,3), (3,15)}
Notification: Performance of prepare postOptimizeDAE: time 0.0005369/3.323, allocations: 339.5 kB / 1.157 GB, free: 103.8 MB / 0.8262 GB
Notification: Performance of postOpt lateInlineFunction (simulation): time 0.0002985/3.323, allocations: 118.5 kB / 1.157 GB, free: 103.7 MB / 0.8262 GB
Notification: Performance of postOpt wrapFunctionCalls (simulation): time 0.002092/3.325, allocations: 1.48 MB / 1.159 GB, free: 102.8 MB / 0.8262 GB
Notification: Performance of postOpt simplifysemiLinear (simulation): time 1.126e-05/3.325, allocations: 0 / 1.159 GB, free: 102.8 MB / 0.8262 GB
Notification: Performance of postOpt simplifyComplexFunction (simulation): time 9.608e-06/3.325, allocations: 0 / 1.159 GB, free: 102.8 MB / 0.8262 GB
Notification: Performance of postOpt removeConstants (simulation): time 0.0004141/3.326, allocations: 266.5 kB / 1.159 GB, free: 102.5 MB / 0.8262 GB
Notification: Performance of postOpt simplifyTimeIndepFuncCalls (simulation): time 0.000161/3.326, allocations: 11 kB / 1.159 GB, free: 102.5 MB / 0.8262 GB
Notification: Performance of postOpt simplifyAllExpressions (simulation): time 0.00059/3.326, allocations: 14.98 kB / 1.159 GB, free: 102.5 MB / 0.8262 GB
Notification: Performance of postOpt findZeroCrossings (simulation): time 0.0001195/3.326, allocations: 59.98 kB / 1.159 GB, free: 102.4 MB / 0.8262 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 (14): (ThermoSysPro.Properties.WaterSteam.Common.PropThermoSat(condenseur.lsat1.P, condenseur.lsat1.T, condenseur.lsat1.rho, condenseur.Hml, condenseur.lsat1.cp, condenseur.lsat1.pt, condenseur.lsat1.cv), condenseur.vsat1) = ThermoSysPro.Properties.Fluid.Water_sat_P(condenseur.Pcond, condenseur.fluid)

Variables:
1: condenseur.lsat1.pt:VARIABLE()  "Derivative of pressure wrt. temperature" type: Real
2: condenseur.vsat1.cv:VARIABLE(unit = "J/(kg.K)" )  "Specific heat capacity at constant volume" type: Real
3: condenseur.lsat1.T:VARIABLE(min = 0.0 start = 288.15 unit = "K" nominal = 300.0 )  "Temperature" type: Real
4: condenseur.vsat1.T:VARIABLE(min = 0.0 start = 288.15 unit = "K" nominal = 300.0 )  "Temperature" type: Real
5: condenseur.lsat1.P:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 )  "Pressure" type: Real
6: condenseur.vsat1.P:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 )  "Pressure" type: Real
7: condenseur.vsat1.h:VARIABLE(unit = "J/kg" )  "Specific enthalpy" type: Real
8: condenseur.lsat1.cp:VARIABLE(unit = "J/(kg.K)" )  "Specific heat capacity at constant pressure" type: Real
9: condenseur.vsat1.pt:VARIABLE()  "Derivative of pressure wrt. temperature" type: Real
10: condenseur.lsat1.rho:VARIABLE(min = 0.0 unit = "kg/m3" )  "Density" type: Real
11: condenseur.Tsat:VARIABLE(min = 0.0 start = 500.0 unit = "K" nominal = 300.0 )  "Water temperature at the saturation point" type: Real
12: condenseur.Pcond:VARIABLE(min = 0.0 start = 2154.77 unit = "Pa" fixed = false nominal = 1e5 )  "Vapor pressure inside the condenser" type: Real
13: condenseur.vsat1.rho:VARIABLE(min = 0.0 unit = "kg/m3" )  "Density" type: Real
14: condenseur.lsat1.cv:VARIABLE(unit = "J/(kg.K)" )  "Specific heat capacity at constant volume" 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 (10): $cse3 = ThermoSysPro.Properties.Fluid.Ph(condenseur.Pee, singularPressureLoss2.h, condenseur.mode_ee, condenseur.fluid_p)
2/11 (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) = $cse3
3/21 (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
4/22 (10): $cse5 = ThermoSysPro.Properties.Fluid.Ph(condenseur.Pse, singularPressureLoss4.h, condenseur.mode_se, condenseur.fluid_p)
5/32 (1): $cse2 = exp(condenseur.XKCO * condenseur.SCO * (condenseur.Tee - condenseur.Tse) / condenseur.W)
6/33 (1): condenseur.XKCO = condenseur.KCO * condenseur.COP * condenseur.KT2 * $cse1 / (condenseur.COPR * condenseur.KT1)
7/34 (1): condenseur.KT2 = 52.0 + 3.3 * (-273.16 + condenseur.Tee) + (-0.05) * (-273.16 + condenseur.Tee) ^ 2.0
8/35 (1): 0.0 = condenseur.Tsat + (condenseur.Tee - condenseur.Tsat) * $cse2 - condenseur.Tse
9/36 (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) = $cse5
10/46 (1): singularPressureLoss4.Pm = 0.5 * (condenseur.Pse + Puit_condenseur.P0)
11/47 (1): singularPressureLoss4.rho = ThermoSysPro.Properties.Fluid.Density_Ph(singularPressureLoss4.Pm, singularPressureLoss4.h, singularPressureLoss4.fluid, singularPressureLoss4.mode, 0.0, 0.0, 0.0, 0.0)
12/48 (1): condenseur.W = Source_condenseur.Q0 * (singularPressureLoss4.h - singularPressureLoss2.h)
13/49 (1): 0.0 = singularPressureLoss3.Q * singularPressureLoss3.h + singularPressureLoss.Q * singularPressureLoss.h + singularPressureLoss1.Q * singularPressureLoss1.h + (-condenseur.W) - singularPressureLoss5.Q * singularPressureLoss5.h
14/50 (1): singularPressureLoss.rho = ThermoSysPro.Properties.Fluid.Density_Ph(singularPressureLoss.Pm, singularPressureLoss.h, singularPressureLoss.fluid, singularPressureLoss.mode, 0.0, 0.0, 0.0, 0.0)
15/51 (1): singularPressureLoss.deltaP = singularPressureLoss.K * $cse6 / singularPressureLoss.rho
16/52 (1): $cse6 = ThermoSysPro.Functions.ThermoSquare(singularPressureLoss.Q, singularPressureLoss.eps)
17/53 (1): singularPressureLoss.h = if singularPressureLoss.Q > 0.0 then 2.5481e6 else condenseur.Hml
18/54 (1): condenseur.Pcond = ThermoSysPro.Properties.Fluid.P_sat(condenseur.Tsat, condenseur.fluid)
19/55 (14): (ThermoSysPro.Properties.WaterSteam.Common.PropThermoSat(condenseur.lsat1.P, condenseur.lsat1.T, condenseur.lsat1.rho, condenseur.Hml, condenseur.lsat1.cp, condenseur.lsat1.pt, condenseur.lsat1.cv), condenseur.vsat1) = ThermoSysPro.Properties.Fluid.Water_sat_P(condenseur.Pcond, condenseur.fluid)
20/69 (1): singularPressureLoss3.Pm = 0.5 * (sourceP.P0 + condenseur.Pcond)
21/70 (1): singularPressureLoss3.rho = ThermoSysPro.Properties.Fluid.Density_Ph(singularPressureLoss3.Pm, singularPressureLoss3.h, singularPressureLoss3.fluid, singularPressureLoss3.mode, 0.0, 0.0, 0.0, 0.0)
22/71 (1): singularPressureLoss3.deltaP = singularPressureLoss3.K * $cse9 / singularPressureLoss3.rho
23/72 (1): $cse9 = ThermoSysPro.Functions.ThermoSquare(singularPressureLoss3.Q, singularPressureLoss3.eps)
24/73 (1): singularPressureLoss3.h = if singularPressureLoss3.Q > 0.0 then 2.5817e6 else condenseur.Hml
25/74 (1): 0.0 = singularPressureLoss3.Q + singularPressureLoss.Q + singularPressureLoss1.Q - singularPressureLoss5.Q
26/75 (1): singularPressureLoss5.h = if singularPressureLoss5.Q > 0.0 then condenseur.Hml else 1e5
27/76 (1): singularPressureLoss3.deltaP = sourceP.P0 - condenseur.Pcond
28/77 (1): singularPressureLoss1.Pm = 0.5 * (sourceP2.P0 + condenseur.Pcond)
29/78 (1): singularPressureLoss1.rho = ThermoSysPro.Properties.Fluid.Density_Ph(singularPressureLoss1.Pm, singularPressureLoss1.h, singularPressureLoss1.fluid, singularPressureLoss1.mode, 0.0, 0.0, 0.0, 0.0)
30/79 (1): singularPressureLoss1.deltaP = singularPressureLoss1.K * $cse7 / singularPressureLoss1.rho
31/80 (1): $cse7 = ThermoSysPro.Functions.ThermoSquare(singularPressureLoss1.Q, singularPressureLoss1.eps)
32/81 (1): singularPressureLoss1.h = if singularPressureLoss1.Q > 0.0 then 2.5055e6 else condenseur.Hml
33/82 (1): singularPressureLoss1.deltaP = sourceP2.P0 - condenseur.Pcond
34/83 (1): singularPressureLoss.Pm = 0.5 * (sourceP1.P0 + condenseur.Pcond)
35/84 (1): singularPressureLoss.deltaP = sourceP1.P0 - condenseur.Pcond
36/85 (1): singularPressureLoss4.deltaP = condenseur.Pse - Puit_condenseur.P0
37/86 (1): singularPressureLoss4.deltaP = singularPressureLoss4.K * $cse10 / singularPressureLoss4.rho

Variables:
1: singularPressureLoss4.rho:VARIABLE(min = 0.0 start = 998.0 unit = "kg/m3" )  "Fluid density" type: Real
2: singularPressureLoss4.deltaP:VARIABLE(unit = "Pa" )  "Singular pressure loss" type: Real
3: singularPressureLoss.deltaP:VARIABLE(unit = "Pa" )  "Singular pressure loss" type: Real
4: singularPressureLoss.Pm:VARIABLE(min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 )  "Average fluid pressure" type: Real
5: singularPressureLoss1.deltaP:VARIABLE(unit = "Pa" )  "Singular pressure loss" type: Real
6: singularPressureLoss1.h:VARIABLE(start = 1e5 unit = "J/kg" )  "Fluid specific enthalpy" type: Real
7: singularPressureLoss1.Q:VARIABLE(start = 1e-5 unit = "kg/s" fixed = true )  "Mass flow rate" type: Real
8: $cse7:VARIABLE(protected = true )  type: Real unreplaceable
9: singularPressureLoss1.rho:VARIABLE(min = 0.0 start = 998.0 unit = "kg/m3" )  "Fluid density" type: Real
10: singularPressureLoss1.Pm:VARIABLE(min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 )  "Average fluid pressure" type: Real
11: singularPressureLoss3.deltaP:VARIABLE(unit = "Pa" )  "Singular pressure loss" type: Real
12: singularPressureLoss5.h:VARIABLE(start = 1e5 unit = "J/kg" )  "Fluid specific enthalpy" type: Real
13: singularPressureLoss5.Q:VARIABLE(start = 100.0 unit = "kg/s" )  "Mass flow rate" type: Real
14: singularPressureLoss3.h:VARIABLE(start = 1e5 unit = "J/kg" )  "Fluid specific enthalpy" type: Real
15: singularPressureLoss3.Q:VARIABLE(start = 100.0 unit = "kg/s" fixed = true )  "Mass flow rate" type: Real
16: $cse9:VARIABLE(protected = true )  type: Real unreplaceable
17: singularPressureLoss3.rho:VARIABLE(min = 0.0 start = 998.0 unit = "kg/m3" )  "Fluid density" type: Real
18: singularPressureLoss3.Pm:VARIABLE(min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 )  "Average fluid pressure" type: Real
19: condenseur.lsat1.pt:VARIABLE()  "Derivative of pressure wrt. temperature" type: Real
20: condenseur.vsat1.cv:VARIABLE(unit = "J/(kg.K)" )  "Specific heat capacity at constant volume" type: Real
21: condenseur.lsat1.T:VARIABLE(min = 0.0 start = 288.15 unit = "K" nominal = 300.0 )  "Temperature" type: Real
22: condenseur.vsat1.T:VARIABLE(min = 0.0 start = 288.15 unit = "K" nominal = 300.0 )  "Temperature" type: Real
23: condenseur.lsat1.P:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 )  "Pressure" type: Real
24: condenseur.vsat1.P:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 )  "Pressure" type: Real
25: condenseur.vsat1.h:VARIABLE(unit = "J/kg" )  "Specific enthalpy" type: Real
26: condenseur.lsat1.cp:VARIABLE(unit = "J/(kg.K)" )  "Specific heat capacity at constant pressure" type: Real
27: condenseur.vsat1.pt:VARIABLE()  "Derivative of pressure wrt. temperature" type: Real
28: condenseur.lsat1.rho:VARIABLE(min = 0.0 unit = "kg/m3" )  "Density" type: Real
29: condenseur.Tsat:VARIABLE(min = 0.0 start = 500.0 unit = "K" nominal = 300.0 )  "Water temperature at the saturation point" type: Real
30: condenseur.Pcond:VARIABLE(min = 0.0 start = 2154.77 unit = "Pa" fixed = false nominal = 1e5 )  "Vapor pressure inside the condenser" type: Real
31: condenseur.vsat1.rho:VARIABLE(min = 0.0 unit = "kg/m3" )  "Density" type: Real
32: condenseur.lsat1.cv:VARIABLE(unit = "J/(kg.K)" )  "Specific heat capacity at constant volume" type: Real
33: condenseur.vsat1.cp:VARIABLE(unit = "J/(kg.K)" )  "Specific heat capacity at constant pressure" type: Real
34: condenseur.Hml:VARIABLE(start = 2.5e5 unit = "J/kg" )  "Extraction water average specific enthalpy" type: Real
35: singularPressureLoss.Q:VARIABLE(start = 1e-5 unit = "kg/s" fixed = true )  "Mass flow rate" type: Real
36: $cse6:VARIABLE(protected = true )  type: Real unreplaceable
37: singularPressureLoss.rho:VARIABLE(min = 0.0 start = 998.0 unit = "kg/m3" )  "Fluid density" type: Real
38: singularPressureLoss.h:VARIABLE(start = 1e5 unit = "J/kg" )  "Fluid specific enthalpy" type: Real
39: condenseur.W:VARIABLE(unit = "W" )  "Heat power released to the cold source" type: Real
40: singularPressureLoss4.h:VARIABLE(start = 1e5 unit = "J/kg" )  "Fluid specific enthalpy" type: Real
41: singularPressureLoss4.Pm:VARIABLE(min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 )  "Average fluid pressure" type: Real
42: condenseur.prose.duph:VARIABLE(unit = "m3/kg" )  "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real
43: condenseur.prose.ddph:VARIABLE(unit = "s2/m2" )  "Derivative of density wrt. pressure at constant specific enthalpy" type: Real
44: condenseur.prose.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific heat capacity at constant presure" type: Real
45: condenseur.prose.ddhp:VARIABLE(unit = "kg.s2/m5" )  "Derivative of density wrt. specific enthalpy at constant pressure" type: Real
46: condenseur.prose.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific entropy" type: Real
47: condenseur.prose.duhp:VARIABLE(unit = "1" )  "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real
48: $cse2:VARIABLE(protected = true )  type: Real unreplaceable
49: 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
50: condenseur.KT2:VARIABLE(start = 50.0 unit = "W/(m2.K)" )  "Second reference value for the exchange coefficient" type: Real
51: condenseur.XKCO:VARIABLE(start = 200.0 unit = "W/(m2.K)" )  "Heat transfer coefficient" type: Real
52: 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
53: condenseur.prose.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 )  "Specific inner energy" type: Real
54: condenseur.prose.x:VARIABLE(min = 0.0 max = 1.0 unit = "1" )  "Vapor mass fraction" type: Real
55: condenseur.prose.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 )  "Density" type: Real
56: $cse5.ddph:VARIABLE(protected = true )  type: Real unreplaceable
57: $cse5.duhp:VARIABLE(protected = true )  type: Real unreplaceable
58: $cse5.x:VARIABLE(protected = true )  type: Real unreplaceable
59: $cse5.ddhp:VARIABLE(protected = true )  type: Real unreplaceable
60: $cse5.duph:VARIABLE(protected = true )  type: Real unreplaceable
61: $cse5.s:VARIABLE(protected = true )  type: Real unreplaceable
62: $cse5.u:VARIABLE(protected = true )  type: Real unreplaceable
63: $cse5.cp:VARIABLE(protected = true )  type: Real unreplaceable
64: $cse5.d:VARIABLE(protected = true )  type: Real unreplaceable
65: $cse5.T:VARIABLE(protected = true )  type: Real unreplaceable
66: condenseur.Pse:VARIABLE(min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 )  "Cooling water pressure at the outlet" type: Real
67: condenseur.proee.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific heat capacity at constant presure" type: Real
68: 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
69: condenseur.proee.ddph:VARIABLE(unit = "s2/m2" )  "Derivative of density wrt. pressure at constant specific enthalpy" type: Real
70: condenseur.proee.ddhp:VARIABLE(unit = "kg.s2/m5" )  "Derivative of density wrt. specific enthalpy at constant pressure" type: Real
71: condenseur.proee.duph:VARIABLE(unit = "m3/kg" )  "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real
72: condenseur.proee.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific entropy" type: Real
73: condenseur.proee.duhp:VARIABLE(unit = "1" )  "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real
74: condenseur.proee.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 )  "Specific inner energy" type: Real
75: $cse3.x:VARIABLE(protected = true )  type: Real unreplaceable
76: condenseur.proee.x:VARIABLE(min = 0.0 max = 1.0 unit = "1" )  "Vapor mass fraction" type: Real
77: $cse3.ddph:VARIABLE(protected = true )  type: Real unreplaceable
78: $cse3.cp:VARIABLE(protected = true )  type: Real unreplaceable
79: $cse3.s:VARIABLE(protected = true )  type: Real unreplaceable
80: $cse3.d:VARIABLE(protected = true )  type: Real unreplaceable
81: $cse3.ddhp:VARIABLE(protected = true )  type: Real unreplaceable
82: $cse3.u:VARIABLE(protected = true )  type: Real unreplaceable
83: $cse3.duph:VARIABLE(protected = true )  type: Real unreplaceable
84: condenseur.Pee:VARIABLE(min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 )  "Cooling water pressure at the inlet" type: Real
85: $cse3.duhp:VARIABLE(protected = true )  type: Real unreplaceable
86: $cse3.T: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 0.002435/3.329, allocations: 3.269 MB / 1.162 GB, free: 98.55 MB / 0.8262 GB
Error: post-optimization module createDAEmodeBDAE (simulation) failed.
Error: Internal error SimCode DAEmode: The model ThermoSysPro.Fluid.Examples.SimpleExamples.TestStaticCondenser could not be translated