Running: ./testmodel.py --libraries=/home/hudson/saved_omc/libraries/.openmodelica/libraries --ompython_omhome=/usr ThermoSysPro_ThermoSysPro.Fluid.Examples.SimpleExamples.TestNTUWaterHeater0.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.TestNTUWaterHeater0,tolerance=1e-06,outputFormat="empty",numberOfIntervals=5000,variableFilter="",fileNamePrefix="ThermoSysPro_ThermoSysPro.Fluid.Examples.SimpleExamples.TestNTUWaterHeater0")
translateModel(ThermoSysPro.Fluid.Examples.SimpleExamples.TestNTUWaterHeater0,tolerance=1e-06,outputFormat="empty",numberOfIntervals=5000,variableFilter="",fileNamePrefix="ThermoSysPro_ThermoSysPro.Fluid.Examples.SimpleExamples.TestNTUWaterHeater0")
Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermoSysPro 4.0.0-master/package.mo): time 0.8632/0.8632, allocations: 150.9 MB / 167.2 MB, free: 14.61 MB / 142.1 MB
Notification: Performance of FrontEnd - loaded program: time 0.0003489/0.0003489, allocations: 24.45 kB / 237.8 MB, free: 1.68 MB / 190.1 MB
Notification: Performance of FrontEnd - Absyn->SCode: time 0.0562/0.05656, allocations: 31.34 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.TestNTUWaterHeater0): time 1.645/1.701, allocations: 299.6 MB / 0.5554 GB, free: 8.426 MB / 446.1 MB
Notification: Performance of NFInst.instExpressions: time 0.507/2.208, allocations: 192.5 MB / 0.7434 GB, free: 1.766 MB / 0.5919 GB
Notification: Performance of NFInst.updateImplicitVariability: time 0.001134/2.21, allocations: 21.5 kB / 0.7434 GB, free: 1.766 MB / 0.5919 GB
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermoSysPro 4.0.0-master/Fluid/BoundaryConditions/SourcePQ.mo:74:3-75:65: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/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/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/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).
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermoSysPro 4.0.0-master/Fluid/HeatExchangers/NTUWaterHeater.mo:99:3-101:16:writable] Warning: Connector Ee 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/NTUWaterHeater.mo:102:3-103:65:writable] Warning: Connector Se 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/NTUWaterHeater.mo:104:3-105:83:writable] Warning: Connector Ep 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/NTUWaterHeater.mo:106:3-107:67:writable] Warning: Connector Sp 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/NTUWaterHeater.mo:108:3-110:55:writable] Warning: Connector Ev 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 0.0008555/2.21, allocations: 351.6 kB / 0.7437 GB, free: 1.762 MB / 0.5919 GB
Notification: Performance of NFTyping.typeBindings: time 0.001567/2.212, allocations: 0.6745 MB / 0.7444 GB, free: 1.758 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 0.03478/2.247, allocations: 12.74 MB / 0.7568 GB, free: 1.484 MB / 0.5919 GB
Notification: Performance of NFFlatten.flatten: time 0.002515/2.249, allocations: 2.152 MB / 0.7589 GB, free: 1.48 MB / 0.5919 GB
Notification: Performance of NFFlatten.resolveConnections: time 0.0008866/2.25, allocations: 0.8786 MB / 0.7598 GB, free: 1.363 MB / 0.5919 GB
Notification: Performance of NFEvalConstants.evaluate: time 0.0009952/2.251, allocations: 0.8665 MB / 0.7606 GB, free: 1.363 MB / 0.5919 GB
Notification: Performance of NFSimplifyModel.simplify: time 0.0007238/2.252, allocations: 0.8218 MB / 0.7614 GB, free: 1.363 MB / 0.5919 GB
Notification: Performance of NFPackage.collectConstants: time 0.0001611/2.252, allocations: 159.6 kB / 0.7616 GB, free: 1.363 MB / 0.5919 GB
Notification: Performance of NFFlatten.collectFunctions: time 0.03382/2.286, allocations: 18.17 MB / 0.7793 GB, free: 15.82 MB / 0.6075 GB
Notification: Performance of NFScalarize.scalarize: time 0.0006592/2.287, allocations: 365.6 kB / 0.7797 GB, free: 15.74 MB / 0.6075 GB
Notification: Performance of NFVerifyModel.verify: time 0.001399/2.288, allocations: 0.8894 MB / 0.7805 GB, free: 15.43 MB / 0.6075 GB
Notification: Performance of NFConvertDAE.convert: time 0.0274/2.316, allocations: 10.76 MB / 0.791 GB, free: 11.29 MB / 0.6075 GB
Notification: Performance of FrontEnd - DAE generated: time 7.284e-06/2.316, allocations: 0 / 0.791 GB, free: 11.29 MB / 0.6075 GB
Notification: Performance of FrontEnd: time 3.145e-06/2.316, allocations: 4.891 kB / 0.791 GB, free: 11.29 MB / 0.6075 GB
Notification: Performance of Transformations before backend: time 2.535e-05/2.316, allocations: 0 / 0.791 GB, free: 11.29 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: 499
 * Number of variables: 499
Notification: Performance of Generate backend data structure: time 0.007078/2.323, allocations: 2.922 MB / 0.7939 GB, free: 9.484 MB / 0.6075 GB
Notification: Performance of prepare preOptimizeDAE: time 4.476e-05/2.323, allocations: 8.781 kB / 0.7939 GB, free: 9.484 MB / 0.6075 GB
Notification: Performance of preOpt normalInlineFunction (simulation): time 0.0003167/2.323, allocations: 187.3 kB / 0.7941 GB, free: 9.391 MB / 0.6075 GB
Notification: Performance of preOpt evaluateParameters (simulation): time 0.001098/2.324, allocations: 0.7045 MB / 0.7948 GB, free: 8.844 MB / 0.6075 GB
Notification: Performance of preOpt simplifyIfEquations (simulation): time 0.0002597/2.324, allocations: 226.7 kB / 0.795 GB, free: 8.664 MB / 0.6075 GB
Notification: Performance of preOpt expandDerOperator (simulation): time 0.000173/2.325, allocations: 136.2 kB / 0.7951 GB, free: 8.621 MB / 0.6075 GB
Notification: Performance of preOpt clockPartitioning (simulation): time 0.002597/2.327, allocations: 1.82 MB / 0.7969 GB, free: 7.453 MB / 0.6075 GB
Notification: Performance of preOpt findStateOrder (simulation): time 2.721e-05/2.327, allocations: 5.5 kB / 0.7969 GB, free: 7.453 MB / 0.6075 GB
Notification: Performance of preOpt replaceEdgeChange (simulation): time 0.0001137/2.327, allocations: 56.84 kB / 0.797 GB, free: 7.41 MB / 0.6075 GB
Notification: Performance of preOpt inlineArrayEqn (simulation): time 5.751e-05/2.327, allocations: 74.41 kB / 0.797 GB, free: 7.379 MB / 0.6075 GB
Notification: Performance of preOpt removeEqualRHS (simulation): time 0.002049/2.33, allocations: 1.287 MB / 0.7983 GB, free: 6.742 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 0.1634/2.493, allocations: 70.13 MB / 0.8668 GB, free: 11.39 MB / 0.6856 GB
Notification: Performance of preOpt comSubExp (simulation): time 0.001357/2.494, allocations: 0.8737 MB / 0.8676 GB, free: 10.49 MB / 0.6856 GB
Notification: Performance of preOpt resolveLoops (simulation): time 0.0008891/2.495, allocations: 0.6413 MB / 0.8682 GB, free: 9.824 MB / 0.6856 GB
Notification: Performance of preOpt evalFunc (simulation): time 1.011/3.507, allocations: 411.9 MB / 1.271 GB, free: 173.7 MB / 0.8262 GB
Notification: Performance of preOpt encapsulateWhenConditions (simulation): time 5.743e-05/3.507, allocations: 44.56 kB / 1.271 GB, free: 173.7 MB / 0.8262 GB
Notification: Performance of pre-optimization done (n=200): time 4.178e-06/3.507, allocations: 0 / 1.271 GB, free: 173.7 MB / 0.8262 GB
Notification: Performance of matching and sorting (n=200): time 0.00746/3.514, allocations: 3.423 MB / 1.274 GB, free: 171.2 MB / 0.8262 GB
Notification: Performance of inlineWhenForInitialization (initialization): time 3.648e-05/3.514, allocations: 158.8 kB / 1.274 GB, free: 171 MB / 0.8262 GB
Notification: Performance of selectInitializationVariablesDAE (initialization): time 0.0009217/3.515, allocations: 0.7017 MB / 1.275 GB, free: 170.5 MB / 0.8262 GB
Notification: Performance of collectPreVariables (initialization): time 5.521e-05/3.515, allocations: 36.83 kB / 1.275 GB, free: 170.4 MB / 0.8262 GB
Notification: Performance of collectInitialEqns (initialization): time 0.00031/3.516, allocations: 0.6182 MB / 1.275 GB, free: 169.9 MB / 0.8262 GB
Notification: Performance of collectInitialBindings (initialization): time 0.0003371/3.516, allocations: 0.6465 MB / 1.276 GB, free: 169.3 MB / 0.8262 GB
Notification: Performance of simplifyInitialFunctions (initialization): time 0.0003283/3.516, allocations: 290.7 kB / 1.276 GB, free: 169 MB / 0.8262 GB
Notification: Performance of setup shared object (initialization): time 6.028e-05/3.516, allocations: 349.9 kB / 1.277 GB, free: 168.6 MB / 0.8262 GB
Notification: Performance of preBalanceInitialSystem (initialization): time 0.0007494/3.517, allocations: 0.5388 MB / 1.277 GB, free: 168.1 MB / 0.8262 GB
Notification: Performance of partitionIndependentBlocks (initialization): time 0.0008726/3.518, allocations: 0.9798 MB / 1.278 GB, free: 166.9 MB / 0.8262 GB
Notification: Performance of analyzeInitialSystem (initialization): time 0.001735/3.52, allocations: 1.691 MB / 1.28 GB, free: 165.1 MB / 0.8262 GB
Notification: Performance of solveInitialSystemEqSystem (initialization): time 1.08e-05/3.52, allocations: 4 kB / 1.28 GB, free: 165.1 MB / 0.8262 GB
Notification: Performance of matching and sorting (n=268) (initialization): time 0.003439/3.523, allocations: 2.341 MB / 1.282 GB, free: 162.8 MB / 0.8262 GB
Notification: Performance of prepare postOptimizeDAE: time 2.281e-05/3.523, allocations: 13.16 kB / 1.282 GB, free: 162.8 MB / 0.8262 GB
Notification: Performance of postOpt simplifyComplexFunction (initialization): time 2.801e-05/3.523, allocations: 16.94 kB / 1.282 GB, free: 162.8 MB / 0.8262 GB
Notification: Performance of postOpt tearingSystem (initialization): time 0.00478/3.528, allocations: 2.107 MB / 1.284 GB, free: 160.7 MB / 0.8262 GB
Notification: Performance of postOpt solveSimpleEquations (initialization): time 0.0004604/3.528, allocations: 151 kB / 1.284 GB, free: 160.6 MB / 0.8262 GB
Notification: Performance of postOpt calculateStrongComponentJacobians (initialization): time 0.003059/3.532, allocations: 3.719 MB / 1.288 GB, free: 156.8 MB / 0.8262 GB
Notification: Performance of postOpt simplifyAllExpressions (initialization): time 0.0009547/3.533, allocations: 181.8 kB / 1.288 GB, free: 156.6 MB / 0.8262 GB
Notification: Performance of postOpt collapseArrayExpressions (initialization): time 9.792e-05/3.533, allocations: 59.98 kB / 1.288 GB, free: 156.5 MB / 0.8262 GB
Notification: Model statistics after passing the back-end for initialization:
 * Number of independent subsystems: 61
 * Number of states: 0 ()
 * Number of discrete variables: 26 (nTUWaterHeating.Sp.ftype,Source_condenseur.C.ftype,nTUWaterHeating.Ep.ftype,sourceP.C.ftype,nTUWaterHeating.fluids[1],Puit_condenseur.fluid,singularPressureLoss2.fluid,singularPressureLoss3.fluid,Puit_condenseur1.fluid,singularPressureLoss4.fluid,singularPressureLoss5.fluid,nTUWaterHeating.fluid_e,sourceP.fluid1,Source_condenseur.fluid1,nTUWaterHeating.Sp.diff_on_1,singularPressureLoss5.C2.diff_on_1,nTUWaterHeating.Ev.diff_on_2,sourceP.C.diff_on_2,nTUWaterHeating.Ep.diff_on_2,nTUWaterHeating.Ee.diff_on_2,Source_condenseur.C.diff_on_2,nTUWaterHeating.Se.diff_on_1,singularPressureLoss4.C2.diff_on_1,nTUWaterHeating.Ep.diff_on_1,singularPressureLoss5.C1.diff_on_2,singularPressureLoss3.C2.diff_on_1)
 * Number of discrete states: 0 ()
 * Number of clocked states: 0 ()
 * Top-level inputs: 0
Notification: Strong component statistics for initialization (92):
 * Single equations (assignments): 85
 * Array equations: 0
 * Algorithm blocks: 0
 * Record equations: 3
 * When equations: 0
 * If-equations: 0
 * Equation systems (not torn): 0
 * Torn equation systems: 4
 * 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): 4 systems
   {(1,3), (1,3), (8,21), (1,3)}
Notification: Performance of prepare postOptimizeDAE: time 0.0005307/3.533, allocations: 316.7 kB / 1.288 GB, free: 156.2 MB / 0.8262 GB
Notification: Performance of postOpt lateInlineFunction (simulation): time 0.0002923/3.533, allocations: 111 kB / 1.289 GB, free: 156.1 MB / 0.8262 GB
Notification: Performance of postOpt wrapFunctionCalls (simulation): time 0.003326/3.537, allocations: 2.401 MB / 1.291 GB, free: 153.7 MB / 0.8262 GB
Notification: Performance of postOpt simplifysemiLinear (simulation): time 1.328e-05/3.537, allocations: 3.984 kB / 1.291 GB, free: 153.7 MB / 0.8262 GB
Notification: Performance of postOpt simplifyComplexFunction (simulation): time 1.089e-05/3.537, allocations: 4.938 kB / 1.291 GB, free: 153.7 MB / 0.8262 GB
Notification: Performance of postOpt removeConstants (simulation): time 0.0004577/3.537, allocations: 294.9 kB / 1.291 GB, free: 153.4 MB / 0.8262 GB
Notification: Performance of postOpt simplifyTimeIndepFuncCalls (simulation): time 0.0001618/3.537, allocations: 19.94 kB / 1.291 GB, free: 153.4 MB / 0.8262 GB
Notification: Performance of postOpt simplifyAllExpressions (simulation): time 0.0006615/3.538, allocations: 19.98 kB / 1.291 GB, free: 153.3 MB / 0.8262 GB
Notification: Performance of postOpt findZeroCrossings (simulation): time 0.000156/3.538, allocations: 67.98 kB / 1.291 GB, free: 153.3 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(nTUWaterHeating.lsatC.P, nTUWaterHeating.TsatC, nTUWaterHeating.lsatC.rho, nTUWaterHeating.HsateC, nTUWaterHeating.lsatC.cp, nTUWaterHeating.lsatC.pt, nTUWaterHeating.lsatC.cv), ThermoSysPro.Properties.WaterSteam.Common.PropThermoSat(nTUWaterHeating.vsatC.P, nTUWaterHeating.vsatC.T, nTUWaterHeating.vsatC.rho, nTUWaterHeating.HsatvC, nTUWaterHeating.vsatC.cp, nTUWaterHeating.vsatC.pt, nTUWaterHeating.vsatC.cv)) = ThermoSysPro.Properties.Fluid.Water_sat_P(nTUWaterHeating.P, nTUWaterHeating.fluid)

Variables:
1: nTUWaterHeating.lsatC.rho:VARIABLE(min = 0.0 unit = "kg/m3" )  "Density" type: Real
2: nTUWaterHeating.lsatC.cp:VARIABLE(unit = "J/(kg.K)" )  "Specific heat capacity at constant pressure" type: Real
3: nTUWaterHeating.vsatC.T:VARIABLE(min = 0.0 start = 288.15 unit = "K" nominal = 300.0 )  "Temperature" type: Real
4: nTUWaterHeating.vsatC.P:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 )  "Pressure" type: Real
5: nTUWaterHeating.vsatC.cv:VARIABLE(unit = "J/(kg.K)" )  "Specific heat capacity at constant volume" type: Real
6: nTUWaterHeating.vsatC.rho:VARIABLE(min = 0.0 unit = "kg/m3" )  "Density" type: Real
7: nTUWaterHeating.lsatC.pt:VARIABLE()  "Derivative of pressure wrt. temperature" type: Real
8: nTUWaterHeating.lsatC.P:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 )  "Pressure" type: Real
9: nTUWaterHeating.vsatC.cp:VARIABLE(unit = "J/(kg.K)" )  "Specific heat capacity at constant pressure" type: Real
10: nTUWaterHeating.HsateC:VARIABLE(min = 0.0 start = 3e5 unit = "J/kg" )  "Saturation specific enthalpy of the water at the pressure of the vapor inlet" type: Real
11: nTUWaterHeating.Hep:VARIABLE(start = 981240.7187349163 unit = "J/kg" )  "Mixing specific enthalpy of the drain and the condensate" type: Real
12: nTUWaterHeating.flashepC.duph:VARIABLE(unit = "m3/kg" )  "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real
13: nTUWaterHeating.flashepC.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 )  "Density" type: Real
14: nTUWaterHeating.flashepC.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific heat capacity at constant presure" type: Real
[/var/lib/jenkins1/ws/OpenModelicaLibraryTestingWork/OpenModelica/OMCompiler/Compiler/BackEnd/DAEMode.mo:528:7-530:90:writable] Error: Internal error DAEMode.traverserStrongComponents failed on equation:
1/1 (1): singularPressureLoss3.h = if singularPressureLoss3.Q > 0.0 then 2.6e6 else nTUWaterHeating.h
2/2 (1): singularPressureLoss3.rho = ThermoSysPro.Properties.Fluid.Density_Ph(singularPressureLoss3.Pm, singularPressureLoss3.h, singularPressureLoss3.fluid, singularPressureLoss3.mode, 0.0, 0.0, 0.0, 0.0)
3/3 (1): singularPressureLoss3.deltaP = singularPressureLoss3.K * $cse2 / singularPressureLoss3.rho
4/4 (1): $cse2 = ThermoSysPro.Functions.ThermoSquare(singularPressureLoss3.Q, singularPressureLoss3.eps)
5/5 (1): $cse6 = ThermoSysPro.Correlations.Thermal.WBHeatExchangerEfficiency(singularPressureLoss3.Q, Source_condenseur.Q0, 1e20, nTUWaterHeating.promcF.cp, nTUWaterHeating.KCond, nTUWaterHeating.SCondDes - nTUWaterHeating.SDes, 0.5)
6/6 (1): 0.0 = if nTUWaterHeating.HsatvC < singularPressureLoss3.h then nTUWaterHeating.Wdes - min(singularPressureLoss3.Q * nTUWaterHeating.prodesmC.cp, Source_condenseur.Q0 * nTUWaterHeating.prodesmF.cp) * ThermoSysPro.Correlations.Thermal.WBHeatExchangerEfficiency(singularPressureLoss3.Q, Source_condenseur.Q0, nTUWaterHeating.prodesmC.cp, nTUWaterHeating.prodesmF.cp, 0.5 * nTUWaterHeating.KCond, nTUWaterHeating.SDes, 1.0) * (nTUWaterHeating.proevC.T - nTUWaterHeating.prodesF.T) else nTUWaterHeating.SDes - 1e-9
7/7 (1): 0.0 = if nTUWaterHeating.HsatvC < singularPressureLoss3.h then Source_condenseur.Q0 * (singularPressureLoss4.h - nTUWaterHeating.HDesF) - singularPressureLoss3.Q * (singularPressureLoss3.h - nTUWaterHeating.HsatvC) else nTUWaterHeating.Wdes - 1e-9
8/8 (10): $cse9 = ThermoSysPro.Properties.Fluid.Ph(0.5 * (singularPressureLoss2.C2.P + nTUWaterHeating.Se.P), 0.5 * (singularPressureLoss2.h + singularPressureLoss4.h), nTUWaterHeating.mode_eeF, nTUWaterHeating.fluid_e)
9/18 (10): ThermoSysPro.Properties.WaterSteam.Common.ThermoProperties_ph(nTUWaterHeating.promeF.T, nTUWaterHeating.rho, nTUWaterHeating.promeF.u, nTUWaterHeating.promeF.s, nTUWaterHeating.promeF.cp, nTUWaterHeating.promeF.ddhp, nTUWaterHeating.promeF.ddph, nTUWaterHeating.promeF.duph, nTUWaterHeating.promeF.duhp, nTUWaterHeating.promeF.x) = $cse9
10/28 (10): nTUWaterHeating.prodesF = ThermoSysPro.Properties.Fluid.Ph(nTUWaterHeating.Se.P, nTUWaterHeating.HDesF, nTUWaterHeating.mode_seF, nTUWaterHeating.fluid_e)
11/38 (10): nTUWaterHeating.promcF = ThermoSysPro.Properties.Fluid.Ph(0.5 * (singularPressureLoss2.C2.P + nTUWaterHeating.Se.P), 0.5 * (nTUWaterHeating.HeiF + nTUWaterHeating.HDesF), nTUWaterHeating.mode_mF, nTUWaterHeating.fluid_e)
12/48 (1): nTUWaterHeating.Wcond = Source_condenseur.Q0 * nTUWaterHeating.promcF.cp * $cse6 * (nTUWaterHeating.TsatC - nTUWaterHeating.TeiF)
13/49 (10): nTUWaterHeating.prodesmF = ThermoSysPro.Properties.Fluid.Ph(nTUWaterHeating.Se.P, 0.5 * (nTUWaterHeating.HDesF + singularPressureLoss4.h), nTUWaterHeating.mode_seF, nTUWaterHeating.fluid_e)
14/59 (1): singularPressureLoss2.C2.P - nTUWaterHeating.Se.P = nTUWaterHeating.lambdaE * $cse5 / nTUWaterHeating.rho
15/60 (1): 0.0 = if nTUWaterHeating.HsatvC < singularPressureLoss3.h then nTUWaterHeating.Wdes - Source_condenseur.Q0 * (singularPressureLoss4.h - nTUWaterHeating.HDesF) else nTUWaterHeating.HDesF - singularPressureLoss4.h
16/61 (1): nTUWaterHeating.Wcond = Source_condenseur.Q0 * (nTUWaterHeating.HDesF - nTUWaterHeating.HeiF)
17/62 (1): 0.0 = if noEvent(singularPressureLoss3.h < nTUWaterHeating.HsatvC) then Source_condenseur.Q0 * (nTUWaterHeating.HDesF - nTUWaterHeating.HeiF) - singularPressureLoss3.Q * (singularPressureLoss3.h - nTUWaterHeating.HsateC) else Source_condenseur.Q0 * (nTUWaterHeating.HDesF - nTUWaterHeating.HeiF) - singularPressureLoss3.Q * (nTUWaterHeating.HsatvC - nTUWaterHeating.HsateC)
18/63 (10): nTUWaterHeating.prodesmC = ThermoSysPro.Properties.Fluid.Ph(nTUWaterHeating.P, 0.5 * (nTUWaterHeating.HsatvC + singularPressureLoss3.h), nTUWaterHeating.mode_evC, nTUWaterHeating.fluid)
19/73 (10): nTUWaterHeating.proevC = ThermoSysPro.Properties.Fluid.Ph(nTUWaterHeating.P, singularPressureLoss3.h, nTUWaterHeating.mode_evC, nTUWaterHeating.fluid)
20/83 (10): nTUWaterHeating.prosp = ThermoSysPro.Properties.Fluid.Ph(nTUWaterHeating.P, nTUWaterHeating.Hep, nTUWaterHeating.mode_spC, nTUWaterHeating.fluid)
21/93 (1): nTUWaterHeating.Wpurge = $cse7 * $cse8 * (nTUWaterHeating.prosp.T - nTUWaterHeating.proeeF.T)
22/94 (1): $cse8 = ThermoSysPro.Correlations.Thermal.WBHeatExchangerEfficiency(singularPressureLoss3.Q, Source_condenseur.Q0, nTUWaterHeating.prompC.cp, nTUWaterHeating.prompF.cp, nTUWaterHeating.KPurge, 656.0, 0.0)
23/95 (1): $cse7 = min(singularPressureLoss3.Q * nTUWaterHeating.prompC.cp, Source_condenseur.Q0 * nTUWaterHeating.prompF.cp)
24/96 (10): nTUWaterHeating.prompC = ThermoSysPro.Properties.Fluid.Ph(nTUWaterHeating.P, 0.5 * (nTUWaterHeating.Hep + singularPressureLoss5.h), nTUWaterHeating.mode_spC, nTUWaterHeating.fluid)
25/106 (1): singularPressureLoss5.h = ThermoSysPro.Functions.SmoothCond(singularPressureLoss3.Q / nTUWaterHeating.gamma0, nTUWaterHeating.h, 1e5, 1.0)
26/107 (1): 0.0 = singularPressureLoss3.Q * (nTUWaterHeating.Hep - singularPressureLoss5.h) + Source_condenseur.Q0 * (singularPressureLoss2.h - nTUWaterHeating.HeiF)
27/108 (10): nTUWaterHeating.prompF = ThermoSysPro.Properties.Fluid.Ph(singularPressureLoss2.C2.P, 0.5 * (singularPressureLoss2.h + nTUWaterHeating.HeiF), nTUWaterHeating.mode_eeF, nTUWaterHeating.fluid_e)
28/118 (10): $cse10 = ThermoSysPro.Properties.Fluid.Ph(singularPressureLoss2.C2.P, nTUWaterHeating.HeiF, nTUWaterHeating.mode_eeF, nTUWaterHeating.fluid_e)
29/128 (10): ThermoSysPro.Properties.WaterSteam.Common.ThermoProperties_ph(nTUWaterHeating.TeiF, nTUWaterHeating.proecF.d, nTUWaterHeating.proecF.u, nTUWaterHeating.proecF.s, nTUWaterHeating.proecF.cp, nTUWaterHeating.proecF.ddhp, nTUWaterHeating.proecF.ddph, nTUWaterHeating.proecF.duph, nTUWaterHeating.proecF.duhp, nTUWaterHeating.proecF.x) = $cse10
30/138 (1): nTUWaterHeating.Wpurge = Source_condenseur.Q0 * (nTUWaterHeating.HeiF - singularPressureLoss2.h)
31/139 (10): nTUWaterHeating.flashepC = ThermoSysPro.Properties.Fluid.Ph(nTUWaterHeating.P, 1e5, nTUWaterHeating.mode_flash, nTUWaterHeating.fluid)
32/149 (1): 0.0 = if nTUWaterHeating.flashepC.x > 0.0 then nTUWaterHeating.Hep - nTUWaterHeating.HsateC else singularPressureLoss3.Q * (nTUWaterHeating.Hep - nTUWaterHeating.HsateC)
33/150 (14): (ThermoSysPro.Properties.WaterSteam.Common.PropThermoSat(nTUWaterHeating.lsatC.P, nTUWaterHeating.TsatC, nTUWaterHeating.lsatC.rho, nTUWaterHeating.HsateC, nTUWaterHeating.lsatC.cp, nTUWaterHeating.lsatC.pt, nTUWaterHeating.lsatC.cv), ThermoSysPro.Properties.WaterSteam.Common.PropThermoSat(nTUWaterHeating.vsatC.P, nTUWaterHeating.vsatC.T, nTUWaterHeating.vsatC.rho, nTUWaterHeating.HsatvC, nTUWaterHeating.vsatC.cp, nTUWaterHeating.vsatC.pt, nTUWaterHeating.vsatC.cv)) = ThermoSysPro.Properties.Fluid.Water_sat_P(nTUWaterHeating.P, nTUWaterHeating.fluid)
34/164 (1): singularPressureLoss3.Pm = 0.5 * (sourceP.P0 + nTUWaterHeating.P)
35/165 (1): singularPressureLoss3.deltaP = sourceP.P0 - nTUWaterHeating.P

Variables:
1: singularPressureLoss3.deltaP:VARIABLE(unit = "Pa" )  "Singular pressure loss" type: Real
2: singularPressureLoss3.Pm:VARIABLE(min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 )  "Average fluid pressure" type: Real
3: nTUWaterHeating.lsatC.rho:VARIABLE(min = 0.0 unit = "kg/m3" )  "Density" type: Real
4: nTUWaterHeating.lsatC.cp:VARIABLE(unit = "J/(kg.K)" )  "Specific heat capacity at constant pressure" type: Real
5: nTUWaterHeating.vsatC.T:VARIABLE(min = 0.0 start = 288.15 unit = "K" nominal = 300.0 )  "Temperature" type: Real
6: nTUWaterHeating.vsatC.P:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 )  "Pressure" type: Real
7: nTUWaterHeating.vsatC.cv:VARIABLE(unit = "J/(kg.K)" )  "Specific heat capacity at constant volume" type: Real
8: nTUWaterHeating.vsatC.rho:VARIABLE(min = 0.0 unit = "kg/m3" )  "Density" type: Real
9: nTUWaterHeating.lsatC.pt:VARIABLE()  "Derivative of pressure wrt. temperature" type: Real
10: nTUWaterHeating.lsatC.P:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 )  "Pressure" type: Real
11: nTUWaterHeating.vsatC.cp:VARIABLE(unit = "J/(kg.K)" )  "Specific heat capacity at constant pressure" type: Real
12: nTUWaterHeating.HsateC:VARIABLE(min = 0.0 start = 3e5 unit = "J/kg" )  "Saturation specific enthalpy of the water at the pressure of the vapor inlet" type: Real
13: nTUWaterHeating.Hep:VARIABLE(start = 981240.7187349163 unit = "J/kg" )  "Mixing specific enthalpy of the drain and the condensate" type: Real
14: nTUWaterHeating.flashepC.duph:VARIABLE(unit = "m3/kg" )  "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real
15: nTUWaterHeating.flashepC.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 )  "Density" type: Real
16: nTUWaterHeating.flashepC.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific heat capacity at constant presure" type: Real
17: nTUWaterHeating.flashepC.ddhp:VARIABLE(unit = "kg.s2/m5" )  "Derivative of density wrt. specific enthalpy at constant pressure" type: Real
18: nTUWaterHeating.flashepC.T:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 320.0 )  "Temperature" type: Real
19: nTUWaterHeating.flashepC.x:VARIABLE(min = 0.0 max = 1.0 unit = "1" )  "Vapor mass fraction" type: Real
20: nTUWaterHeating.flashepC.ddph:VARIABLE(unit = "s2/m2" )  "Derivative of density wrt. pressure at constant specific enthalpy" type: Real
21: nTUWaterHeating.flashepC.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 )  "Specific inner energy" type: Real
22: nTUWaterHeating.flashepC.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific entropy" type: Real
23: nTUWaterHeating.flashepC.duhp:VARIABLE(unit = "1" )  "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real
24: nTUWaterHeating.Wpurge:VARIABLE(start = 1.0 unit = "W" )  "Energy transfer during drain cooling" type: Real
25: nTUWaterHeating.proecF.x:VARIABLE(min = 0.0 max = 1.0 unit = "1" )  "Vapor mass fraction" type: Real
26: nTUWaterHeating.proecF.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 )  "Specific inner energy" type: Real
27: nTUWaterHeating.proecF.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 )  "Density" type: Real
28: nTUWaterHeating.proecF.ddph:VARIABLE(unit = "s2/m2" )  "Derivative of density wrt. pressure at constant specific enthalpy" type: Real
29: nTUWaterHeating.proecF.ddhp:VARIABLE(unit = "kg.s2/m5" )  "Derivative of density wrt. specific enthalpy at constant pressure" type: Real
30: nTUWaterHeating.proecF.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific heat capacity at constant presure" type: Real
31: nTUWaterHeating.TeiF:VARIABLE(min = 200.0 max = 6000.0 start = 400.0 unit = "K" nominal = 300.0 )  "Fluid temperature after drain cooling" type: Real
32: nTUWaterHeating.proecF.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific entropy" type: Real
33: nTUWaterHeating.proecF.duph:VARIABLE(unit = "m3/kg" )  "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real
34: nTUWaterHeating.proecF.duhp:VARIABLE(unit = "1" )  "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real
35: $cse10.d:VARIABLE(protected = true )  type: Real unreplaceable
36: $cse10.u:VARIABLE(protected = true )  type: Real unreplaceable
37: $cse10.duhp:VARIABLE(protected = true )  type: Real unreplaceable
38: $cse10.duph:VARIABLE(protected = true )  type: Real unreplaceable
39: $cse10.ddhp:VARIABLE(protected = true )  type: Real unreplaceable
40: $cse10.x:VARIABLE(protected = true )  type: Real unreplaceable
41: $cse10.cp:VARIABLE(protected = true )  type: Real unreplaceable
42: $cse10.ddph:VARIABLE(protected = true )  type: Real unreplaceable
43: $cse10.T:VARIABLE(protected = true )  type: Real unreplaceable
44: $cse10.s:VARIABLE(protected = true )  type: Real unreplaceable
45: nTUWaterHeating.prompF.duph:VARIABLE(unit = "m3/kg" )  "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real
46: nTUWaterHeating.prompF.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific heat capacity at constant presure" type: Real
47: nTUWaterHeating.prompF.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 )  "Density" type: Real
48: nTUWaterHeating.prompF.x:VARIABLE(min = 0.0 max = 1.0 unit = "1" )  "Vapor mass fraction" type: Real
49: nTUWaterHeating.prompF.duhp:VARIABLE(unit = "1" )  "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real
50: nTUWaterHeating.prompF.T:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 320.0 )  "Temperature" type: Real
51: nTUWaterHeating.prompF.ddhp:VARIABLE(unit = "kg.s2/m5" )  "Derivative of density wrt. specific enthalpy at constant pressure" type: Real
52: nTUWaterHeating.prompF.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 )  "Specific inner energy" type: Real
53: nTUWaterHeating.prompF.ddph:VARIABLE(unit = "s2/m2" )  "Derivative of density wrt. pressure at constant specific enthalpy" type: Real
54: nTUWaterHeating.prompF.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific entropy" type: Real
55: nTUWaterHeating.HeiF:VARIABLE(start = 878162.3337936474 unit = "J/kg" )  "Fluid specific enthalpy after drain cooling" type: Real
56: nTUWaterHeating.h:VARIABLE(start = 1e6 unit = "J/kg" )  "Fluid specific enthalpy" type: Real
57: singularPressureLoss5.h:VARIABLE(start = 1e5 unit = "J/kg" )  "Fluid specific enthalpy" type: Real
58: nTUWaterHeating.prompC.duhp:VARIABLE(unit = "1" )  "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real
59: nTUWaterHeating.prompC.ddph:VARIABLE(unit = "s2/m2" )  "Derivative of density wrt. pressure at constant specific enthalpy" type: Real
60: nTUWaterHeating.prompC.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 )  "Specific inner energy" type: Real
61: nTUWaterHeating.prompC.T:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 320.0 )  "Temperature" type: Real
62: nTUWaterHeating.prompC.duph:VARIABLE(unit = "m3/kg" )  "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real
63: nTUWaterHeating.prompC.ddhp:VARIABLE(unit = "kg.s2/m5" )  "Derivative of density wrt. specific enthalpy at constant pressure" type: Real
64: nTUWaterHeating.prompC.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 )  "Density" type: Real
65: nTUWaterHeating.prompC.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific entropy" type: Real
66: nTUWaterHeating.prompC.x:VARIABLE(min = 0.0 max = 1.0 unit = "1" )  "Vapor mass fraction" type: Real
67: $cse7:VARIABLE(protected = true )  type: Real unreplaceable
68: nTUWaterHeating.prompC.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific heat capacity at constant presure" type: Real
69: $cse8:VARIABLE(protected = true )  type: Real unreplaceable
70: nTUWaterHeating.prosp.duhp:VARIABLE(unit = "1" )  "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real
71: nTUWaterHeating.prosp.ddhp:VARIABLE(unit = "kg.s2/m5" )  "Derivative of density wrt. specific enthalpy at constant pressure" type: Real
72: nTUWaterHeating.prosp.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific entropy" type: Real
73: nTUWaterHeating.prosp.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific heat capacity at constant presure" type: Real
74: nTUWaterHeating.prosp.duph:VARIABLE(unit = "m3/kg" )  "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real
75: nTUWaterHeating.prosp.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 )  "Specific inner energy" type: Real
76: nTUWaterHeating.prosp.ddph:VARIABLE(unit = "s2/m2" )  "Derivative of density wrt. pressure at constant specific enthalpy" type: Real
77: nTUWaterHeating.prosp.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 )  "Density" type: Real
78: nTUWaterHeating.prosp.x:VARIABLE(min = 0.0 max = 1.0 unit = "1" )  "Vapor mass fraction" type: Real
79: nTUWaterHeating.prosp.T:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 320.0 )  "Temperature" type: Real
80: nTUWaterHeating.proevC.ddhp:VARIABLE(unit = "kg.s2/m5" )  "Derivative of density wrt. specific enthalpy at constant pressure" type: Real
81: nTUWaterHeating.proevC.x:VARIABLE(min = 0.0 max = 1.0 unit = "1" )  "Vapor mass fraction" type: Real
82: nTUWaterHeating.proevC.duph:VARIABLE(unit = "m3/kg" )  "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real
83: nTUWaterHeating.proevC.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 )  "Density" type: Real
84: nTUWaterHeating.proevC.T:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 320.0 )  "Temperature" type: Real
85: nTUWaterHeating.proevC.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific heat capacity at constant presure" type: Real
86: nTUWaterHeating.proevC.duhp:VARIABLE(unit = "1" )  "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real
87: nTUWaterHeating.proevC.ddph:VARIABLE(unit = "s2/m2" )  "Derivative of density wrt. pressure at constant specific enthalpy" type: Real
88: nTUWaterHeating.proevC.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 )  "Specific inner energy" type: Real
89: nTUWaterHeating.proevC.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific entropy" type: Real
90: nTUWaterHeating.P:VARIABLE(min = 0.0 start = 1e6 unit = "Pa" nominal = 1e5 )  "Fluid pressure" type: Real
91: nTUWaterHeating.lsatC.cv:VARIABLE(unit = "J/(kg.K)" )  "Specific heat capacity at constant volume" type: Real
92: nTUWaterHeating.vsatC.pt:VARIABLE()  "Derivative of pressure wrt. temperature" type: Real
93: nTUWaterHeating.TsatC:VARIABLE(min = 0.0 start = 400.0 unit = "K" nominal = 300.0 )  "Saturation temperature" type: Real
94: nTUWaterHeating.prodesmC.ddph:VARIABLE(unit = "s2/m2" )  "Derivative of density wrt. pressure at constant specific enthalpy" type: Real
95: nTUWaterHeating.prodesmC.ddhp:VARIABLE(unit = "kg.s2/m5" )  "Derivative of density wrt. specific enthalpy at constant pressure" type: Real
96: nTUWaterHeating.prodesmC.duhp:VARIABLE(unit = "1" )  "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real
97: nTUWaterHeating.prodesmC.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific heat capacity at constant presure" type: Real
98: nTUWaterHeating.prodesmC.duph:VARIABLE(unit = "m3/kg" )  "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real
99: nTUWaterHeating.prodesmC.x:VARIABLE(min = 0.0 max = 1.0 unit = "1" )  "Vapor mass fraction" type: Real
100: nTUWaterHeating.prodesmC.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 )  "Specific inner energy" type: Real
101: nTUWaterHeating.prodesmC.T:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 320.0 )  "Temperature" type: Real
102: nTUWaterHeating.prodesmC.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 )  "Density" type: Real
103: nTUWaterHeating.prodesmC.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific entropy" type: Real
104: nTUWaterHeating.HsatvC:VARIABLE(min = 0.0 start = 2.5e6 unit = "J/kg" )  "Saturation specific enthalpy of the vapor at the pressure of the vapor inlet" type: Real
105: nTUWaterHeating.Wcond:VARIABLE(start = 1.0 unit = "W" )  "Energy transfer during condensation" type: Real
106: nTUWaterHeating.HDesF:VARIABLE(start = 980281.0129225359 unit = "J/kg" )  "Fluid specific enthalpy after deheating" type: Real
107: nTUWaterHeating.rho:VARIABLE(min = 1e-9 max = 1e5 start = 1000.0 unit = "kg/m3" nominal = 998.0 )  "Average water density" type: Real
108: nTUWaterHeating.prodesmF.ddhp:VARIABLE(unit = "kg.s2/m5" )  "Derivative of density wrt. specific enthalpy at constant pressure" type: Real
109: nTUWaterHeating.prodesmF.x:VARIABLE(min = 0.0 max = 1.0 unit = "1" )  "Vapor mass fraction" type: Real
110: nTUWaterHeating.prodesmF.T:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 320.0 )  "Temperature" type: Real
111: nTUWaterHeating.prodesmF.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific entropy" type: Real
112: nTUWaterHeating.prodesmF.duhp:VARIABLE(unit = "1" )  "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real
113: nTUWaterHeating.prodesmF.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 )  "Density" type: Real
114: nTUWaterHeating.prodesmF.ddph:VARIABLE(unit = "s2/m2" )  "Derivative of density wrt. pressure at constant specific enthalpy" type: Real
115: nTUWaterHeating.prodesmF.duph:VARIABLE(unit = "m3/kg" )  "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real
116: nTUWaterHeating.prodesmF.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 )  "Specific inner energy" type: Real
117: nTUWaterHeating.prodesmF.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific heat capacity at constant presure" type: Real
118: $cse6:VARIABLE(protected = true )  type: Real unreplaceable
119: nTUWaterHeating.promcF.ddph:VARIABLE(unit = "s2/m2" )  "Derivative of density wrt. pressure at constant specific enthalpy" type: Real
120: nTUWaterHeating.promcF.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific heat capacity at constant presure" type: Real
121: nTUWaterHeating.promcF.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 )  "Density" type: Real
122: nTUWaterHeating.promcF.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific entropy" type: Real
123: nTUWaterHeating.promcF.ddhp:VARIABLE(unit = "kg.s2/m5" )  "Derivative of density wrt. specific enthalpy at constant pressure" type: Real
124: nTUWaterHeating.promcF.duph:VARIABLE(unit = "m3/kg" )  "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real
125: nTUWaterHeating.promcF.x:VARIABLE(min = 0.0 max = 1.0 unit = "1" )  "Vapor mass fraction" type: Real
126: nTUWaterHeating.promcF.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 )  "Specific inner energy" type: Real
127: nTUWaterHeating.promcF.T:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 320.0 )  "Temperature" type: Real
128: nTUWaterHeating.promcF.duhp:VARIABLE(unit = "1" )  "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real
129: nTUWaterHeating.prodesF.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific entropy" type: Real
130: nTUWaterHeating.prodesF.x:VARIABLE(min = 0.0 max = 1.0 unit = "1" )  "Vapor mass fraction" type: Real
131: nTUWaterHeating.prodesF.ddph:VARIABLE(unit = "s2/m2" )  "Derivative of density wrt. pressure at constant specific enthalpy" type: Real
132: nTUWaterHeating.prodesF.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific heat capacity at constant presure" type: Real
133: nTUWaterHeating.prodesF.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 )  "Density" type: Real
134: nTUWaterHeating.prodesF.duhp:VARIABLE(unit = "1" )  "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real
135: nTUWaterHeating.prodesF.duph:VARIABLE(unit = "m3/kg" )  "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real
136: nTUWaterHeating.prodesF.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 )  "Specific inner energy" type: Real
137: nTUWaterHeating.prodesF.T:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 320.0 )  "Temperature" type: Real
138: nTUWaterHeating.prodesF.ddhp:VARIABLE(unit = "kg.s2/m5" )  "Derivative of density wrt. specific enthalpy at constant pressure" type: Real
139: $cse9.duph:VARIABLE(protected = true )  type: Real unreplaceable
140: nTUWaterHeating.promeF.ddph:VARIABLE(unit = "s2/m2" )  "Derivative of density wrt. pressure at constant specific enthalpy" type: Real
141: nTUWaterHeating.promeF.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 )  "Specific inner energy" type: Real
142: nTUWaterHeating.promeF.T:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 320.0 )  "Temperature" type: Real
143: nTUWaterHeating.promeF.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific heat capacity at constant presure" type: Real
144: nTUWaterHeating.promeF.duph:VARIABLE(unit = "m3/kg" )  "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real
145: nTUWaterHeating.promeF.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific entropy" type: Real
146: nTUWaterHeating.promeF.ddhp:VARIABLE(unit = "kg.s2/m5" )  "Derivative of density wrt. specific enthalpy at constant pressure" type: Real
147: nTUWaterHeating.promeF.x:VARIABLE(min = 0.0 max = 1.0 unit = "1" )  "Vapor mass fraction" type: Real
148: nTUWaterHeating.promeF.duhp:VARIABLE(unit = "1" )  "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real
149: $cse9.ddph:VARIABLE(protected = true )  type: Real unreplaceable
150: $cse9.d:VARIABLE(protected = true )  type: Real unreplaceable
151: $cse9.cp:VARIABLE(protected = true )  type: Real unreplaceable
152: $cse9.ddhp:VARIABLE(protected = true )  type: Real unreplaceable
153: $cse9.u:VARIABLE(protected = true )  type: Real unreplaceable
154: $cse9.duhp:VARIABLE(protected = true )  type: Real unreplaceable
155: $cse9.s:VARIABLE(protected = true )  type: Real unreplaceable
156: nTUWaterHeating.Se.P:VARIABLE(flow=false start = 8e6 unit = "Pa" )  "Fluid pressure in the control volume" type: Real
157: $cse9.x:VARIABLE(protected = true )  type: Real unreplaceable
158: $cse9.T:VARIABLE(protected = true )  type: Real unreplaceable
159: singularPressureLoss4.h:VARIABLE(start = 1e5 unit = "J/kg" )  "Fluid specific enthalpy" type: Real
160: nTUWaterHeating.Wdes:VARIABLE(start = 1.0 unit = "W" )  "Energy transfer during deheating" type: Real
161: nTUWaterHeating.SDes:VARIABLE(start = 1e-9 unit = "m2" )  "Heat exchange surface for deheating" type: Real
162: singularPressureLoss3.Q:VARIABLE(start = 100.0 unit = "kg/s" )  "Mass flow rate" type: Real
163: $cse2:VARIABLE(protected = true )  type: Real unreplaceable
164: singularPressureLoss3.rho:VARIABLE(min = 0.0 start = 998.0 unit = "kg/m3" )  "Fluid density" type: Real
165: singularPressureLoss3.h:VARIABLE(start = 1e5 unit = "J/kg" )  "Fluid specific enthalpy" 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 0.003548/3.542, allocations: 8.872 MB / 1.3 GB, free: 143.1 MB / 0.8262 GB
Error: post-optimization module createDAEmodeBDAE (simulation) failed.
Error: Internal error SimCode DAEmode: The model ThermoSysPro.Fluid.Examples.SimpleExamples.TestNTUWaterHeater0 could not be translated