Running: ./testmodel.py --libraries=/home/hudson/saved_omc/libraries/.openmodelica/libraries --ompython_omhome=/usr ThermoSysPro_ThermoSysPro.Examples.SimpleExamples.TestNTUWaterHeating0.conf.json
loadFile("/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermoSysPro 4.0.0-master/package.mo", uses=false)
Using package ThermoSysPro with version 4.0 (/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermoSysPro 4.0.0-master/package.mo)
Running command: translateModel(ThermoSysPro.Examples.SimpleExamples.TestNTUWaterHeating0,tolerance=1e-06,outputFormat="empty",numberOfIntervals=5000,variableFilter="",fileNamePrefix="ThermoSysPro_ThermoSysPro.Examples.SimpleExamples.TestNTUWaterHeating0")
translateModel(ThermoSysPro.Examples.SimpleExamples.TestNTUWaterHeating0,tolerance=1e-06,outputFormat="empty",numberOfIntervals=5000,variableFilter="",fileNamePrefix="ThermoSysPro_ThermoSysPro.Examples.SimpleExamples.TestNTUWaterHeating0")
Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermoSysPro 4.0.0-master/package.mo): time 0.823/0.823, allocations: 150.9 MB / 167.2 MB, free: 14.54 MB / 142.1 MB
Notification: Performance of FrontEnd - loaded program: time 0.0003582/0.0003582, allocations: 21.11 kB / 237.8 MB, free: 1.781 MB / 190.1 MB
Notification: Performance of FrontEnd - Absyn->SCode: time 0.05006/0.05044, allocations: 31.35 MB / 269.1 MB, free: 7.031 MB / 222.1 MB
Notification: Automatically loaded package Complex 4.0.0 due to uses annotation from Modelica.
Notification: Automatically loaded package ModelicaServices 4.0.0 due to uses annotation from Modelica.
Notification: Automatically loaded package Modelica 4.0.0 due to usage.
Notification: Performance of NFInst.instantiate(ThermoSysPro.Examples.SimpleExamples.TestNTUWaterHeating0): time 1.639/1.689, allocations: 298.2 MB / 0.5541 GB, free: 9.5 MB / 446.1 MB
Notification: Performance of NFInst.instExpressions: time 0.04352/1.733, allocations: 37.06 MB / 0.5902 GB, free: 4.293 MB / 478.1 MB
Notification: Performance of NFInst.updateImplicitVariability: time 0.0006877/1.734, allocations: 15.94 kB / 0.5903 GB, free: 4.277 MB / 478.1 MB
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermoSysPro 4.0.0-master/WaterSteam/BoundaryConditions/SourcePQ.mo:29:3-30:52: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/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/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/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/NTUWaterHeating.mo:65:3-67:38:writable] Warning: Connector Ee 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/NTUWaterHeating.mo:68:3-70:36:writable] Warning: Connector Se 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/NTUWaterHeating.mo:71:3-73:37:writable] Warning: Connector Ep 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/NTUWaterHeating.mo:74:3-76:38:writable] Warning: Connector Sp 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/NTUWaterHeating.mo:77:3-79:36:writable] Warning: Connector Ev 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 0.0007938/1.735, allocations: 280.4 kB / 0.5905 GB, free: 4.004 MB / 478.1 MB
Notification: Performance of NFTyping.typeBindings: time 0.001224/1.736, allocations: 460.3 kB / 0.591 GB, free: 3.551 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 0.02538/1.761, allocations: 10.23 MB / 0.601 GB, free: 9.301 MB / 494.1 MB
Notification: Performance of NFFlatten.flatten: time 0.001812/1.763, allocations: 1.599 MB / 0.6025 GB, free: 7.691 MB / 494.1 MB
Notification: Performance of NFFlatten.resolveConnections: time 0.0005014/1.763, allocations: 464.3 kB / 0.603 GB, free: 7.23 MB / 494.1 MB
Notification: Performance of NFEvalConstants.evaluate: time 0.0006567/1.764, allocations: 0.611 MB / 0.6036 GB, free: 6.617 MB / 494.1 MB
Notification: Performance of NFSimplifyModel.simplify: time 0.0004965/1.765, allocations: 0.4937 MB / 0.604 GB, free: 6.121 MB / 494.1 MB
Notification: Performance of NFPackage.collectConstants: time 9.845e-05/1.765, allocations: 84 kB / 0.6041 GB, free: 6.039 MB / 494.1 MB
Notification: Performance of NFFlatten.collectFunctions: time 0.02717/1.792, allocations: 15.97 MB / 0.6197 GB, free: 6.051 MB / 0.4981 GB
Notification: Performance of NFScalarize.scalarize: time 0.0002129/1.792, allocations: 195.1 kB / 0.6199 GB, free: 5.859 MB / 0.4981 GB
Notification: Performance of NFVerifyModel.verify: time 0.0007292/1.793, allocations: 0.579 MB / 0.6205 GB, free: 5.277 MB / 0.4981 GB
Notification: Performance of NFConvertDAE.convert: time 0.02012/1.813, allocations: 8.868 MB / 0.6291 GB, free: 12.39 MB / 0.5137 GB
Notification: Performance of FrontEnd - DAE generated: time 6.392e-06/1.813, allocations: 0 / 0.6291 GB, free: 12.39 MB / 0.5137 GB
Notification: Performance of FrontEnd: time 1.924e-06/1.813, allocations: 0 / 0.6291 GB, free: 12.39 MB / 0.5137 GB
Notification: Performance of Transformations before backend: time 1.424e-05/1.813, allocations: 0 / 0.6291 GB, free: 12.39 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: 367
 * Number of variables: 367
Notification: Performance of Generate backend data structure: time 0.005052/1.818, allocations: 2.146 MB / 0.6312 GB, free: 10.18 MB / 0.5137 GB
Notification: Performance of prepare preOptimizeDAE: time 4.632e-05/1.818, allocations: 12.03 kB / 0.6312 GB, free: 10.17 MB / 0.5137 GB
Notification: Performance of preOpt normalInlineFunction (simulation): time 0.0001601/1.818, allocations: 118.3 kB / 0.6313 GB, free: 10.05 MB / 0.5137 GB
Notification: Performance of preOpt evaluateParameters (simulation): time 0.0004625/1.819, allocations: 441 kB / 0.6318 GB, free: 9.582 MB / 0.5137 GB
Notification: Performance of preOpt simplifyIfEquations (simulation): time 0.0001771/1.819, allocations: 172.8 kB / 0.6319 GB, free: 9.391 MB / 0.5137 GB
Notification: Performance of preOpt expandDerOperator (simulation): time 8.694e-05/1.819, allocations: 72 kB / 0.632 GB, free: 9.32 MB / 0.5137 GB
Notification: Performance of preOpt clockPartitioning (simulation): time 0.00157/1.821, allocations: 1.265 MB / 0.6332 GB, free: 7.98 MB / 0.5137 GB
Notification: Performance of preOpt findStateOrder (simulation): time 2.151e-05/1.821, allocations: 7.875 kB / 0.6332 GB, free: 7.973 MB / 0.5137 GB
Notification: Performance of preOpt replaceEdgeChange (simulation): time 6.161e-05/1.821, allocations: 32 kB / 0.6333 GB, free: 7.941 MB / 0.5137 GB
Notification: Performance of preOpt inlineArrayEqn (simulation): time 5.141e-05/1.821, allocations: 67.92 kB / 0.6333 GB, free: 7.875 MB / 0.5137 GB
Notification: Performance of preOpt removeEqualRHS (simulation): time 0.001292/1.822, allocations: 0.9003 MB / 0.6342 GB, free: 6.969 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 0.004473/1.827, allocations: 5.788 MB / 0.6399 GB, free: 0.6836 MB / 0.5137 GB
Notification: Performance of preOpt comSubExp (simulation): time 0.001126/1.828, allocations: 0.8004 MB / 0.6407 GB, free: 15.87 MB / 0.5294 GB
Notification: Performance of preOpt resolveLoops (simulation): time 0.0007674/1.829, allocations: 0.6534 MB / 0.6413 GB, free: 15.21 MB / 0.5294 GB
Notification: Performance of preOpt evalFunc (simulation): time 0.4006/2.229, allocations: 111.4 MB / 0.7501 GB, free: 186.5 MB / 0.5919 GB
Notification: Performance of preOpt encapsulateWhenConditions (simulation): time 3.107e-05/2.229, allocations: 43.34 kB / 0.7501 GB, free: 186.5 MB / 0.5919 GB
Notification: Performance of pre-optimization done (n=233): time 4.158e-06/2.229, allocations: 2.969 kB / 0.7501 GB, free: 186.5 MB / 0.5919 GB
Notification: Performance of matching and sorting (n=233): time 0.007923/2.237, allocations: 3.532 MB / 0.7536 GB, free: 186 MB / 0.5919 GB
Notification: Performance of inlineWhenForInitialization (initialization): time 1.936e-05/2.237, allocations: 56.09 kB / 0.7536 GB, free: 186 MB / 0.5919 GB
Notification: Performance of selectInitializationVariablesDAE (initialization): time 0.0003938/2.238, allocations: 424 kB / 0.754 GB, free: 185.8 MB / 0.5919 GB
Notification: Performance of collectPreVariables (initialization): time 3.307e-05/2.238, allocations: 33.58 kB / 0.7541 GB, free: 185.8 MB / 0.5919 GB
Notification: Performance of collectInitialEqns (initialization): time 0.0001444/2.238, allocations: 294.8 kB / 0.7543 GB, free: 185.6 MB / 0.5919 GB
Notification: Performance of collectInitialBindings (initialization): time 0.0003024/2.238, allocations: 0.7346 MB / 0.7551 GB, free: 185.1 MB / 0.5919 GB
Notification: Performance of simplifyInitialFunctions (initialization): time 0.0002102/2.238, allocations: 202.5 kB / 0.7552 GB, free: 185 MB / 0.5919 GB
Notification: Performance of setup shared object (initialization): time 5.463e-05/2.238, allocations: 336.7 kB / 0.7556 GB, free: 184.7 MB / 0.5919 GB
Notification: Performance of preBalanceInitialSystem (initialization): time 0.0005526/2.239, allocations: 482 kB / 0.756 GB, free: 184.7 MB / 0.5919 GB
Notification: Performance of partitionIndependentBlocks (initialization): time 0.0006338/2.24, allocations: 0.706 MB / 0.7567 GB, free: 184.4 MB / 0.5919 GB
Notification: Performance of analyzeInitialSystem (initialization): time 0.001349/2.241, allocations: 1.361 MB / 0.758 GB, free: 184 MB / 0.5919 GB
Notification: Performance of solveInitialSystemEqSystem (initialization): time 4.087e-06/2.241, allocations: 0 / 0.758 GB, free: 184 MB / 0.5919 GB
Notification: Performance of matching and sorting (n=255) (initialization): time 0.002254/2.243, allocations: 1.926 MB / 0.7599 GB, free: 183.7 MB / 0.5919 GB
Notification: Performance of prepare postOptimizeDAE: time 1.816e-05/2.243, allocations: 9.594 kB / 0.7599 GB, free: 183.7 MB / 0.5919 GB
Notification: Performance of postOpt simplifyComplexFunction (initialization): time 1.786e-05/2.243, allocations: 3.969 kB / 0.7599 GB, free: 183.7 MB / 0.5919 GB
Notification: Performance of postOpt tearingSystem (initialization): time 0.003573/2.247, allocations: 2.389 MB / 0.7623 GB, free: 183.4 MB / 0.5919 GB
Notification: Performance of postOpt solveSimpleEquations (initialization): time 0.0001087/2.247, allocations: 30.19 kB / 0.7623 GB, free: 183.4 MB / 0.5919 GB
Notification: Performance of postOpt calculateStrongComponentJacobians (initialization): time 0.002601/2.25, allocations: 3.063 MB / 0.7653 GB, free: 181.6 MB / 0.5919 GB
Notification: Performance of postOpt simplifyAllExpressions (initialization): time 0.0004346/2.25, allocations: 146 kB / 0.7654 GB, free: 181.5 MB / 0.5919 GB
Notification: Performance of postOpt collapseArrayExpressions (initialization): time 5.042e-05/2.25, allocations: 35.58 kB / 0.7655 GB, free: 181.5 MB / 0.5919 GB
Notification: Model statistics after passing the back-end for initialization:
 * Number of independent subsystems: 24
 * Number of states: 0 ()
 * Number of discrete variables: 18 (nTUWaterHeating.Ev.a,nTUWaterHeating.Sp.b,nTUWaterHeating.Ep.a,nTUWaterHeating.Se.b,nTUWaterHeating.Ee.a,singularPressureLoss5.C2.b,singularPressureLoss5.C1.a,singularPressureLoss4.C2.b,singularPressureLoss4.C1.a,Puit_condenseur1.C.a,singularPressureLoss3.C2.b,singularPressureLoss3.C1.a,singularPressureLoss2.C2.b,singularPressureLoss2.C1.a,sourceP.C.b,Puit_condenseur.C.a,Source_condenseur.C.b,nTUWaterHeating.Ep.b)
 * Number of discrete states: 0 ()
 * Number of clocked states: 0 ()
 * Top-level inputs: 0
Notification: Strong component statistics for initialization (34):
 * Single equations (assignments): 24
 * Array equations: 0
 * Algorithm blocks: 0
 * Record equations: 7
 * When equations: 0
 * If-equations: 0
 * Equation systems (not torn): 0
 * Torn equation systems: 3
 * 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): 3 systems
   {(1,3), (1,3), (11,21)}
Notification: Performance of prepare postOptimizeDAE: time 0.0002928/2.25, allocations: 230.5 kB / 0.7657 GB, free: 181.4 MB / 0.5919 GB
Notification: Performance of postOpt lateInlineFunction (simulation): time 0.0001071/2.251, allocations: 92.83 kB / 0.7658 GB, free: 181.3 MB / 0.5919 GB
Notification: Performance of postOpt wrapFunctionCalls (simulation): time 0.002961/2.254, allocations: 2.861 MB / 0.7686 GB, free: 179.9 MB / 0.5919 GB
Notification: Performance of postOpt simplifysemiLinear (simulation): time 9.889e-06/2.254, allocations: 5.141 kB / 0.7686 GB, free: 179.9 MB / 0.5919 GB
Notification: Performance of postOpt simplifyComplexFunction (simulation): time 6.342e-06/2.254, allocations: 0 / 0.7686 GB, free: 179.9 MB / 0.5919 GB
Notification: Performance of postOpt removeConstants (simulation): time 0.000243/2.254, allocations: 286.9 kB / 0.7688 GB, free: 179.6 MB / 0.5919 GB
Notification: Performance of postOpt simplifyTimeIndepFuncCalls (simulation): time 7.138e-05/2.254, allocations: 23.22 kB / 0.7689 GB, free: 179.6 MB / 0.5919 GB
Notification: Performance of postOpt simplifyAllExpressions (simulation): time 0.000345/2.254, allocations: 25.3 kB / 0.7689 GB, free: 179.6 MB / 0.5919 GB
Notification: Performance of postOpt findZeroCrossings (simulation): time 9.876e-05/2.254, allocations: 40 kB / 0.7689 GB, free: 179.5 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(singularPressureLoss2.T, singularPressureLoss2.rho, singularPressureLoss2.pro.u, singularPressureLoss2.pro.s, singularPressureLoss2.pro.cp, singularPressureLoss2.pro.ddhp, singularPressureLoss2.pro.ddph, singularPressureLoss2.pro.duph, singularPressureLoss2.pro.duhp, singularPressureLoss2.pro.x) = $cse13

Variables:
1: singularPressureLoss2.pro.x:VARIABLE(min = 0.0 max = 1.0 unit = "1" )  "Vapor mass fraction" type: Real
2: singularPressureLoss2.pro.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific entropy" type: Real
3: singularPressureLoss2.T:VARIABLE(min = 200.0 max = 6000.0 start = 290.0 unit = "K" nominal = 300.0 )  "Fluid temperature" type: Real
4: singularPressureLoss2.pro.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific heat capacity at constant presure" type: Real
5: singularPressureLoss2.pro.duph:VARIABLE(unit = "m3/kg" )  "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real
6: singularPressureLoss2.pro.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 )  "Specific inner energy" type: Real
7: singularPressureLoss2.pro.ddhp:VARIABLE(unit = "kg.s2/m5" )  "Derivative of density wrt. specific enthalpy at constant pressure" type: Real
8: singularPressureLoss2.pro.duhp:VARIABLE(unit = "1" )  "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real
9: singularPressureLoss2.pro.ddph:VARIABLE(unit = "s2/m2" )  "Derivative of density wrt. pressure at constant specific enthalpy" type: Real
10: $cse13.ddhp: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): nTUWaterHeating.Wcond = Source_condenseur.Q0 * nTUWaterHeating.promcF.cp * $cse5 * (nTUWaterHeating.TsatC - nTUWaterHeating.TeiF)
2/2 (10): $cse1 = ThermoSysPro.Properties.WaterSteam.IF97.Water_Ph(singularPressureLoss2.C2.P, nTUWaterHeating.HeiF, nTUWaterHeating.mode_eeF)
3/12 (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) = $cse1
4/22 (10): nTUWaterHeating.promcF = ThermoSysPro.Properties.WaterSteam.IF97.Water_Ph(0.5 * (singularPressureLoss2.C2.P + nTUWaterHeating.Se.P), 0.5 * (nTUWaterHeating.HeiF + nTUWaterHeating.HDesF), nTUWaterHeating.mode_mF)
5/32 (10): nTUWaterHeating.prompF = ThermoSysPro.Properties.WaterSteam.IF97.Water_Ph(singularPressureLoss2.C2.P, 0.5 * (singularPressureLoss2.h + nTUWaterHeating.HeiF), nTUWaterHeating.mode_eeF)
6/42 (1): $cse3 = min(singularPressureLoss5.Q * nTUWaterHeating.prompC.cp, Source_condenseur.Q0 * nTUWaterHeating.prompF.cp)
7/43 (1): nTUWaterHeating.Wpurge = $cse3 * $cse4 * (nTUWaterHeating.prosp.T - nTUWaterHeating.proeeF.T)
8/44 (1): $cse4 = ThermoSysPro.Correlations.Thermal.WBHeatExchangerEfficiency(singularPressureLoss5.Q, Source_condenseur.Q0, nTUWaterHeating.prompC.cp, nTUWaterHeating.prompF.cp, nTUWaterHeating.KPurge, 656.0, 0.0)
9/45 (10): nTUWaterHeating.prompC = ThermoSysPro.Properties.WaterSteam.IF97.Water_Ph(nTUWaterHeating.P, 0.5 * (nTUWaterHeating.Hep + singularPressureLoss5.h), nTUWaterHeating.mode_spC)
10/55 (1): 0.0 = if singularPressureLoss5.Q > 0.0 then singularPressureLoss5.h - nTUWaterHeating.h else singularPressureLoss5.h - Puit_condenseur1.h0
11/56 (1): 0.0 = if singularPressureLoss3.Q > 0.0 then singularPressureLoss3.h - sourceP.h0 else singularPressureLoss3.h - nTUWaterHeating.h
12/57 (10): $cse11 = ThermoSysPro.Properties.Fluid.Ph(singularPressureLoss3.Pm, singularPressureLoss3.h, singularPressureLoss3.mode, singularPressureLoss3.fluid)
13/67 (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) = $cse11
14/77 (1): singularPressureLoss3.Pm = 0.5 * (sourceP.P0 + nTUWaterHeating.P)
15/78 (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.WaterSteam.IF97.Water_sat_P(nTUWaterHeating.P)
16/92 (1): nTUWaterHeating.Wcond = if noEvent(singularPressureLoss3.h < nTUWaterHeating.HsatvC) then singularPressureLoss3.Q * (singularPressureLoss3.h - nTUWaterHeating.HsateC) + nTUWaterHeating.Wflash else singularPressureLoss3.Q * (nTUWaterHeating.HsatvC - nTUWaterHeating.HsateC) + nTUWaterHeating.Wflash
17/93 (1): nTUWaterHeating.Wcond = Source_condenseur.Q0 * (nTUWaterHeating.HDesF - nTUWaterHeating.HeiF)
18/94 (10): $cse2 = ThermoSysPro.Properties.WaterSteam.IF97.Water_Ph(0.5 * (singularPressureLoss2.C2.P + nTUWaterHeating.Se.P), 0.5 * (singularPressureLoss2.h + nTUWaterHeating.HDesF), nTUWaterHeating.mode_eeF)
19/104 (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) = $cse2
20/114 (1): singularPressureLoss2.C2.P - nTUWaterHeating.Se.P = nTUWaterHeating.lambdaE * $cse6 / nTUWaterHeating.rho
21/115 (1): 0.0 = if Source_condenseur.Q0 > 0.0 then nTUWaterHeating.HDesF - nTUWaterHeating.Se.h_vol else nTUWaterHeating.HDesF - Puit_condenseur.h0
22/116 (1): 0.0 = if noEvent(Source_condenseur.Q0 > 0.0) then singularPressureLoss2.h - singularPressureLoss2.C2.h_vol else nTUWaterHeating.HDesF - nTUWaterHeating.Se.h_vol
23/117 (10): nTUWaterHeating.proeeF = ThermoSysPro.Properties.WaterSteam.IF97.Water_Ph(singularPressureLoss2.C2.P, singularPressureLoss2.h, nTUWaterHeating.mode_eeF)
24/127 (10): $cse13 = ThermoSysPro.Properties.Fluid.Ph(singularPressureLoss2.Pm, singularPressureLoss2.h, singularPressureLoss2.mode, singularPressureLoss2.fluid)
25/137 (10): ThermoSysPro.Properties.WaterSteam.Common.ThermoProperties_ph(singularPressureLoss2.T, singularPressureLoss2.rho, singularPressureLoss2.pro.u, singularPressureLoss2.pro.s, singularPressureLoss2.pro.cp, singularPressureLoss2.pro.ddhp, singularPressureLoss2.pro.ddph, singularPressureLoss2.pro.duph, singularPressureLoss2.pro.duhp, singularPressureLoss2.pro.x) = $cse13
26/147 (1): singularPressureLoss2.Pm = 0.5 * (Source_condenseur.P0 + singularPressureLoss2.C2.P)
27/148 (1): Source_condenseur.P0 - singularPressureLoss2.C2.P = singularPressureLoss2.deltaP
28/149 (1): singularPressureLoss2.deltaP = singularPressureLoss2.K * $cse14 / singularPressureLoss2.rho
29/150 (1): 0.0 = if Source_condenseur.Q0 > 0.0 then singularPressureLoss2.h - Source_condenseur.h0 else singularPressureLoss2.h - singularPressureLoss2.C2.h_vol
30/151 (1): nTUWaterHeating.Wpurge = Source_condenseur.Q0 * (nTUWaterHeating.HeiF - singularPressureLoss2.h)
31/152 (1): nTUWaterHeating.Wpurge = singularPressureLoss5.Q * (nTUWaterHeating.Hep - singularPressureLoss5.h)
32/153 (1): singularPressureLoss5.Q = 1e-6 + singularPressureLoss3.Q
33/154 (1): $cse5 = ThermoSysPro.Correlations.Thermal.WBHeatExchangerEfficiency(singularPressureLoss3.Q, Source_condenseur.Q0, 1e20, nTUWaterHeating.promcF.cp, nTUWaterHeating.KCond, nTUWaterHeating.SCondDes - 1e-9, 0.5)
34/155 (1): $cse12 = ThermoSysPro.Functions.ThermoSquare(singularPressureLoss3.Q, singularPressureLoss3.eps)
35/156 (1): singularPressureLoss3.deltaP = singularPressureLoss3.K * $cse12 / singularPressureLoss3.rho
36/157 (1): 0.0 = if nTUWaterHeating.flashepC.x > 0.0 then nTUWaterHeating.Hep - nTUWaterHeating.HsateC else singularPressureLoss5.Q * nTUWaterHeating.Hep - (nTUWaterHeating.HsateC * singularPressureLoss3.Q + 0.09999999999999999)
37/158 (10): nTUWaterHeating.prosp = ThermoSysPro.Properties.WaterSteam.IF97.Water_Ph(nTUWaterHeating.P, nTUWaterHeating.Hep, nTUWaterHeating.mode_spC)
38/168 (1): nTUWaterHeating.Wflash = if nTUWaterHeating.flashepC.x > 0.0 then 1e-6 * (1e5 - nTUWaterHeating.HsateC) else 0.0
39/169 (10): nTUWaterHeating.flashepC = ThermoSysPro.Properties.WaterSteam.IF97.Water_Ph(nTUWaterHeating.P, 1e5, nTUWaterHeating.mode_flash)
40/179 (1): sourceP.P0 - nTUWaterHeating.P = singularPressureLoss3.deltaP

Variables:
1: singularPressureLoss3.deltaP:VARIABLE(unit = "Pa" )  "Singular pressure loss" type: Real
2: nTUWaterHeating.flashepC.T:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 320.0 )  "Temperature" type: Real
3: nTUWaterHeating.flashepC.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 )  "Specific inner energy" type: Real
4: nTUWaterHeating.flashepC.ddph:VARIABLE(unit = "s2/m2" )  "Derivative of density wrt. pressure at constant specific enthalpy" type: Real
5: nTUWaterHeating.flashepC.x:VARIABLE(min = 0.0 max = 1.0 unit = "1" )  "Vapor mass fraction" type: Real
6: nTUWaterHeating.flashepC.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 )  "Density" type: Real
7: nTUWaterHeating.flashepC.duph:VARIABLE(unit = "m3/kg" )  "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real
8: nTUWaterHeating.flashepC.ddhp:VARIABLE(unit = "kg.s2/m5" )  "Derivative of density wrt. specific enthalpy at constant pressure" type: Real
9: nTUWaterHeating.flashepC.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific heat capacity at constant presure" type: Real
10: nTUWaterHeating.flashepC.duhp:VARIABLE(unit = "1" )  "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real
11: nTUWaterHeating.flashepC.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific entropy" type: Real
12: nTUWaterHeating.Wflash:VARIABLE(start = 1.0 unit = "W" )  "Energy transfer during partial vaporisation in the drain" type: Real
13: nTUWaterHeating.prosp.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 )  "Density" type: Real
14: nTUWaterHeating.prosp.x:VARIABLE(min = 0.0 max = 1.0 unit = "1" )  "Vapor mass fraction" type: Real
15: nTUWaterHeating.prosp.ddhp:VARIABLE(unit = "kg.s2/m5" )  "Derivative of density wrt. specific enthalpy at constant pressure" type: Real
16: nTUWaterHeating.prosp.T:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 320.0 )  "Temperature" type: Real
17: nTUWaterHeating.prosp.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific entropy" type: Real
18: nTUWaterHeating.prosp.duhp:VARIABLE(unit = "1" )  "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real
19: nTUWaterHeating.prosp.duph:VARIABLE(unit = "m3/kg" )  "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real
20: nTUWaterHeating.prosp.ddph:VARIABLE(unit = "s2/m2" )  "Derivative of density wrt. pressure at constant specific enthalpy" type: Real
21: nTUWaterHeating.prosp.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific heat capacity at constant presure" type: Real
22: nTUWaterHeating.prosp.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 )  "Specific inner energy" type: Real
23: nTUWaterHeating.Hep:VARIABLE(start = 5e5 unit = "J/kg" )  "Mixing specific enthalpy of the drain and the condensate" type: Real
24: singularPressureLoss3.rho:VARIABLE(min = 1e-9 max = 1e5 start = 998.0 unit = "kg/m3" nominal = 998.0 )  "Fluid density" type: Real
25: $cse12:VARIABLE(protected = true )  type: Real unreplaceable
26: $cse5:VARIABLE(protected = true )  type: Real unreplaceable
27: singularPressureLoss3.Q:VARIABLE(start = 100.0 unit = "kg/s" )  "Mass flow rate" type: Real
28: singularPressureLoss5.Q:VARIABLE(start = 100.0 unit = "kg/s" )  "Mass flow rate" type: Real
29: nTUWaterHeating.Wpurge:VARIABLE(start = 1.0 unit = "W" )  "Energy transfer during drain cooling" type: Real
30: singularPressureLoss2.C2.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" )  "Fluid specific enthalpy in the control volume" type: Real
31: singularPressureLoss2.rho:VARIABLE(min = 1e-9 max = 1e5 start = 998.0 unit = "kg/m3" nominal = 998.0 )  "Fluid density" type: Real
32: singularPressureLoss2.deltaP:VARIABLE(unit = "Pa" )  "Singular pressure loss" type: Real
33: singularPressureLoss2.C2.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 )  "Fluid pressure in the control volume" type: Real
34: singularPressureLoss2.pro.x:VARIABLE(min = 0.0 max = 1.0 unit = "1" )  "Vapor mass fraction" type: Real
35: singularPressureLoss2.pro.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific entropy" type: Real
36: singularPressureLoss2.T:VARIABLE(min = 200.0 max = 6000.0 start = 290.0 unit = "K" nominal = 300.0 )  "Fluid temperature" type: Real
37: singularPressureLoss2.pro.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific heat capacity at constant presure" type: Real
38: singularPressureLoss2.pro.duph:VARIABLE(unit = "m3/kg" )  "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real
39: singularPressureLoss2.pro.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 )  "Specific inner energy" type: Real
40: singularPressureLoss2.pro.ddhp:VARIABLE(unit = "kg.s2/m5" )  "Derivative of density wrt. specific enthalpy at constant pressure" type: Real
41: singularPressureLoss2.pro.duhp:VARIABLE(unit = "1" )  "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real
42: singularPressureLoss2.pro.ddph:VARIABLE(unit = "s2/m2" )  "Derivative of density wrt. pressure at constant specific enthalpy" type: Real
43: $cse13.ddhp:VARIABLE(protected = true )  type: Real unreplaceable
44: $cse13.cp:VARIABLE(protected = true )  type: Real unreplaceable
45: $cse13.duph:VARIABLE(protected = true )  type: Real unreplaceable
46: $cse13.duhp:VARIABLE(protected = true )  type: Real unreplaceable
47: singularPressureLoss2.Pm:VARIABLE(min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 )  "Average fluid pressure" type: Real
48: $cse13.u:VARIABLE(protected = true )  type: Real unreplaceable
49: $cse13.s:VARIABLE(protected = true )  type: Real unreplaceable
50: $cse13.d:VARIABLE(protected = true )  type: Real unreplaceable
51: $cse13.x:VARIABLE(protected = true )  type: Real unreplaceable
52: $cse13.T:VARIABLE(protected = true )  type: Real unreplaceable
53: $cse13.ddph:VARIABLE(protected = true )  type: Real unreplaceable
54: nTUWaterHeating.proeeF.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific entropy" type: Real
55: nTUWaterHeating.proeeF.ddhp:VARIABLE(unit = "kg.s2/m5" )  "Derivative of density wrt. specific enthalpy at constant pressure" type: Real
56: nTUWaterHeating.proeeF.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific heat capacity at constant presure" type: Real
57: nTUWaterHeating.proeeF.duhp:VARIABLE(unit = "1" )  "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real
58: nTUWaterHeating.proeeF.duph:VARIABLE(unit = "m3/kg" )  "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real
59: nTUWaterHeating.proeeF.T:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 320.0 )  "Temperature" type: Real
60: nTUWaterHeating.proeeF.x:VARIABLE(min = 0.0 max = 1.0 unit = "1" )  "Vapor mass fraction" type: Real
61: nTUWaterHeating.proeeF.ddph:VARIABLE(unit = "s2/m2" )  "Derivative of density wrt. pressure at constant specific enthalpy" type: Real
62: nTUWaterHeating.proeeF.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 )  "Density" type: Real
63: nTUWaterHeating.proeeF.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 )  "Specific inner energy" type: Real
64: singularPressureLoss2.h:VARIABLE(start = 1e5 unit = "J/kg" )  "Fluid specific enthalpy" type: Real
65: nTUWaterHeating.Se.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" )  "Fluid specific enthalpy in the control volume" type: Real
66: nTUWaterHeating.rho:VARIABLE(min = 1e-9 max = 1e5 start = 1000.0 unit = "kg/m3" nominal = 998.0 )  "Average water density" type: Real
67: nTUWaterHeating.promeF.duhp:VARIABLE(unit = "1" )  "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real
68: $cse2.x:VARIABLE(protected = true )  type: Real unreplaceable
69: nTUWaterHeating.promeF.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific heat capacity at constant presure" type: Real
70: nTUWaterHeating.promeF.x:VARIABLE(min = 0.0 max = 1.0 unit = "1" )  "Vapor mass fraction" type: Real
71: nTUWaterHeating.promeF.ddhp:VARIABLE(unit = "kg.s2/m5" )  "Derivative of density wrt. specific enthalpy at constant pressure" type: Real
72: nTUWaterHeating.promeF.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 )  "Specific inner energy" type: Real
73: nTUWaterHeating.promeF.T:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 320.0 )  "Temperature" type: Real
74: nTUWaterHeating.promeF.ddph:VARIABLE(unit = "s2/m2" )  "Derivative of density wrt. pressure at constant specific enthalpy" type: Real
75: nTUWaterHeating.promeF.duph:VARIABLE(unit = "m3/kg" )  "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real
76: nTUWaterHeating.promeF.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific entropy" type: Real
77: $cse2.cp:VARIABLE(protected = true )  type: Real unreplaceable
78: $cse2.s:VARIABLE(protected = true )  type: Real unreplaceable
79: $cse2.ddph:VARIABLE(protected = true )  type: Real unreplaceable
80: $cse2.ddhp:VARIABLE(protected = true )  type: Real unreplaceable
81: $cse2.d:VARIABLE(protected = true )  type: Real unreplaceable
82: nTUWaterHeating.Se.P:VARIABLE(flow=false min = 0.0 start = 8e6 unit = "Pa" nominal = 1e5 )  "Fluid pressure in the control volume" type: Real
83: $cse2.T:VARIABLE(protected = true )  type: Real unreplaceable
84: $cse2.duhp:VARIABLE(protected = true )  type: Real unreplaceable
85: $cse2.u:VARIABLE(protected = true )  type: Real unreplaceable
86: $cse2.duph:VARIABLE(protected = true )  type: Real unreplaceable
87: nTUWaterHeating.HDesF:VARIABLE(start = 9e5 unit = "J/kg" )  "Fluid specific enthalpy after deheating" type: Real
88: nTUWaterHeating.Wcond:VARIABLE(start = 1.0 unit = "W" )  "Energy transfer during condensation" type: Real
89: nTUWaterHeating.lsatC.cp:VARIABLE(unit = "J/(kg.K)" )  "Specific heat capacity at constant pressure" type: Real
90: nTUWaterHeating.vsatC.P:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 )  "Pressure" type: Real
91: nTUWaterHeating.vsatC.cp:VARIABLE(unit = "J/(kg.K)" )  "Specific heat capacity at constant pressure" type: Real
92: nTUWaterHeating.lsatC.cv:VARIABLE(unit = "J/(kg.K)" )  "Specific heat capacity at constant volume" type: Real
93: nTUWaterHeating.vsatC.T:VARIABLE(min = 0.0 start = 288.15 unit = "K" nominal = 300.0 )  "Temperature" type: Real
94: nTUWaterHeating.lsatC.P:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 )  "Pressure" type: Real
95: 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
96: 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
97: nTUWaterHeating.vsatC.rho:VARIABLE(min = 0.0 unit = "kg/m3" )  "Density" type: Real
98: nTUWaterHeating.lsatC.rho:VARIABLE(min = 0.0 unit = "kg/m3" )  "Density" type: Real
99: nTUWaterHeating.vsatC.pt:VARIABLE()  "Derivative of pressure wrt. temperature" type: Real
100: nTUWaterHeating.vsatC.cv:VARIABLE(unit = "J/(kg.K)" )  "Specific heat capacity at constant volume" type: Real
101: nTUWaterHeating.TsatC:VARIABLE(min = 0.0 start = 400.0 unit = "K" nominal = 300.0 )  "Saturation temperature" type: Real
102: nTUWaterHeating.lsatC.pt:VARIABLE()  "Derivative of pressure wrt. temperature" type: Real
103: nTUWaterHeating.P:VARIABLE(min = 0.0 start = 1e6 unit = "Pa" nominal = 1e5 )  "Fluid pressure" type: Real
104: $cse11.x:VARIABLE(protected = true )  type: Real unreplaceable
105: singularPressureLoss3.pro.duph:VARIABLE(unit = "m3/kg" )  "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real
106: singularPressureLoss3.T:VARIABLE(min = 200.0 max = 6000.0 start = 290.0 unit = "K" nominal = 300.0 )  "Fluid temperature" type: Real
107: singularPressureLoss3.pro.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific entropy" type: Real
108: singularPressureLoss3.pro.x:VARIABLE(min = 0.0 max = 1.0 unit = "1" )  "Vapor mass fraction" type: Real
109: singularPressureLoss3.pro.ddph:VARIABLE(unit = "s2/m2" )  "Derivative of density wrt. pressure at constant specific enthalpy" type: Real
110: singularPressureLoss3.pro.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific heat capacity at constant presure" type: Real
111: singularPressureLoss3.pro.ddhp:VARIABLE(unit = "kg.s2/m5" )  "Derivative of density wrt. specific enthalpy at constant pressure" type: Real
112: singularPressureLoss3.pro.duhp:VARIABLE(unit = "1" )  "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real
113: singularPressureLoss3.pro.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 )  "Specific inner energy" type: Real
114: $cse11.duph:VARIABLE(protected = true )  type: Real unreplaceable
115: $cse11.ddph:VARIABLE(protected = true )  type: Real unreplaceable
116: $cse11.u:VARIABLE(protected = true )  type: Real unreplaceable
117: $cse11.duhp:VARIABLE(protected = true )  type: Real unreplaceable
118: $cse11.ddhp:VARIABLE(protected = true )  type: Real unreplaceable
119: $cse11.d:VARIABLE(protected = true )  type: Real unreplaceable
120: singularPressureLoss3.Pm:VARIABLE(min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 )  "Average fluid pressure" type: Real
121: $cse11.cp:VARIABLE(protected = true )  type: Real unreplaceable
122: $cse11.s:VARIABLE(protected = true )  type: Real unreplaceable
123: $cse11.T:VARIABLE(protected = true )  type: Real unreplaceable
124: singularPressureLoss3.h:VARIABLE(start = 1e5 unit = "J/kg" )  "Fluid specific enthalpy" type: Real
125: nTUWaterHeating.h:VARIABLE(start = 1e6 unit = "J/kg" )  "Fluid specific enthalpy" type: Real
126: nTUWaterHeating.prompC.T:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 320.0 )  "Temperature" type: Real
127: nTUWaterHeating.prompC.duph:VARIABLE(unit = "m3/kg" )  "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real
128: nTUWaterHeating.prompC.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 )  "Specific inner energy" type: Real
129: nTUWaterHeating.prompC.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific entropy" type: Real
130: nTUWaterHeating.prompC.ddhp:VARIABLE(unit = "kg.s2/m5" )  "Derivative of density wrt. specific enthalpy at constant pressure" type: Real
131: nTUWaterHeating.prompC.x:VARIABLE(min = 0.0 max = 1.0 unit = "1" )  "Vapor mass fraction" type: Real
132: nTUWaterHeating.prompC.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 )  "Density" type: Real
133: singularPressureLoss5.h:VARIABLE(start = 1e5 unit = "J/kg" )  "Fluid specific enthalpy" type: Real
134: nTUWaterHeating.prompC.ddph:VARIABLE(unit = "s2/m2" )  "Derivative of density wrt. pressure at constant specific enthalpy" type: Real
135: nTUWaterHeating.prompC.duhp:VARIABLE(unit = "1" )  "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real
136: nTUWaterHeating.prompC.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific heat capacity at constant presure" type: Real
137: $cse4:VARIABLE(protected = true )  type: Real unreplaceable
138: $cse3:VARIABLE(protected = true )  type: Real unreplaceable
139: nTUWaterHeating.prompF.ddph:VARIABLE(unit = "s2/m2" )  "Derivative of density wrt. pressure at constant specific enthalpy" type: Real
140: nTUWaterHeating.prompF.duph:VARIABLE(unit = "m3/kg" )  "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real
141: nTUWaterHeating.prompF.duhp:VARIABLE(unit = "1" )  "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real
142: nTUWaterHeating.prompF.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific entropy" type: Real
143: nTUWaterHeating.prompF.T:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 320.0 )  "Temperature" type: Real
144: nTUWaterHeating.prompF.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 )  "Density" type: Real
145: nTUWaterHeating.prompF.ddhp:VARIABLE(unit = "kg.s2/m5" )  "Derivative of density wrt. specific enthalpy at constant pressure" type: Real
146: nTUWaterHeating.prompF.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 )  "Specific inner energy" type: Real
147: nTUWaterHeating.prompF.x:VARIABLE(min = 0.0 max = 1.0 unit = "1" )  "Vapor mass fraction" type: Real
148: nTUWaterHeating.prompF.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific heat capacity at constant presure" type: Real
149: nTUWaterHeating.promcF.x:VARIABLE(min = 0.0 max = 1.0 unit = "1" )  "Vapor mass fraction" type: Real
150: nTUWaterHeating.promcF.duph:VARIABLE(unit = "m3/kg" )  "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real
151: nTUWaterHeating.promcF.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 )  "Specific inner energy" type: Real
152: nTUWaterHeating.proecF.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 )  "Specific inner energy" type: Real
153: nTUWaterHeating.proecF.ddph:VARIABLE(unit = "s2/m2" )  "Derivative of density wrt. pressure at constant specific enthalpy" type: Real
154: nTUWaterHeating.proecF.duph:VARIABLE(unit = "m3/kg" )  "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real
155: nTUWaterHeating.proecF.duhp:VARIABLE(unit = "1" )  "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real
156: nTUWaterHeating.proecF.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific heat capacity at constant presure" type: Real
157: nTUWaterHeating.proecF.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific entropy" type: Real
158: nTUWaterHeating.proecF.x:VARIABLE(min = 0.0 max = 1.0 unit = "1" )  "Vapor mass fraction" type: Real
159: $cse1.ddph:VARIABLE(protected = true )  type: Real unreplaceable
160: $cse1.x:VARIABLE(protected = true )  type: Real unreplaceable
161: $cse1.s:VARIABLE(protected = true )  type: Real unreplaceable
162: $cse1.duph:VARIABLE(protected = true )  type: Real unreplaceable
163: $cse1.d:VARIABLE(protected = true )  type: Real unreplaceable
164: $cse1.T:VARIABLE(protected = true )  type: Real unreplaceable
165: $cse1.ddhp:VARIABLE(protected = true )  type: Real unreplaceable
166: $cse1.u:VARIABLE(protected = true )  type: Real unreplaceable
167: $cse1.cp:VARIABLE(protected = true )  type: Real unreplaceable
168: $cse1.duhp:VARIABLE(protected = true )  type: Real unreplaceable
169: nTUWaterHeating.HeiF:VARIABLE(start = 9e5 unit = "J/kg" )  "Fluid specific enthalpy after drain cooling" type: Real
170: nTUWaterHeating.promcF.T:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 320.0 )  "Temperature" type: Real
171: nTUWaterHeating.promcF.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific entropy" type: Real
172: nTUWaterHeating.promcF.ddph:VARIABLE(unit = "s2/m2" )  "Derivative of density wrt. pressure at constant specific enthalpy" type: Real
173: nTUWaterHeating.promcF.duhp:VARIABLE(unit = "1" )  "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real
174: nTUWaterHeating.promcF.ddhp:VARIABLE(unit = "kg.s2/m5" )  "Derivative of density wrt. specific enthalpy at constant pressure" type: Real
175: nTUWaterHeating.promcF.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 )  "Density" type: Real
176: nTUWaterHeating.promcF.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific heat capacity at constant presure" type: Real
177: nTUWaterHeating.TeiF:VARIABLE(min = 200.0 max = 6000.0 start = 400.0 unit = "K" nominal = 300.0 )  "Fluid temperature after drain cooling" type: Real
178: nTUWaterHeating.proecF.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 )  "Density" type: Real
179: nTUWaterHeating.proecF.ddhp:VARIABLE(unit = "kg.s2/m5" )  "Derivative of density wrt. specific enthalpy at constant pressure" 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 0.00359/2.258, allocations: 10.01 MB / 0.7787 GB, free: 168.1 MB / 0.5919 GB
Error: post-optimization module createDAEmodeBDAE (simulation) failed.
Error: Internal error SimCode DAEmode: The model ThermoSysPro.Examples.SimpleExamples.TestNTUWaterHeating0 could not be translated