Running: ./testmodel.py --libraries=/home/hudson/saved_omc/libraries/.openmodelica/libraries --ompython_omhome=/usr ThermoSysPro_ThermoSysPro.Examples.SimpleExamples.TestStaticWaterWaterExchanger.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.TestStaticWaterWaterExchanger,tolerance=1e-06,outputFormat="empty",numberOfIntervals=5000,variableFilter="",fileNamePrefix="ThermoSysPro_ThermoSysPro.Examples.SimpleExamples.TestStaticWaterWaterExchanger")
translateModel(ThermoSysPro.Examples.SimpleExamples.TestStaticWaterWaterExchanger,tolerance=1e-06,outputFormat="empty",numberOfIntervals=5000,variableFilter="",fileNamePrefix="ThermoSysPro_ThermoSysPro.Examples.SimpleExamples.TestStaticWaterWaterExchanger")
Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermoSysPro 4.0.0-master/package.mo): time 0.834/0.834, allocations: 150.9 MB / 167.2 MB, free: 14.49 MB / 142.1 MB
Notification: Performance of FrontEnd - loaded program: time 0.0003506/0.0003506, allocations: 23.64 kB / 237.8 MB, free: 1.785 MB / 190.1 MB
Notification: Performance of FrontEnd - Absyn->SCode: time 0.05326/0.05363, allocations: 31.34 MB / 269.1 MB, free: 7.035 MB / 222.1 MB
Notification: Automatically loaded package Complex 4.0.0 due to uses annotation from Modelica.
Notification: Automatically loaded package ModelicaServices 4.0.0 due to uses annotation from Modelica.
Notification: Automatically loaded package Modelica 4.0.0 due to usage.
Notification: Performance of NFInst.instantiate(ThermoSysPro.Examples.SimpleExamples.TestStaticWaterWaterExchanger): time 1.639/1.693, allocations: 296.3 MB / 0.5522 GB, free: 11.66 MB / 446.1 MB
Notification: Performance of NFInst.instExpressions: time 0.02663/1.719, allocations: 22.97 MB / 0.5746 GB, free: 4.605 MB / 462.1 MB
Notification: Performance of NFInst.updateImplicitVariability: time 0.0003337/1.72, allocations: 4 kB / 0.5746 GB, free: 4.602 MB / 462.1 MB
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermoSysPro 4.0.0-master/WaterSteam/HeatExchangers/StaticWaterWaterExchanger.mo:81:3-83:42:writable] Warning: Connector Ec 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/StaticWaterWaterExchanger.mo:84:3-86:38:writable] Warning: Connector Ef 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/StaticWaterWaterExchanger.mo:87:3-89:37:writable] Warning: Connector Sf 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/StaticWaterWaterExchanger.mo:90:3-92:37:writable] Warning: Connector Sc 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/BoundaryConditions/SinkP.mo:33:3-34:47:writable] Warning: Connector C is not balanced: The number of potential variables (4) is not equal to the number of flow variables (0).
Notification: Performance of NFTyping.typeComponents: time 0.0004742/1.72, allocations: 180.9 kB / 0.5748 GB, free: 4.426 MB / 462.1 MB
Notification: Performance of NFTyping.typeBindings: time 0.0004637/1.721, allocations: 257.9 kB / 0.575 GB, free: 4.172 MB / 462.1 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.
Notification: Performance of NFTyping.typeClassSections: time 0.01746/1.738, allocations: 7.231 MB / 0.5821 GB, free: 12.93 MB / 478.1 MB
Notification: Performance of NFFlatten.flatten: time 0.001216/1.739, allocations: 0.9803 MB / 0.583 GB, free: 11.95 MB / 478.1 MB
Notification: Performance of NFFlatten.resolveConnections: time 0.0003668/1.74, allocations: 280.8 kB / 0.5833 GB, free: 11.67 MB / 478.1 MB
Notification: Performance of NFEvalConstants.evaluate: time 0.000428/1.74, allocations: 386.6 kB / 0.5837 GB, free: 11.29 MB / 478.1 MB
Notification: Performance of NFSimplifyModel.simplify: time 0.0003576/1.741, allocations: 326.5 kB / 0.584 GB, free: 10.97 MB / 478.1 MB
Notification: Performance of NFPackage.collectConstants: time 6.707e-05/1.741, allocations: 48 kB / 0.584 GB, free: 10.93 MB / 478.1 MB
Notification: Performance of NFFlatten.collectFunctions: time 0.0237/1.764, allocations: 15.38 MB / 0.599 GB, free: 11.53 MB / 494.1 MB
Notification: Performance of NFScalarize.scalarize: time 0.0001855/1.765, allocations: 131.5 kB / 0.5992 GB, free: 11.4 MB / 494.1 MB
Notification: Performance of NFVerifyModel.verify: time 0.0004454/1.765, allocations: 366.2 kB / 0.5995 GB, free: 11.04 MB / 494.1 MB
Notification: Performance of NFConvertDAE.convert: time 0.01247/1.778, allocations: 6.923 MB / 0.6063 GB, free: 4.105 MB / 494.1 MB
Notification: Performance of FrontEnd - DAE generated: time 3.346e-06/1.778, allocations: 0 / 0.6063 GB, free: 4.105 MB / 494.1 MB
Notification: Performance of FrontEnd: time 2.595e-06/1.778, allocations: 0 / 0.6063 GB, free: 4.105 MB / 494.1 MB
Notification: Performance of Transformations before backend: time 9.107e-06/1.778, allocations: 3.938 kB / 0.6063 GB, free: 4.102 MB / 494.1 MB
Notification: Model statistics after passing the front-end and creating the data structures used by the back-end:
 * Number of equations: 210
 * Number of variables: 210
Notification: Performance of Generate backend data structure: time 0.004088/1.782, allocations: 1.536 MB / 0.6078 GB, free: 2.512 MB / 494.1 MB
Notification: Performance of prepare preOptimizeDAE: time 3.959e-05/1.782, allocations: 8.031 kB / 0.6078 GB, free: 2.504 MB / 494.1 MB
Notification: Performance of preOpt normalInlineFunction (simulation): time 0.0001176/1.782, allocations: 72 kB / 0.6079 GB, free: 2.434 MB / 494.1 MB
Notification: Performance of preOpt evaluateParameters (simulation): time 0.0003775/1.782, allocations: 350.6 kB / 0.6082 GB, free: 2.051 MB / 494.1 MB
Notification: Performance of preOpt simplifyIfEquations (simulation): time 0.0001955/1.782, allocations: 126.1 kB / 0.6083 GB, free: 1.91 MB / 494.1 MB
Notification: Performance of preOpt expandDerOperator (simulation): time 6.386e-05/1.783, allocations: 48 kB / 0.6084 GB, free: 1.863 MB / 494.1 MB
Notification: Performance of preOpt clockPartitioning (simulation): time 0.001167/1.784, allocations: 0.7835 MB / 0.6091 GB, free: 1.035 MB / 494.1 MB
Notification: Performance of preOpt findStateOrder (simulation): time 1.509e-05/1.784, allocations: 0 / 0.6091 GB, free: 1.035 MB / 494.1 MB
Notification: Performance of preOpt replaceEdgeChange (simulation): time 4.554e-05/1.784, allocations: 24 kB / 0.6092 GB, free: 1.012 MB / 494.1 MB
Notification: Performance of preOpt inlineArrayEqn (simulation): time 3.178e-05/1.784, allocations: 35.97 kB / 0.6092 GB, free: 0.9766 MB / 494.1 MB
Notification: Performance of preOpt removeEqualRHS (simulation): time 0.001077/1.785, allocations: 0.5786 MB / 0.6098 GB, free: 404 kB / 494.1 MB
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 0.07406/1.859, allocations: 36.64 MB / 0.6455 GB, free: 8.004 MB / 0.5294 GB
Notification: Performance of preOpt comSubExp (simulation): time 0.001333/1.86, allocations: 0.5425 MB / 0.6461 GB, free: 7.453 MB / 0.5294 GB
Notification: Performance of preOpt resolveLoops (simulation): time 0.0006004/1.861, allocations: 350.8 kB / 0.6464 GB, free: 7.109 MB / 0.5294 GB
Notification: Performance of preOpt evalFunc (simulation): time 0.0734/1.934, allocations: 33.81 MB / 0.6794 GB, free: 2.012 MB / 0.5606 GB
Notification: Performance of preOpt encapsulateWhenConditions (simulation): time 3.791e-05/1.934, allocations: 38.5 kB / 0.6795 GB, free: 1.965 MB / 0.5606 GB
Notification: Performance of pre-optimization done (n=126): time 4.579e-06/1.934, allocations: 3.984 kB / 0.6795 GB, free: 1.961 MB / 0.5606 GB
Notification: Performance of matching and sorting (n=126): time 0.01802/1.952, allocations: 3.3 MB / 0.6827 GB, free: 14.63 MB / 0.5762 GB
Notification: Performance of inlineWhenForInitialization (initialization): time 3.404e-05/1.953, allocations: 55.41 kB / 0.6827 GB, free: 14.56 MB / 0.5762 GB
Notification: Performance of selectInitializationVariablesDAE (initialization): time 0.0004422/1.953, allocations: 336.4 kB / 0.6831 GB, free: 14.22 MB / 0.5762 GB
Notification: Performance of collectPreVariables (initialization): time 3.713e-05/1.953, allocations: 29.7 kB / 0.6831 GB, free: 14.19 MB / 0.5762 GB
Notification: Performance of collectInitialEqns (initialization): time 0.0001818/1.953, allocations: 233.3 kB / 0.6833 GB, free: 13.95 MB / 0.5762 GB
Notification: Performance of collectInitialBindings (initialization): time 0.0002896/1.954, allocations: 405.7 kB / 0.6837 GB, free: 13.55 MB / 0.5762 GB
Notification: Performance of simplifyInitialFunctions (initialization): time 0.0002026/1.954, allocations: 134.1 kB / 0.6838 GB, free: 13.41 MB / 0.5762 GB
Notification: Performance of setup shared object (initialization): time 0.0001707/1.954, allocations: 366.8 kB / 0.6842 GB, free: 13.05 MB / 0.5762 GB
Notification: Performance of preBalanceInitialSystem (initialization): time 0.0006184/1.955, allocations: 281.6 kB / 0.6844 GB, free: 12.77 MB / 0.5762 GB
Notification: Performance of partitionIndependentBlocks (initialization): time 0.0006733/1.955, allocations: 389.1 kB / 0.6848 GB, free: 12.36 MB / 0.5762 GB
Notification: Performance of analyzeInitialSystem (initialization): time 0.001332/1.957, allocations: 0.7225 MB / 0.6855 GB, free: 11.61 MB / 0.5762 GB
Notification: Performance of solveInitialSystemEqSystem (initialization): time 5.67e-06/1.957, allocations: 0 / 0.6855 GB, free: 11.61 MB / 0.5762 GB
Notification: Performance of matching and sorting (n=142) (initialization): time 0.004458/1.961, allocations: 1.283 MB / 0.6868 GB, free: 10.32 MB / 0.5762 GB
Notification: Performance of prepare postOptimizeDAE: time 2.741e-05/1.961, allocations: 4 kB / 0.6868 GB, free: 10.32 MB / 0.5762 GB
Notification: Performance of postOpt simplifyComplexFunction (initialization): time 1.506e-05/1.961, allocations: 11.94 kB / 0.6868 GB, free: 10.3 MB / 0.5762 GB
Notification: Performance of postOpt tearingSystem (initialization): time 0.00389/1.965, allocations: 1.383 MB / 0.6881 GB, free: 8.918 MB / 0.5762 GB
Notification: Performance of postOpt solveSimpleEquations (initialization): time 0.0001157/1.965, allocations: 15.94 kB / 0.6881 GB, free: 8.902 MB / 0.5762 GB
Notification: Performance of postOpt calculateStrongComponentJacobians (initialization): time 0.002311/1.967, allocations: 1.386 MB / 0.6895 GB, free: 7.492 MB / 0.5762 GB
Notification: Performance of postOpt simplifyAllExpressions (initialization): time 0.0004693/1.968, allocations: 98.8 kB / 0.6896 GB, free: 7.395 MB / 0.5762 GB
Notification: Performance of postOpt collapseArrayExpressions (initialization): time 4.533e-05/1.968, allocations: 23.98 kB / 0.6896 GB, free: 7.371 MB / 0.5762 GB
Notification: Model statistics after passing the back-end for initialization:
 * Number of independent subsystems: 9
 * Number of states: 0 ()
 * Number of discrete variables: 8 (puitsP3.C.a,puitsP2.C.a,sourceP3.C.b,sourceP2.C.b,plateHeatExchanger.Sc.b,plateHeatExchanger.Sf.b,plateHeatExchanger.Ef.a,plateHeatExchanger.Ec.a)
 * Number of discrete states: 0 ()
 * Number of clocked states: 0 ()
 * Top-level inputs: 0
Notification: Strong component statistics for initialization (22):
 * Single equations (assignments): 17
 * Array equations: 0
 * Algorithm blocks: 0
 * Record equations: 4
 * When equations: 0
 * If-equations: 0
 * Equation systems (not torn): 0
 * Torn equation systems: 1
 * 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): 1 system
   {(6,25)}
Notification: Performance of prepare postOptimizeDAE: time 0.0002601/1.968, allocations: 175.4 kB / 0.6898 GB, free: 7.191 MB / 0.5762 GB
Notification: Performance of postOpt lateInlineFunction (simulation): time 0.0001275/1.968, allocations: 55.25 kB / 0.6898 GB, free: 7.137 MB / 0.5762 GB
Notification: Performance of postOpt wrapFunctionCalls (simulation): time 0.004366/1.973, allocations: 3.947 MB / 0.6937 GB, free: 3.051 MB / 0.5762 GB
Notification: Performance of postOpt simplifysemiLinear (simulation): time 6.733e-06/1.973, allocations: 7.938 kB / 0.6937 GB, free: 3.043 MB / 0.5762 GB
Notification: Performance of postOpt simplifyComplexFunction (simulation): time 2.855e-06/1.973, allocations: 0 / 0.6937 GB, free: 3.043 MB / 0.5762 GB
Notification: Performance of postOpt removeConstants (simulation): time 0.0001648/1.973, allocations: 159.9 kB / 0.6938 GB, free: 2.867 MB / 0.5762 GB
Notification: Performance of postOpt simplifyTimeIndepFuncCalls (simulation): time 0.0001073/1.973, allocations: 27.75 kB / 0.6939 GB, free: 2.84 MB / 0.5762 GB
Notification: Performance of postOpt simplifyAllExpressions (simulation): time 0.0003519/1.973, allocations: 15.98 kB / 0.6939 GB, free: 2.824 MB / 0.5762 GB
Notification: Performance of postOpt findZeroCrossings (simulation): time 9.174e-05/1.974, allocations: 27.95 kB / 0.6939 GB, free: 2.797 MB / 0.5762 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(plateHeatExchanger.Tmf, plateHeatExchanger.rhof, plateHeatExchanger.prof.u, plateHeatExchanger.prof.s, plateHeatExchanger.prof.cp, plateHeatExchanger.prof.ddhp, plateHeatExchanger.prof.ddph, plateHeatExchanger.prof.duph, plateHeatExchanger.prof.duhp, plateHeatExchanger.prof.x) = $cse5

Variables:
1: plateHeatExchanger.prof.ddph:VARIABLE(unit = "s2/m2" )  "Derivative of density wrt. pressure at constant specific enthalpy" type: Real
2: plateHeatExchanger.prof.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific heat capacity at constant presure" type: Real
3: plateHeatExchanger.prof.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific entropy" type: Real
4: plateHeatExchanger.prof.ddhp:VARIABLE(unit = "kg.s2/m5" )  "Derivative of density wrt. specific enthalpy at constant pressure" type: Real
5: plateHeatExchanger.Tmf:VARIABLE(min = 200.0 max = 6000.0 start = 290.0 unit = "K" nominal = 300.0 )  "Cold fluid average temperature" type: Real
6: plateHeatExchanger.prof.duhp:VARIABLE(unit = "1" )  "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real
7: plateHeatExchanger.prof.x:VARIABLE(min = 0.0 max = 1.0 unit = "1" )  "Vapor mass fraction" type: Real
8: plateHeatExchanger.prof.duph:VARIABLE(unit = "m3/kg" )  "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real
9: plateHeatExchanger.quf:VARIABLE()  type: Real
10: plateHeatExchanger.qmf:VARIABLE()  type: Real
[/var/lib/jenkins1/ws/OpenModelicaLibraryTestingWork/OpenModelica/OMCompiler/Compiler/BackEnd/DAEMode.mo:528:7-530:90:writable] Error: Internal error DAEMode.traverserStrongComponents failed on equation:
1/1 (10): ThermoSysPro.Properties.WaterSteam.Common.ThermoProperties_ph(plateHeatExchanger.Tsf, plateHeatExchanger.profs.d, plateHeatExchanger.profs.u, plateHeatExchanger.profs.s, plateHeatExchanger.profs.cp, plateHeatExchanger.profs.ddhp, plateHeatExchanger.profs.ddph, plateHeatExchanger.profs.duph, plateHeatExchanger.profs.duhp, plateHeatExchanger.profs.x) = $cse1
2/11 (10): $cse1 = ThermoSysPro.Properties.WaterSteam.IF97.Water_Ph(puitsP3.P0, plateHeatExchanger.Sf.h, plateHeatExchanger.modef)
3/21 (1): 0.0 = if plateHeatExchanger.Qf > 0.0 then sourceP3.C.h - sourceP3.h else plateHeatExchanger.Sf.h - puitsP3.h
4/22 (10): $cse2 = ThermoSysPro.Properties.WaterSteam.IF97.Water_Ph(sourceP3.P0, sourceP3.C.h, plateHeatExchanger.modef)
5/32 (1): 0.0 = if abs(plateHeatExchanger.Qf) > 0.001 then plateHeatExchanger.W - plateHeatExchanger.Qf * plateHeatExchanger.prof.cp * (plateHeatExchanger.Tsf - plateHeatExchanger.Tef) else plateHeatExchanger.Tef - plateHeatExchanger.Tsf
6/33 (1): plateHeatExchanger.W = plateHeatExchanger.K * plateHeatExchanger.S * plateHeatExchanger.DTm
7/34 (1): plateHeatExchanger.DTm = if noEvent(plateHeatExchanger.DT1 > plateHeatExchanger.DT2) and noEvent(plateHeatExchanger.DT2 > 0.0) or noEvent(plateHeatExchanger.DT1 < plateHeatExchanger.DT2) and noEvent(plateHeatExchanger.DT2 < 0.0) then (plateHeatExchanger.DT1 - plateHeatExchanger.DT2) / log(plateHeatExchanger.DT1 / plateHeatExchanger.DT2) else 0.5 * (plateHeatExchanger.DT1 + plateHeatExchanger.DT2)
8/35 (1): plateHeatExchanger.DT1 = plateHeatExchanger.Tec - plateHeatExchanger.Tsf
9/36 (1): 0.0 = if abs(plateHeatExchanger.Qc) > 0.001 then plateHeatExchanger.W - plateHeatExchanger.Qc * plateHeatExchanger.proc.cp * (plateHeatExchanger.Tec - plateHeatExchanger.Tsc) else plateHeatExchanger.Tec - plateHeatExchanger.Tsc
10/37 (1): plateHeatExchanger.DT2 = plateHeatExchanger.Tsc - plateHeatExchanger.Tef
11/38 (10): $cse3 = ThermoSysPro.Properties.WaterSteam.IF97.Water_Ph(puitsP2.P0, plateHeatExchanger.Sc.h, plateHeatExchanger.modec)
12/48 (10): ThermoSysPro.Properties.WaterSteam.Common.ThermoProperties_ph(plateHeatExchanger.Tsc, plateHeatExchanger.procs.d, plateHeatExchanger.procs.u, plateHeatExchanger.procs.s, plateHeatExchanger.procs.cp, plateHeatExchanger.procs.ddhp, plateHeatExchanger.procs.ddph, plateHeatExchanger.procs.duph, plateHeatExchanger.procs.duhp, plateHeatExchanger.procs.x) = $cse3
13/58 (1): 0.0 = if plateHeatExchanger.Qc > 0.0 then sourceP2.C.h - sourceP2.h else plateHeatExchanger.Sc.h - puitsP2.h
14/59 (10): $cse4 = ThermoSysPro.Properties.WaterSteam.IF97.Water_Ph(sourceP2.P0, sourceP2.C.h, plateHeatExchanger.modec)
15/69 (10): ThermoSysPro.Properties.WaterSteam.Common.ThermoProperties_ph(plateHeatExchanger.Tec, plateHeatExchanger.proce.d, plateHeatExchanger.proce.u, plateHeatExchanger.proce.s, plateHeatExchanger.proce.cp, plateHeatExchanger.proce.ddhp, plateHeatExchanger.proce.ddph, plateHeatExchanger.proce.duph, plateHeatExchanger.proce.duhp, plateHeatExchanger.proce.x) = $cse4
16/79 (1): plateHeatExchanger.Hmc = 0.5 * (sourceP2.C.h + plateHeatExchanger.Sc.h)
17/80 (10): $cse6 = ThermoSysPro.Properties.WaterSteam.IF97.Water_Ph(plateHeatExchanger.Pmc, plateHeatExchanger.Hmc, plateHeatExchanger.modec)
18/90 (1): plateHeatExchanger.lambdac = ThermoSysPro.Properties.WaterSteam.IF97.ThermalConductivity_rhoT(plateHeatExchanger.rhoc, plateHeatExchanger.Tmc, plateHeatExchanger.Pmc, 0)
19/91 (1): plateHeatExchanger.hc = if noEvent(plateHeatExchanger.qmc < 0.001) then 0.0 else 11.245 * plateHeatExchanger.qmc ^ 0.8 * abs(plateHeatExchanger.muc * plateHeatExchanger.proc.cp / plateHeatExchanger.lambdac) ^ 0.4 * plateHeatExchanger.lambdac
20/92 (1): plateHeatExchanger.K = plateHeatExchanger.hc * plateHeatExchanger.hf / (plateHeatExchanger.hc + plateHeatExchanger.hf + plateHeatExchanger.hc * plateHeatExchanger.hf * plateHeatExchanger.emetal / plateHeatExchanger.lambdam)
21/93 (1): plateHeatExchanger.muc = ThermoSysPro.Properties.WaterSteam.IF97.DynamicViscosity_rhoT(plateHeatExchanger.rhoc, plateHeatExchanger.Tmc)
22/94 (1): plateHeatExchanger.qmc = abs(plateHeatExchanger.Qc) / (plateHeatExchanger.N * plateHeatExchanger.muc)
23/95 (1): plateHeatExchanger.DPc = if noEvent(plateHeatExchanger.qmc < 0.001) then 0.0 else plateHeatExchanger.c1 * 14423.2 / (plateHeatExchanger.rhoc * plateHeatExchanger.qmc ^ 0.097) * plateHeatExchanger.quc ^ 2.0 * (1472.47 + 0.77 * (plateHeatExchanger.N - 1.0) + 104.97 / plateHeatExchanger.qmc ^ 0.25)
24/96 (1): plateHeatExchanger.quc = abs(plateHeatExchanger.Qc) / plateHeatExchanger.N
25/97 (1): puitsP2.P0 = if plateHeatExchanger.Qc > 0.0 then sourceP2.P0 - plateHeatExchanger.DPc else sourceP2.P0 + plateHeatExchanger.DPc
26/98 (10): ThermoSysPro.Properties.WaterSteam.Common.ThermoProperties_ph(plateHeatExchanger.Tmc, plateHeatExchanger.rhoc, plateHeatExchanger.proc.u, plateHeatExchanger.proc.s, plateHeatExchanger.proc.cp, plateHeatExchanger.proc.ddhp, plateHeatExchanger.proc.ddph, plateHeatExchanger.proc.duph, plateHeatExchanger.proc.duhp, plateHeatExchanger.proc.x) = $cse6
27/108 (10): ThermoSysPro.Properties.WaterSteam.Common.ThermoProperties_ph(plateHeatExchanger.Tef, plateHeatExchanger.profe.d, plateHeatExchanger.profe.u, plateHeatExchanger.profe.s, plateHeatExchanger.profe.cp, plateHeatExchanger.profe.ddhp, plateHeatExchanger.profe.ddph, plateHeatExchanger.profe.duph, plateHeatExchanger.profe.duhp, plateHeatExchanger.profe.x) = $cse2
28/118 (1): plateHeatExchanger.Hmf = 0.5 * (sourceP3.C.h + plateHeatExchanger.Sf.h)
29/119 (10): $cse5 = ThermoSysPro.Properties.WaterSteam.IF97.Water_Ph(plateHeatExchanger.Pmf, plateHeatExchanger.Hmf, plateHeatExchanger.modef)
30/129 (1): plateHeatExchanger.lambdaf = ThermoSysPro.Properties.WaterSteam.IF97.ThermalConductivity_rhoT(plateHeatExchanger.rhof, plateHeatExchanger.Tmf, plateHeatExchanger.Pmf, 0)
31/130 (1): plateHeatExchanger.hf = if noEvent(plateHeatExchanger.qmf < 0.001) then 0.0 else 11.245 * plateHeatExchanger.qmf ^ 0.8 * abs(plateHeatExchanger.muf * plateHeatExchanger.prof.cp / plateHeatExchanger.lambdaf) ^ 0.4 * plateHeatExchanger.lambdaf
32/131 (1): plateHeatExchanger.muf = ThermoSysPro.Properties.WaterSteam.IF97.DynamicViscosity_rhoT(plateHeatExchanger.rhof, plateHeatExchanger.Tmf)
33/132 (1): plateHeatExchanger.qmf = abs(plateHeatExchanger.Qf) / (plateHeatExchanger.N * plateHeatExchanger.muf)
34/133 (1): puitsP3.P0 = if plateHeatExchanger.Qf > 0.0 then sourceP3.P0 - plateHeatExchanger.DPf else sourceP3.P0 + plateHeatExchanger.DPf
35/134 (1): plateHeatExchanger.DPf = if noEvent(plateHeatExchanger.qmf < 0.001) then 0.0 else 14423.2 / (plateHeatExchanger.rhof * plateHeatExchanger.qmf ^ 0.097) * plateHeatExchanger.quf ^ 2.0 * (1472.47 + 0.77 * (plateHeatExchanger.N - 1.0) + 104.97 / plateHeatExchanger.qmf ^ 0.25)
36/135 (1): plateHeatExchanger.quf = abs(plateHeatExchanger.Qf) / plateHeatExchanger.N
37/136 (10): ThermoSysPro.Properties.WaterSteam.Common.ThermoProperties_ph(plateHeatExchanger.Tmf, plateHeatExchanger.rhof, plateHeatExchanger.prof.u, plateHeatExchanger.prof.s, plateHeatExchanger.prof.cp, plateHeatExchanger.prof.ddhp, plateHeatExchanger.prof.ddph, plateHeatExchanger.prof.duph, plateHeatExchanger.prof.duhp, plateHeatExchanger.prof.x) = $cse5

Variables:
1: plateHeatExchanger.prof.ddph:VARIABLE(unit = "s2/m2" )  "Derivative of density wrt. pressure at constant specific enthalpy" type: Real
2: plateHeatExchanger.prof.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific heat capacity at constant presure" type: Real
3: plateHeatExchanger.prof.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific entropy" type: Real
4: plateHeatExchanger.prof.ddhp:VARIABLE(unit = "kg.s2/m5" )  "Derivative of density wrt. specific enthalpy at constant pressure" type: Real
5: plateHeatExchanger.Tmf:VARIABLE(min = 200.0 max = 6000.0 start = 290.0 unit = "K" nominal = 300.0 )  "Cold fluid average temperature" type: Real
6: plateHeatExchanger.prof.duhp:VARIABLE(unit = "1" )  "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real
7: plateHeatExchanger.prof.x:VARIABLE(min = 0.0 max = 1.0 unit = "1" )  "Vapor mass fraction" type: Real
8: plateHeatExchanger.prof.duph:VARIABLE(unit = "m3/kg" )  "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real
9: plateHeatExchanger.quf:VARIABLE()  type: Real
10: plateHeatExchanger.qmf:VARIABLE()  type: Real
11: plateHeatExchanger.DPf:VARIABLE(unit = "Pa" )  "Pressure loss of the cold fluid" type: Real
12: plateHeatExchanger.Qf:VARIABLE(start = 500.0 unit = "kg/s" )  "Mass flow rate of the cold fluid" type: Real
13: plateHeatExchanger.muf:VARIABLE(min = 0.0 start = 0.001 unit = "Pa.s" )  "Cold fluid dynamic viscosity" type: Real
14: plateHeatExchanger.hf:VARIABLE(unit = "W/(m2.K)" )  "Heat transfer coefficient of the cold fluid" type: Real
15: plateHeatExchanger.lambdaf:VARIABLE(start = 0.597928 unit = "W/(m.K)" )  "Cold fluid thermal conductivity" type: Real
16: plateHeatExchanger.rhof:VARIABLE(min = 1e-9 max = 1e5 start = 998.0 unit = "kg/m3" nominal = 998.0 )  "Cold fluid density" type: Real
17: plateHeatExchanger.prof.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 )  "Specific inner energy" type: Real
18: $cse5.d:VARIABLE(protected = true )  type: Real unreplaceable
19: $cse5.s:VARIABLE(protected = true )  type: Real unreplaceable
20: $cse5.x:VARIABLE(protected = true )  type: Real unreplaceable
21: $cse5.duhp:VARIABLE(protected = true )  type: Real unreplaceable
22: $cse5.u:VARIABLE(protected = true )  type: Real unreplaceable
23: $cse5.T:VARIABLE(protected = true )  type: Real unreplaceable
24: $cse5.duph:VARIABLE(protected = true )  type: Real unreplaceable
25: $cse5.ddhp:VARIABLE(protected = true )  type: Real unreplaceable
26: $cse5.cp:VARIABLE(protected = true )  type: Real unreplaceable
27: $cse5.ddph:VARIABLE(protected = true )  type: Real unreplaceable
28: plateHeatExchanger.Hmf:VARIABLE(start = 1e5 unit = "J/kg" )  "Cold fluid average specific enthalpy" type: Real
29: plateHeatExchanger.profe.duhp:VARIABLE(unit = "1" )  "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real
30: plateHeatExchanger.profe.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific entropy" type: Real
31: plateHeatExchanger.profe.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 )  "Density" type: Real
32: plateHeatExchanger.profe.x:VARIABLE(min = 0.0 max = 1.0 unit = "1" )  "Vapor mass fraction" type: Real
33: plateHeatExchanger.profe.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 )  "Specific inner energy" type: Real
34: plateHeatExchanger.proc.ddph:VARIABLE(unit = "s2/m2" )  "Derivative of density wrt. pressure at constant specific enthalpy" type: Real
35: plateHeatExchanger.proc.ddhp:VARIABLE(unit = "kg.s2/m5" )  "Derivative of density wrt. specific enthalpy at constant pressure" type: Real
36: plateHeatExchanger.proc.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific entropy" type: Real
37: plateHeatExchanger.proc.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 )  "Specific inner energy" type: Real
38: plateHeatExchanger.proc.x:VARIABLE(min = 0.0 max = 1.0 unit = "1" )  "Vapor mass fraction" type: Real
39: plateHeatExchanger.proc.duph:VARIABLE(unit = "m3/kg" )  "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real
40: plateHeatExchanger.proc.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific heat capacity at constant presure" type: Real
41: plateHeatExchanger.Tmc:VARIABLE(min = 200.0 max = 6000.0 start = 290.0 unit = "K" nominal = 300.0 )  "Hot fluid average temperature" type: Real
42: plateHeatExchanger.DPc:VARIABLE(unit = "Pa" )  "Pressure loss of the hot fluid" type: Real
43: plateHeatExchanger.Qc:VARIABLE(start = 500.0 unit = "kg/s" )  "Mass flow rate of the hot fluid" type: Real
44: plateHeatExchanger.quc:VARIABLE()  type: Real
45: plateHeatExchanger.qmc:VARIABLE()  type: Real
46: plateHeatExchanger.muc:VARIABLE(min = 0.0 start = 0.001 unit = "Pa.s" )  "Hot fluid dynamic viscosity" type: Real
47: plateHeatExchanger.K:VARIABLE(unit = "W/(m2.K)" )  "Global heat transfer coefficient" type: Real
48: plateHeatExchanger.hc:VARIABLE(unit = "W/(m2.K)" )  "Heat transfer coefficient of the hot fluid" type: Real
49: plateHeatExchanger.lambdac:VARIABLE(start = 0.602698 unit = "W/(m.K)" )  "Hot fluid thermal conductivity" type: Real
50: plateHeatExchanger.rhoc:VARIABLE(min = 1e-9 max = 1e5 start = 998.0 unit = "kg/m3" nominal = 998.0 )  "Hot fluid density" type: Real
51: plateHeatExchanger.proc.duhp:VARIABLE(unit = "1" )  "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real
52: $cse6.ddhp:VARIABLE(protected = true )  type: Real unreplaceable
53: $cse6.x:VARIABLE(protected = true )  type: Real unreplaceable
54: $cse6.ddph:VARIABLE(protected = true )  type: Real unreplaceable
55: $cse6.duph:VARIABLE(protected = true )  type: Real unreplaceable
56: $cse6.s:VARIABLE(protected = true )  type: Real unreplaceable
57: $cse6.d:VARIABLE(protected = true )  type: Real unreplaceable
58: $cse6.duhp:VARIABLE(protected = true )  type: Real unreplaceable
59: $cse6.u:VARIABLE(protected = true )  type: Real unreplaceable
60: $cse6.cp:VARIABLE(protected = true )  type: Real unreplaceable
61: $cse6.T:VARIABLE(protected = true )  type: Real unreplaceable
62: plateHeatExchanger.Hmc:VARIABLE(start = 1e5 unit = "J/kg" )  "Hot fluid average specific enthalpy" type: Real
63: plateHeatExchanger.proce.ddph:VARIABLE(unit = "s2/m2" )  "Derivative of density wrt. pressure at constant specific enthalpy" type: Real
64: plateHeatExchanger.proce.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific heat capacity at constant presure" type: Real
65: plateHeatExchanger.proce.x:VARIABLE(min = 0.0 max = 1.0 unit = "1" )  "Vapor mass fraction" type: Real
66: plateHeatExchanger.proce.duph:VARIABLE(unit = "m3/kg" )  "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real
67: plateHeatExchanger.proce.duhp:VARIABLE(unit = "1" )  "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real
68: plateHeatExchanger.proce.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific entropy" type: Real
69: plateHeatExchanger.proce.ddhp:VARIABLE(unit = "kg.s2/m5" )  "Derivative of density wrt. specific enthalpy at constant pressure" type: Real
70: plateHeatExchanger.proce.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 )  "Specific inner energy" type: Real
71: plateHeatExchanger.Tec:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 300.0 )  "Fluid temperature at the hot inlet" type: Real
72: plateHeatExchanger.proce.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 )  "Density" type: Real
73: $cse4.d:VARIABLE(protected = true )  type: Real unreplaceable
74: $cse4.u:VARIABLE(protected = true )  type: Real unreplaceable
75: $cse4.duhp:VARIABLE(protected = true )  type: Real unreplaceable
76: $cse4.ddph:VARIABLE(protected = true )  type: Real unreplaceable
77: $cse4.duph:VARIABLE(protected = true )  type: Real unreplaceable
78: $cse4.cp:VARIABLE(protected = true )  type: Real unreplaceable
79: $cse4.s:VARIABLE(protected = true )  type: Real unreplaceable
80: $cse4.ddhp:VARIABLE(protected = true )  type: Real unreplaceable
81: $cse4.T:VARIABLE(protected = true )  type: Real unreplaceable
82: $cse4.x:VARIABLE(protected = true )  type: Real unreplaceable
83: sourceP2.C.h:VARIABLE(flow=false start = 1e5 unit = "J/kg" )  "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real
84: plateHeatExchanger.procs.ddhp:VARIABLE(unit = "kg.s2/m5" )  "Derivative of density wrt. specific enthalpy at constant pressure" type: Real
85: plateHeatExchanger.procs.duhp:VARIABLE(unit = "1" )  "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real
86: plateHeatExchanger.procs.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific heat capacity at constant presure" type: Real
87: plateHeatExchanger.procs.duph:VARIABLE(unit = "m3/kg" )  "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real
88: plateHeatExchanger.procs.ddph:VARIABLE(unit = "s2/m2" )  "Derivative of density wrt. pressure at constant specific enthalpy" type: Real
89: plateHeatExchanger.procs.x:VARIABLE(min = 0.0 max = 1.0 unit = "1" )  "Vapor mass fraction" type: Real
90: plateHeatExchanger.procs.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 )  "Specific inner energy" type: Real
91: plateHeatExchanger.procs.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 )  "Density" type: Real
92: $cse3.d:VARIABLE(protected = true )  type: Real unreplaceable
93: $cse3.duph:VARIABLE(protected = true )  type: Real unreplaceable
94: $cse3.cp:VARIABLE(protected = true )  type: Real unreplaceable
95: $cse3.T:VARIABLE(protected = true )  type: Real unreplaceable
96: plateHeatExchanger.Sc.h:VARIABLE(flow=false start = 1e5 unit = "J/kg" )  "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real
97: $cse3.u:VARIABLE(protected = true )  type: Real unreplaceable
98: $cse3.ddph:VARIABLE(protected = true )  type: Real unreplaceable
99: $cse3.x:VARIABLE(protected = true )  type: Real unreplaceable
100: $cse3.ddhp:VARIABLE(protected = true )  type: Real unreplaceable
101: $cse3.duhp:VARIABLE(protected = true )  type: Real unreplaceable
102: $cse3.s:VARIABLE(protected = true )  type: Real unreplaceable
103: plateHeatExchanger.procs.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific entropy" type: Real
104: plateHeatExchanger.DT2:VARIABLE(unit = "K" )  "Temperature difference at the outlet of the exchanger" type: Real
105: plateHeatExchanger.Tsc:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 300.0 )  "Fluid temperature at the hot outlet" type: Real
106: plateHeatExchanger.Tsf:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 300.0 )  "Fluid temperature at the cold outlet" type: Real
107: plateHeatExchanger.DT1:VARIABLE(unit = "K" )  "Temperature difference at the inlet of the exchanger" type: Real
108: plateHeatExchanger.DTm:VARIABLE(unit = "K" )  "Difference in average temperature" type: Real
109: plateHeatExchanger.W:VARIABLE(unit = "W" )  "Thermal power exchanged between the two sides" type: Real
110: plateHeatExchanger.Tef:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 300.0 )  "Fluid temperature at the cold inlet" type: Real
111: plateHeatExchanger.profe.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific heat capacity at constant presure" type: Real
112: plateHeatExchanger.profe.ddhp:VARIABLE(unit = "kg.s2/m5" )  "Derivative of density wrt. specific enthalpy at constant pressure" type: Real
113: plateHeatExchanger.profe.duph:VARIABLE(unit = "m3/kg" )  "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real
114: plateHeatExchanger.profe.ddph:VARIABLE(unit = "s2/m2" )  "Derivative of density wrt. pressure at constant specific enthalpy" type: Real
115: $cse2.d:VARIABLE(protected = true )  type: Real unreplaceable
116: $cse2.x:VARIABLE(protected = true )  type: Real unreplaceable
117: $cse2.s:VARIABLE(protected = true )  type: Real unreplaceable
118: $cse2.u:VARIABLE(protected = true )  type: Real unreplaceable
119: $cse2.ddhp:VARIABLE(protected = true )  type: Real unreplaceable
120: $cse2.duph:VARIABLE(protected = true )  type: Real unreplaceable
121: $cse2.ddph:VARIABLE(protected = true )  type: Real unreplaceable
122: $cse2.duhp:VARIABLE(protected = true )  type: Real unreplaceable
123: $cse2.cp:VARIABLE(protected = true )  type: Real unreplaceable
124: $cse2.T:VARIABLE(protected = true )  type: Real unreplaceable
125: sourceP3.C.h:VARIABLE(flow=false start = 1e5 unit = "J/kg" )  "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real
126: plateHeatExchanger.Sf.h:VARIABLE(flow=false start = 1e5 unit = "J/kg" )  "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real
127: $cse1.duph:VARIABLE(protected = true )  type: Real unreplaceable
128: $cse1.u:VARIABLE(protected = true )  type: Real unreplaceable
129: $cse1.ddph:VARIABLE(protected = true )  type: Real unreplaceable
130: $cse1.cp:VARIABLE(protected = true )  type: Real unreplaceable
131: $cse1.s:VARIABLE(protected = true )  type: Real unreplaceable
132: $cse1.d:VARIABLE(protected = true )  type: Real unreplaceable
133: $cse1.ddhp:VARIABLE(protected = true )  type: Real unreplaceable
134: $cse1.T:VARIABLE(protected = true )  type: Real unreplaceable
135: $cse1.duhp:VARIABLE(protected = true )  type: Real unreplaceable
136: $cse1.x:VARIABLE(protected = true )  type: Real unreplaceable
137: plateHeatExchanger.profs.x:VARIABLE(min = 0.0 max = 1.0 unit = "1" )  "Vapor mass fraction" type: Real
138: plateHeatExchanger.profs.duhp:VARIABLE(unit = "1" )  "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real
139: plateHeatExchanger.profs.ddhp:VARIABLE(unit = "kg.s2/m5" )  "Derivative of density wrt. specific enthalpy at constant pressure" type: Real
140: plateHeatExchanger.profs.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 )  "Specific inner energy" type: Real
141: plateHeatExchanger.profs.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific entropy" type: Real
142: plateHeatExchanger.profs.ddph:VARIABLE(unit = "s2/m2" )  "Derivative of density wrt. pressure at constant specific enthalpy" type: Real
143: plateHeatExchanger.profs.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific heat capacity at constant presure" type: Real
144: plateHeatExchanger.profs.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 )  "Density" type: Real
145: plateHeatExchanger.profs.duph:VARIABLE(unit = "m3/kg" )  "Derivative of specific inner energy wrt. pressure at constant 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 0.004554/1.978, allocations: 6.583 MB / 0.7003 GB, free: 10.86 MB / 0.5919 GB
Error: post-optimization module createDAEmodeBDAE (simulation) failed.
Error: Internal error SimCode DAEmode: The model ThermoSysPro.Examples.SimpleExamples.TestStaticWaterWaterExchanger could not be translated