Running: ./testmodel.py --libraries=/home/hudson/saved_omc/libraries/.openmodelica/libraries --ompython_omhome=/usr ThermoSysPro_ThermoSysPro.Fluid.Examples.SimpleExamples.TestStaticPlateHeatExchanger.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.TestStaticPlateHeatExchanger,tolerance=1e-06,outputFormat="empty",numberOfIntervals=5000,variableFilter="",fileNamePrefix="ThermoSysPro_ThermoSysPro.Fluid.Examples.SimpleExamples.TestStaticPlateHeatExchanger")
translateModel(ThermoSysPro.Fluid.Examples.SimpleExamples.TestStaticPlateHeatExchanger,tolerance=1e-06,outputFormat="empty",numberOfIntervals=5000,variableFilter="",fileNamePrefix="ThermoSysPro_ThermoSysPro.Fluid.Examples.SimpleExamples.TestStaticPlateHeatExchanger")
Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermoSysPro 4.0.0-master/package.mo): time 0.8428/0.8428, allocations: 150.9 MB / 167.2 MB, free: 14.59 MB / 142.1 MB
Notification: Performance of FrontEnd - loaded program: time 0.0003484/0.0003485, allocations: 18.88 kB / 237.8 MB, free: 1.715 MB / 190.1 MB
Notification: Performance of FrontEnd - Absyn->SCode: time 0.05873/0.05909, allocations: 31.35 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.TestStaticPlateHeatExchanger): time 1.69/1.749, allocations: 296.8 MB / 0.5526 GB, free: 10.98 MB / 446.1 MB
Notification: Performance of NFInst.instExpressions: time 0.5128/2.262, allocations: 188.7 MB / 0.737 GB, free: 15.76 MB / 0.6075 GB
Notification: Performance of NFInst.updateImplicitVariability: time 0.0007055/2.263, allocations: 12.5 kB / 0.737 GB, free: 15.76 MB / 0.6075 GB
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermoSysPro 4.0.0-master/Fluid/HeatExchangers/StaticPlateHeatExchanger.mo:91:3-92:54:writable] Warning: Connector Ec 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/StaticPlateHeatExchanger.mo:93:3-94:54:writable] Warning: Connector Ef 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/StaticPlateHeatExchanger.mo:95:3-96:52:writable] Warning: Connector Sf 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/StaticPlateHeatExchanger.mo:97:3-98:51:writable] Warning: Connector Sc 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/BoundaryConditions/SinkP.mo:46:3-47:67:writable] Warning: Connector C is not balanced: The number of potential variables (9) is not equal to the number of flow variables (0).
Notification: Performance of NFTyping.typeComponents: time 0.0007755/2.264, allocations: 183.3 kB / 0.7371 GB, free: 15.76 MB / 0.6075 GB
Notification: Performance of NFTyping.typeBindings: time 0.001227/2.265, allocations: 326.7 kB / 0.7375 GB, free: 15.75 MB / 0.6075 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.
Notification: Performance of NFTyping.typeClassSections: time 0.02948/2.294, allocations: 11.62 MB / 0.7488 GB, free: 15.52 MB / 0.6075 GB
Notification: Performance of NFFlatten.flatten: time 0.001726/2.296, allocations: 1.129 MB / 0.7499 GB, free: 15.52 MB / 0.6075 GB
Notification: Performance of NFFlatten.resolveConnections: time 0.0005852/2.297, allocations: 464.7 kB / 0.7503 GB, free: 15.45 MB / 0.6075 GB
Notification: Performance of NFEvalConstants.evaluate: time 0.0005664/2.297, allocations: 468.4 kB / 0.7508 GB, free: 15.45 MB / 0.6075 GB
Notification: Performance of NFSimplifyModel.simplify: time 0.0004461/2.298, allocations: 443.6 kB / 0.7512 GB, free: 15.45 MB / 0.6075 GB
Notification: Performance of NFPackage.collectConstants: time 9.682e-05/2.298, allocations: 77.91 kB / 0.7513 GB, free: 15.45 MB / 0.6075 GB
Notification: Performance of NFFlatten.collectFunctions: time 0.03794/2.336, allocations: 19.43 MB / 0.7703 GB, free: 12.71 MB / 0.6075 GB
Notification: Performance of NFScalarize.scalarize: time 0.0003796/2.336, allocations: 188 kB / 0.7704 GB, free: 12.68 MB / 0.6075 GB
Notification: Performance of NFVerifyModel.verify: time 0.0008246/2.337, allocations: 489.7 kB / 0.7709 GB, free: 12.65 MB / 0.6075 GB
Notification: Performance of NFConvertDAE.convert: time 0.02693/2.364, allocations: 10.24 MB / 0.7809 GB, free: 8.922 MB / 0.6075 GB
Notification: Performance of FrontEnd - DAE generated: time 7.224e-06/2.364, allocations: 1.203 kB / 0.7809 GB, free: 8.922 MB / 0.6075 GB
Notification: Performance of FrontEnd: time 1.563e-06/2.364, allocations: 2.344 kB / 0.7809 GB, free: 8.922 MB / 0.6075 GB
Notification: Performance of Transformations before backend: time 1.352e-05/2.364, allocations: 2.906 kB / 0.7809 GB, free: 8.922 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: 250
 * Number of variables: 250
Notification: Performance of Generate backend data structure: time 0.006179/2.37, allocations: 2.246 MB / 0.7831 GB, free: 7.551 MB / 0.6075 GB
Notification: Performance of prepare preOptimizeDAE: time 4.51e-05/2.37, allocations: 10.09 kB / 0.7831 GB, free: 7.551 MB / 0.6075 GB
Notification: Performance of preOpt normalInlineFunction (simulation): time 0.0001575/2.37, allocations: 104.8 kB / 0.7832 GB, free: 7.496 MB / 0.6075 GB
Notification: Performance of preOpt evaluateParameters (simulation): time 0.0006273/2.371, allocations: 490.6 kB / 0.7837 GB, free: 7.152 MB / 0.6075 GB
Notification: Performance of preOpt simplifyIfEquations (simulation): time 0.0002041/2.371, allocations: 150.5 kB / 0.7838 GB, free: 7.051 MB / 0.6075 GB
Notification: Performance of preOpt expandDerOperator (simulation): time 8.84e-05/2.371, allocations: 74.28 kB / 0.7839 GB, free: 7.051 MB / 0.6075 GB
Notification: Performance of preOpt clockPartitioning (simulation): time 0.001299/2.373, allocations: 0.9224 MB / 0.7848 GB, free: 6.754 MB / 0.6075 GB
Notification: Performance of preOpt findStateOrder (simulation): time 2.171e-05/2.373, allocations: 3.969 kB / 0.7848 GB, free: 6.754 MB / 0.6075 GB
Notification: Performance of preOpt replaceEdgeChange (simulation): time 5.9e-05/2.373, allocations: 36.7 kB / 0.7848 GB, free: 6.754 MB / 0.6075 GB
Notification: Performance of preOpt inlineArrayEqn (simulation): time 2.646e-05/2.373, allocations: 31.02 kB / 0.7849 GB, free: 6.75 MB / 0.6075 GB
Notification: Performance of preOpt removeEqualRHS (simulation): time 0.001205/2.374, allocations: 0.6701 MB / 0.7855 GB, free: 6.648 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 0.01634/2.39, allocations: 12.8 MB / 0.798 GB, free: 11.94 MB / 0.6231 GB
Notification: Performance of preOpt comSubExp (simulation): time 0.001083/2.392, allocations: 454.6 kB / 0.7985 GB, free: 11.86 MB / 0.6231 GB
Notification: Performance of preOpt resolveLoops (simulation): time 0.0004804/2.392, allocations: 261.8 kB / 0.7987 GB, free: 11.83 MB / 0.6231 GB
Notification: Performance of preOpt evalFunc (simulation): time 0.08889/2.481, allocations: 52.45 MB / 0.8499 GB, free: 2.848 MB / 0.67 GB
Notification: Performance of preOpt encapsulateWhenConditions (simulation): time 3.924e-05/2.481, allocations: 30.56 kB / 0.85 GB, free: 2.809 MB / 0.67 GB
Notification: Performance of pre-optimization done (n=88): time 3.957e-06/2.481, allocations: 4.688 kB / 0.85 GB, free: 2.809 MB / 0.67 GB
Notification: Performance of matching and sorting (n=88): time 0.01656/2.498, allocations: 3.024 MB / 0.8529 GB, free: 15.77 MB / 0.6856 GB
Notification: Performance of inlineWhenForInitialization (initialization): time 3.475e-05/2.498, allocations: 56.89 kB / 0.853 GB, free: 15.7 MB / 0.6856 GB
Notification: Performance of selectInitializationVariablesDAE (initialization): time 0.0006122/2.498, allocations: 0.4947 MB / 0.8535 GB, free: 15.2 MB / 0.6856 GB
Notification: Performance of collectPreVariables (initialization): time 3.488e-05/2.498, allocations: 29.7 kB / 0.8535 GB, free: 15.16 MB / 0.6856 GB
Notification: Performance of collectInitialEqns (initialization): time 0.0002409/2.499, allocations: 384.1 kB / 0.8539 GB, free: 14.78 MB / 0.6856 GB
Notification: Performance of collectInitialBindings (initialization): time 0.0002018/2.499, allocations: 297.1 kB / 0.8541 GB, free: 14.5 MB / 0.6856 GB
Notification: Performance of simplifyInitialFunctions (initialization): time 0.0001981/2.499, allocations: 150 kB / 0.8543 GB, free: 14.34 MB / 0.6856 GB
Notification: Performance of setup shared object (initialization): time 0.0001517/2.499, allocations: 378.7 kB / 0.8546 GB, free: 13.96 MB / 0.6856 GB
Notification: Performance of preBalanceInitialSystem (initialization): time 0.0005357/2.5, allocations: 234.6 kB / 0.8549 GB, free: 13.74 MB / 0.6856 GB
Notification: Performance of partitionIndependentBlocks (initialization): time 0.000654/2.5, allocations: 424.2 kB / 0.8553 GB, free: 13.25 MB / 0.6856 GB
Notification: Performance of analyzeInitialSystem (initialization): time 0.001219/2.502, allocations: 0.7008 MB / 0.856 GB, free: 12.49 MB / 0.6856 GB
Notification: Performance of solveInitialSystemEqSystem (initialization): time 6.903e-06/2.502, allocations: 4 kB / 0.856 GB, free: 12.49 MB / 0.6856 GB
Notification: Performance of matching and sorting (n=122) (initialization): time 0.002721/2.504, allocations: 1.094 MB / 0.857 GB, free: 11.42 MB / 0.6856 GB
Notification: Performance of prepare postOptimizeDAE: time 2.102e-05/2.504, allocations: 8 kB / 0.857 GB, free: 11.41 MB / 0.6856 GB
Notification: Performance of postOpt simplifyComplexFunction (initialization): time 1.554e-05/2.504, allocations: 8 kB / 0.857 GB, free: 11.41 MB / 0.6856 GB
Notification: Performance of postOpt tearingSystem (initialization): time 0.003064/2.507, allocations: 0.9476 MB / 0.858 GB, free: 10.46 MB / 0.6856 GB
Notification: Performance of postOpt solveSimpleEquations (initialization): time 0.0002182/2.508, allocations: 71.66 kB / 0.858 GB, free: 10.39 MB / 0.6856 GB
Notification: Performance of postOpt calculateStrongComponentJacobians (initialization): time 0.002166/2.51, allocations: 1.393 MB / 0.8594 GB, free: 8.98 MB / 0.6856 GB
Notification: Performance of postOpt simplifyAllExpressions (initialization): time 0.0005494/2.51, allocations: 102.6 kB / 0.8595 GB, free: 8.883 MB / 0.6856 GB
Notification: Performance of postOpt collapseArrayExpressions (initialization): time 5.125e-05/2.51, allocations: 35.98 kB / 0.8595 GB, free: 8.848 MB / 0.6856 GB
Notification: Model statistics after passing the back-end for initialization:
 * Number of independent subsystems: 25
 * Number of states: 0 ()
 * Number of discrete variables: 8 (sourceP3.C.ftype,sourceP2.C.ftype,plateHeatExchanger.fluid_c,plateHeatExchanger.fluid_f,puitsP2.fluid,puitsP3.fluid,sourceP3.fluid1,sourceP2.fluid1)
 * Number of discrete states: 0 ()
 * Number of clocked states: 0 ()
 * Top-level inputs: 0
Notification: Strong component statistics for initialization (38):
 * Single equations (assignments): 37
 * Array equations: 0
 * Algorithm blocks: 0
 * Record equations: 0
 * 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
   {(4,27)}
Notification: Performance of prepare postOptimizeDAE: time 0.0003053/2.511, allocations: 206.5 kB / 0.8597 GB, free: 8.645 MB / 0.6856 GB
Notification: Performance of postOpt lateInlineFunction (simulation): time 0.0001038/2.511, allocations: 67.09 kB / 0.8598 GB, free: 8.578 MB / 0.6856 GB
Notification: Performance of postOpt wrapFunctionCalls (simulation): time 0.002497/2.513, allocations: 1.747 MB / 0.8615 GB, free: 6.824 MB / 0.6856 GB
Notification: Performance of postOpt simplifysemiLinear (simulation): time 1.043e-05/2.513, allocations: 10.42 kB / 0.8615 GB, free: 6.816 MB / 0.6856 GB
Notification: Performance of postOpt simplifyComplexFunction (simulation): time 3.126e-06/2.513, allocations: 0 / 0.8615 GB, free: 6.816 MB / 0.6856 GB
Notification: Performance of postOpt removeConstants (simulation): time 0.0002719/2.514, allocations: 223.6 kB / 0.8617 GB, free: 6.578 MB / 0.6856 GB
Notification: Performance of postOpt simplifyTimeIndepFuncCalls (simulation): time 6.53e-05/2.514, allocations: 4 kB / 0.8617 GB, free: 6.574 MB / 0.6856 GB
Notification: Performance of postOpt simplifyAllExpressions (simulation): time 0.0003145/2.514, allocations: 19.98 kB / 0.8617 GB, free: 6.555 MB / 0.6856 GB
Notification: Performance of postOpt findZeroCrossings (simulation): time 8.883e-05/2.514, allocations: 29.16 kB / 0.8618 GB, free: 6.527 MB / 0.6856 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.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

Variables:
1: plateHeatExchanger.profe.ddhp:VARIABLE(unit = "kg.s2/m5" )  "Derivative of density wrt. specific enthalpy at constant pressure" type: Real
2: plateHeatExchanger.profe.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 )  "Specific inner energy" type: Real
3: plateHeatExchanger.profe.x:VARIABLE(min = 0.0 max = 1.0 unit = "1" )  "Vapor mass fraction" type: Real
4: plateHeatExchanger.profe.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific heat capacity at constant presure" type: Real
5: plateHeatExchanger.profe.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific entropy" type: Real
6: plateHeatExchanger.profs.ddhp:VARIABLE(unit = "kg.s2/m5" )  "Derivative of density wrt. specific enthalpy at constant pressure" type: Real
7: 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
8: plateHeatExchanger.profs.duhp:VARIABLE(unit = "1" )  "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real
9: plateHeatExchanger.profs.x:VARIABLE(min = 0.0 max = 1.0 unit = "1" )  "Vapor mass fraction" type: Real
10: 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/DAEMode.mo:528:7-530:90:writable] Error: Internal error DAEMode.traverserStrongComponents failed on equation:
1/1 (1): sourceP3.C.h = if puitsP3.Q > 0.0 then sourceP3.h else puitsP3.h
2/2 (10): $cse2 = ThermoSysPro.Properties.Fluid.Ph(sourceP3.P0, sourceP3.C.h, plateHeatExchanger.mode_f, plateHeatExchanger.fluid_c)
3/12 (1): 0.0 = if abs(puitsP3.Q) > 0.001 then plateHeatExchanger.W - puitsP3.Q * plateHeatExchanger.prof.cp * (plateHeatExchanger.Tsf - plateHeatExchanger.Tef) else plateHeatExchanger.Tef - plateHeatExchanger.Tsf
4/13 (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
5/14 (1): plateHeatExchanger.K = plateHeatExchanger.hc * plateHeatExchanger.hf / (plateHeatExchanger.hc + plateHeatExchanger.hf + plateHeatExchanger.hc * plateHeatExchanger.hf * plateHeatExchanger.emetal / plateHeatExchanger.lambdam)
6/15 (1): plateHeatExchanger.W = plateHeatExchanger.K * plateHeatExchanger.S * plateHeatExchanger.DTm
7/16 (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)
8/17 (1): plateHeatExchanger.DT2 = plateHeatExchanger.Tsc - plateHeatExchanger.Tef
9/18 (1): 0.0 = if abs(puitsP2.Q) > 0.001 then plateHeatExchanger.W - puitsP2.Q * plateHeatExchanger.proc.cp * (plateHeatExchanger.Tec - plateHeatExchanger.Tsc) else plateHeatExchanger.Tec - plateHeatExchanger.Tsc
10/19 (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
11/29 (10): $cse3 = ThermoSysPro.Properties.Fluid.Ph(puitsP2.P0, plateHeatExchanger.Sc.h, plateHeatExchanger.mode_c, plateHeatExchanger.fluid_f)
12/39 (1): plateHeatExchanger.Hmc = 0.5 * (sourceP2.C.h + plateHeatExchanger.Sc.h)
13/40 (10): $cse6 = ThermoSysPro.Properties.Fluid.Ph(plateHeatExchanger.Pmc, plateHeatExchanger.Hmc, plateHeatExchanger.mode_c, plateHeatExchanger.fluid_c)
14/50 (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
15/51 (1): plateHeatExchanger.lambdac = ThermoSysPro.Properties.Fluid.ThermalConductivity_rhoT(plateHeatExchanger.rhoc, plateHeatExchanger.Tmc, plateHeatExchanger.Pmc, 0, plateHeatExchanger.fluid_c)
16/52 (1): plateHeatExchanger.muc = ThermoSysPro.Properties.Fluid.DynamicViscosity_rhoT(plateHeatExchanger.rhoc, plateHeatExchanger.Tmc, plateHeatExchanger.fluid_c)
17/53 (1): plateHeatExchanger.qmc = abs(puitsP2.Q) / (plateHeatExchanger.muc * plateHeatExchanger.N)
18/54 (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)
19/55 (1): plateHeatExchanger.quc = abs(puitsP2.Q) / plateHeatExchanger.N
20/56 (1): puitsP2.P0 = if puitsP2.Q > 0.0 then sourceP2.P0 - plateHeatExchanger.DPc else sourceP2.P0 + plateHeatExchanger.DPc
21/57 (1): sourceP2.C.h = if puitsP2.Q > 0.0 then sourceP2.h else puitsP2.h
22/58 (10): $cse4 = ThermoSysPro.Properties.Fluid.Ph(sourceP2.P0, sourceP2.C.h, plateHeatExchanger.mode_c, plateHeatExchanger.fluid_c)
23/68 (1): plateHeatExchanger.DT1 = plateHeatExchanger.Tec - plateHeatExchanger.Tsf
24/69 (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
25/79 (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
26/89 (1): plateHeatExchanger.lambdaf = ThermoSysPro.Properties.Fluid.ThermalConductivity_rhoT(plateHeatExchanger.rhof, plateHeatExchanger.Tmf, plateHeatExchanger.Pmf, 0, plateHeatExchanger.fluid_f)
27/90 (1): plateHeatExchanger.muf = ThermoSysPro.Properties.Fluid.DynamicViscosity_rhoT(plateHeatExchanger.rhof, plateHeatExchanger.Tmf, plateHeatExchanger.fluid_f)
28/91 (1): plateHeatExchanger.qmf = abs(puitsP3.Q) / (plateHeatExchanger.muf * plateHeatExchanger.N)
29/92 (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)
30/93 (1): plateHeatExchanger.quf = abs(puitsP3.Q) / plateHeatExchanger.N
31/94 (1): puitsP3.P0 = if puitsP3.Q > 0.0 then sourceP3.P0 - plateHeatExchanger.DPf else sourceP3.P0 + plateHeatExchanger.DPf
32/95 (10): $cse5 = ThermoSysPro.Properties.Fluid.Ph(plateHeatExchanger.Pmf, plateHeatExchanger.Hmf, plateHeatExchanger.mode_f, plateHeatExchanger.fluid_f)
33/105 (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
34/115 (1): plateHeatExchanger.Hmf = 0.5 * (sourceP3.C.h + plateHeatExchanger.Sf.h)
35/116 (10): $cse1 = ThermoSysPro.Properties.Fluid.Ph(puitsP3.P0, plateHeatExchanger.Sf.h, plateHeatExchanger.mode_f, plateHeatExchanger.fluid_f)
36/126 (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
37/136 (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

Variables:
1: plateHeatExchanger.profe.ddhp:VARIABLE(unit = "kg.s2/m5" )  "Derivative of density wrt. specific enthalpy at constant pressure" type: Real
2: plateHeatExchanger.profe.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 )  "Specific inner energy" type: Real
3: plateHeatExchanger.profe.x:VARIABLE(min = 0.0 max = 1.0 unit = "1" )  "Vapor mass fraction" type: Real
4: plateHeatExchanger.profe.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific heat capacity at constant presure" type: Real
5: plateHeatExchanger.profe.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific entropy" type: Real
6: plateHeatExchanger.profs.ddhp:VARIABLE(unit = "kg.s2/m5" )  "Derivative of density wrt. specific enthalpy at constant pressure" type: Real
7: 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
8: plateHeatExchanger.profs.duhp:VARIABLE(unit = "1" )  "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real
9: plateHeatExchanger.profs.x:VARIABLE(min = 0.0 max = 1.0 unit = "1" )  "Vapor mass fraction" type: Real
10: plateHeatExchanger.profs.duph:VARIABLE(unit = "m3/kg" )  "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real
11: plateHeatExchanger.profs.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific entropy" type: Real
12: plateHeatExchanger.profs.ddph:VARIABLE(unit = "s2/m2" )  "Derivative of density wrt. pressure at constant specific enthalpy" type: Real
13: plateHeatExchanger.profs.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 )  "Specific inner energy" type: Real
14: plateHeatExchanger.profs.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific heat capacity at constant presure" type: Real
15: plateHeatExchanger.profs.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 )  "Density" type: Real
16: $cse1.T:VARIABLE(protected = true )  type: Real unreplaceable
17: $cse1.d:VARIABLE(protected = true )  type: Real unreplaceable
18: $cse1.s:VARIABLE(protected = true )  type: Real unreplaceable
19: $cse1.duhp:VARIABLE(protected = true )  type: Real unreplaceable
20: $cse1.ddhp:VARIABLE(protected = true )  type: Real unreplaceable
21: $cse1.u:VARIABLE(protected = true )  type: Real unreplaceable
22: $cse1.cp:VARIABLE(protected = true )  type: Real unreplaceable
23: $cse1.ddph:VARIABLE(protected = true )  type: Real unreplaceable
24: $cse1.duph:VARIABLE(protected = true )  type: Real unreplaceable
25: $cse1.x:VARIABLE(protected = true )  type: Real unreplaceable
26: 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
27: plateHeatExchanger.prof.ddhp:VARIABLE(unit = "kg.s2/m5" )  "Derivative of density wrt. specific enthalpy at constant pressure" type: Real
28: plateHeatExchanger.prof.duhp:VARIABLE(unit = "1" )  "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real
29: plateHeatExchanger.prof.ddph:VARIABLE(unit = "s2/m2" )  "Derivative of density wrt. pressure at constant specific enthalpy" type: Real
30: plateHeatExchanger.prof.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific entropy" type: Real
31: plateHeatExchanger.Tmf:VARIABLE(min = 200.0 max = 6000.0 start = 290.0 unit = "K" nominal = 300.0 )  "Cold fluid average temperature" type: Real
32: $cse5.duph:VARIABLE(protected = true )  type: Real unreplaceable
33: $cse5.s:VARIABLE(protected = true )  type: Real unreplaceable
34: plateHeatExchanger.Hmf:VARIABLE(start = 1e5 unit = "J/kg" )  "Cold fluid average specific enthalpy" type: Real
35: $cse5.d:VARIABLE(protected = true )  type: Real unreplaceable
36: $cse5.u:VARIABLE(protected = true )  type: Real unreplaceable
37: $cse5.T:VARIABLE(protected = true )  type: Real unreplaceable
38: $cse5.ddhp:VARIABLE(protected = true )  type: Real unreplaceable
39: $cse5.duhp:VARIABLE(protected = true )  type: Real unreplaceable
40: $cse5.cp:VARIABLE(protected = true )  type: Real unreplaceable
41: $cse5.ddph:VARIABLE(protected = true )  type: Real unreplaceable
42: $cse5.x:VARIABLE(protected = true )  type: Real unreplaceable
43: plateHeatExchanger.prof.duph:VARIABLE(unit = "m3/kg" )  "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real
44: plateHeatExchanger.prof.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 )  "Specific inner energy" type: Real
45: plateHeatExchanger.prof.x:VARIABLE(min = 0.0 max = 1.0 unit = "1" )  "Vapor mass fraction" type: Real
46: plateHeatExchanger.DPf:VARIABLE(unit = "Pa" )  "Pressure loss of the cold fluid" type: Real
47: puitsP3.Q:VARIABLE(start = 500.0 unit = "kg/s" )  "Fluid mass flow rate" type: Real
48: plateHeatExchanger.quf:VARIABLE()  type: Real
49: plateHeatExchanger.qmf:VARIABLE()  type: Real
50: plateHeatExchanger.muf:VARIABLE(min = 0.0 start = 0.001 unit = "Pa.s" )  "Cold fluid dynamic viscosity" type: Real
51: plateHeatExchanger.lambdaf:VARIABLE(start = 0.597928 unit = "W/(m.K)" )  "Cold fluid thermal conductivity" type: Real
52: plateHeatExchanger.rhof:VARIABLE(min = 1e-9 max = 1e5 start = 998.0 unit = "kg/m3" nominal = 998.0 )  "Cold fluid density" type: Real
53: plateHeatExchanger.rhoc:VARIABLE(min = 1e-9 max = 1e5 start = 998.0 unit = "kg/m3" nominal = 998.0 )  "Hot fluid density" type: Real
54: plateHeatExchanger.proce.duph:VARIABLE(unit = "m3/kg" )  "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real
55: plateHeatExchanger.proce.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 )  "Specific inner energy" type: Real
56: plateHeatExchanger.proce.ddhp:VARIABLE(unit = "kg.s2/m5" )  "Derivative of density wrt. specific enthalpy at constant pressure" type: Real
57: plateHeatExchanger.proce.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific heat capacity at constant presure" type: Real
58: plateHeatExchanger.proce.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 )  "Density" type: Real
59: plateHeatExchanger.proce.duhp:VARIABLE(unit = "1" )  "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real
60: plateHeatExchanger.proce.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific entropy" type: Real
61: plateHeatExchanger.proce.ddph:VARIABLE(unit = "s2/m2" )  "Derivative of density wrt. pressure at constant specific enthalpy" type: Real
62: plateHeatExchanger.proce.x:VARIABLE(min = 0.0 max = 1.0 unit = "1" )  "Vapor mass fraction" type: Real
63: plateHeatExchanger.DT1:VARIABLE(unit = "K" )  "Temperature difference at the inlet of the exchanger" type: Real
64: 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
65: $cse4.duhp:VARIABLE(protected = true )  type: Real unreplaceable
66: $cse4.u:VARIABLE(protected = true )  type: Real unreplaceable
67: $cse4.d:VARIABLE(protected = true )  type: Real unreplaceable
68: $cse4.ddph:VARIABLE(protected = true )  type: Real unreplaceable
69: $cse4.duph:VARIABLE(protected = true )  type: Real unreplaceable
70: $cse4.ddhp:VARIABLE(protected = true )  type: Real unreplaceable
71: $cse4.s:VARIABLE(protected = true )  type: Real unreplaceable
72: $cse4.cp:VARIABLE(protected = true )  type: Real unreplaceable
73: $cse4.T:VARIABLE(protected = true )  type: Real unreplaceable
74: $cse4.x:VARIABLE(protected = true )  type: Real unreplaceable
75: 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
76: plateHeatExchanger.DPc:VARIABLE(unit = "Pa" )  "Pressure loss of the hot fluid" type: Real
77: puitsP2.Q:VARIABLE(start = 500.0 unit = "kg/s" )  "Fluid mass flow rate" type: Real
78: plateHeatExchanger.quc:VARIABLE()  type: Real
79: plateHeatExchanger.qmc:VARIABLE()  type: Real
80: plateHeatExchanger.muc:VARIABLE(min = 0.0 start = 0.001 unit = "Pa.s" )  "Hot fluid dynamic viscosity" type: Real
81: plateHeatExchanger.lambdac:VARIABLE(start = 0.602698 unit = "W/(m.K)" )  "Hot fluid thermal conductivity" type: Real
82: plateHeatExchanger.Tmc:VARIABLE(min = 200.0 max = 6000.0 start = 290.0 unit = "K" nominal = 300.0 )  "Hot fluid average temperature" type: Real
83: plateHeatExchanger.proc.duph:VARIABLE(unit = "m3/kg" )  "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real
84: plateHeatExchanger.proc.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 )  "Specific inner energy" type: Real
85: plateHeatExchanger.proc.ddhp:VARIABLE(unit = "kg.s2/m5" )  "Derivative of density wrt. specific enthalpy at constant pressure" type: Real
86: plateHeatExchanger.proc.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific entropy" type: Real
87: plateHeatExchanger.proc.x:VARIABLE(min = 0.0 max = 1.0 unit = "1" )  "Vapor mass fraction" type: Real
88: plateHeatExchanger.proc.duhp:VARIABLE(unit = "1" )  "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real
89: plateHeatExchanger.proc.ddph:VARIABLE(unit = "s2/m2" )  "Derivative of density wrt. pressure at constant specific enthalpy" type: Real
90: plateHeatExchanger.hc:VARIABLE(unit = "W/(m2.K)" )  "Heat transfer coefficient of the hot fluid" type: Real
91: plateHeatExchanger.proc.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific heat capacity at constant presure" type: Real
92: $cse6.cp:VARIABLE(protected = true )  type: Real unreplaceable
93: $cse6.u:VARIABLE(protected = true )  type: Real unreplaceable
94: $cse6.s:VARIABLE(protected = true )  type: Real unreplaceable
95: $cse6.x:VARIABLE(protected = true )  type: Real unreplaceable
96: $cse6.ddph:VARIABLE(protected = true )  type: Real unreplaceable
97: $cse6.d:VARIABLE(protected = true )  type: Real unreplaceable
98: $cse6.duhp:VARIABLE(protected = true )  type: Real unreplaceable
99: $cse6.duph:VARIABLE(protected = true )  type: Real unreplaceable
100: $cse6.ddhp:VARIABLE(protected = true )  type: Real unreplaceable
101: $cse6.T:VARIABLE(protected = true )  type: Real unreplaceable
102: plateHeatExchanger.Hmc:VARIABLE(start = 1e5 unit = "J/kg" )  "Hot fluid average specific enthalpy" type: Real
103: $cse3.ddhp:VARIABLE(protected = true )  type: Real unreplaceable
104: $cse3.duph:VARIABLE(protected = true )  type: Real unreplaceable
105: $cse3.s:VARIABLE(protected = true )  type: Real unreplaceable
106: $cse3.duhp:VARIABLE(protected = true )  type: Real unreplaceable
107: 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
108: $cse3.d:VARIABLE(protected = true )  type: Real unreplaceable
109: $cse3.cp:VARIABLE(protected = true )  type: Real unreplaceable
110: $cse3.u:VARIABLE(protected = true )  type: Real unreplaceable
111: $cse3.ddph:VARIABLE(protected = true )  type: Real unreplaceable
112: $cse3.T:VARIABLE(protected = true )  type: Real unreplaceable
113: $cse3.x:VARIABLE(protected = true )  type: Real unreplaceable
114: plateHeatExchanger.procs.x:VARIABLE(min = 0.0 max = 1.0 unit = "1" )  "Vapor mass fraction" type: Real
115: plateHeatExchanger.procs.duhp:VARIABLE(unit = "1" )  "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real
116: plateHeatExchanger.procs.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 )  "Specific inner energy" type: Real
117: plateHeatExchanger.procs.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific heat capacity at constant presure" type: Real
118: plateHeatExchanger.procs.ddhp:VARIABLE(unit = "kg.s2/m5" )  "Derivative of density wrt. specific enthalpy at constant pressure" type: Real
119: plateHeatExchanger.procs.duph:VARIABLE(unit = "m3/kg" )  "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real
120: plateHeatExchanger.procs.ddph:VARIABLE(unit = "s2/m2" )  "Derivative of density wrt. pressure at constant specific enthalpy" type: Real
121: plateHeatExchanger.procs.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific entropy" type: Real
122: plateHeatExchanger.procs.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 )  "Density" type: Real
123: plateHeatExchanger.W:VARIABLE(unit = "W" )  "Thermal power exchanged between the two sides" type: Real
124: 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
125: plateHeatExchanger.DT2:VARIABLE(unit = "K" )  "Temperature difference at the outlet of the exchanger" type: Real
126: plateHeatExchanger.DTm:VARIABLE(unit = "K" )  "Difference in average temperature" type: Real
127: plateHeatExchanger.K:VARIABLE(unit = "W/(m2.K)" )  "Global heat transfer coefficient" type: Real
128: plateHeatExchanger.hf:VARIABLE(unit = "W/(m2.K)" )  "Heat transfer coefficient of the cold fluid" type: Real
129: plateHeatExchanger.prof.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific heat capacity at constant presure" type: Real
130: 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
131: plateHeatExchanger.profe.ddph:VARIABLE(unit = "s2/m2" )  "Derivative of density wrt. pressure at constant specific enthalpy" type: Real
132: plateHeatExchanger.profe.duph:VARIABLE(unit = "m3/kg" )  "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real
133: plateHeatExchanger.profe.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 )  "Density" type: Real
134: plateHeatExchanger.profe.duhp:VARIABLE(unit = "1" )  "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real
135: $cse2.d:VARIABLE(protected = true )  type: Real unreplaceable
136: $cse2.x:VARIABLE(protected = true )  type: Real unreplaceable
137: $cse2.duhp:VARIABLE(protected = true )  type: Real unreplaceable
138: $cse2.cp:VARIABLE(protected = true )  type: Real unreplaceable
139: $cse2.ddhp:VARIABLE(protected = true )  type: Real unreplaceable
140: $cse2.u:VARIABLE(protected = true )  type: Real unreplaceable
141: $cse2.ddph:VARIABLE(protected = true )  type: Real unreplaceable
142: $cse2.s:VARIABLE(protected = true )  type: Real unreplaceable
143: $cse2.duph:VARIABLE(protected = true )  type: Real unreplaceable
144: $cse2.T:VARIABLE(protected = true )  type: Real unreplaceable
145: 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
[/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 0.004099/2.518, allocations: 6.561 MB / 0.8682 GB, free: 14.74 MB / 0.7012 GB
Error: post-optimization module createDAEmodeBDAE (simulation) failed.
Error: Internal error SimCode DAEmode: The model ThermoSysPro.Fluid.Examples.SimpleExamples.TestStaticPlateHeatExchanger could not be translated