Running: ./testmodel.py --libraries=/home/hudson/saved_omc/libraries/.openmodelica/libraries --ompython_omhome=/usr ThermoSysPro_ThermoSysPro.Examples.SimpleExamples.TestDynamicWaterWaterExchanger.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.TestDynamicWaterWaterExchanger,tolerance=1e-06,outputFormat="empty",numberOfIntervals=5000,variableFilter="",fileNamePrefix="ThermoSysPro_ThermoSysPro.Examples.SimpleExamples.TestDynamicWaterWaterExchanger")
translateModel(ThermoSysPro.Examples.SimpleExamples.TestDynamicWaterWaterExchanger,tolerance=1e-06,outputFormat="empty",numberOfIntervals=5000,variableFilter="",fileNamePrefix="ThermoSysPro_ThermoSysPro.Examples.SimpleExamples.TestDynamicWaterWaterExchanger")
Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermoSysPro 4.0.0-master/package.mo): time 0.8262/0.8262, allocations: 150.9 MB / 167.2 MB, free: 14.52 MB / 142.1 MB
Notification: Performance of FrontEnd - loaded program: time 0.0003539/0.0003539, allocations: 20.72 kB / 237.8 MB, free: 1.734 MB / 190.1 MB
Notification: Performance of FrontEnd - Absyn->SCode: time 0.05591/0.05628, allocations: 31.35 MB / 269.1 MB, free: 7.035 MB / 222.1 MB
Notification: Automatically loaded package Complex 4.0.0 due to uses annotation from Modelica.
Notification: Automatically loaded package ModelicaServices 4.0.0 due to uses annotation from Modelica.
Notification: Automatically loaded package Modelica 4.0.0 due to usage.
Notification: Performance of NFInst.instantiate(ThermoSysPro.Examples.SimpleExamples.TestDynamicWaterWaterExchanger): time 1.66/1.716, allocations: 296.4 MB / 0.5522 GB, free: 11.45 MB / 446.1 MB
Notification: Performance of NFInst.instExpressions: time 0.02689/1.743, allocations: 23.09 MB / 0.5748 GB, free: 4.27 MB / 462.1 MB
Notification: Performance of NFInst.updateImplicitVariability: time 0.0003871/1.744, allocations: 8 kB / 0.5748 GB, free: 4.262 MB / 462.1 MB
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermoSysPro 4.0.0-master/WaterSteam/HeatExchangers/DynamicWaterWaterExchanger.mo:117:3-118:48: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/DynamicWaterWaterExchanger.mo:119:3-120:48: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/DynamicWaterWaterExchanger.mo:121:3-122:46: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/DynamicWaterWaterExchanger.mo:123:3-124:46: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 0.0005512/1.744, allocations: 200.9 kB / 0.575 GB, free: 4.066 MB / 462.1 MB
Notification: Performance of NFTyping.typeBindings: time 0.0006647/1.745, allocations: 357.6 kB / 0.5753 GB, free: 3.715 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 0.01718/1.762, allocations: 7.292 MB / 0.5824 GB, free: 12.42 MB / 478.1 MB
Notification: Performance of NFFlatten.flatten: time 0.002762/1.765, allocations: 2.545 MB / 0.5849 GB, free: 9.867 MB / 478.1 MB
Notification: Performance of NFFlatten.resolveConnections: time 0.0008905/1.766, allocations: 0.6805 MB / 0.5856 GB, free: 9.176 MB / 478.1 MB
Notification: Performance of NFEvalConstants.evaluate: time 0.001154/1.767, allocations: 0.8766 MB / 0.5864 GB, free: 8.297 MB / 478.1 MB
Notification: Performance of NFSimplifyModel.simplify: time 0.001139/1.768, allocations: 0.8607 MB / 0.5873 GB, free: 7.434 MB / 478.1 MB
Notification: Performance of NFPackage.collectConstants: time 0.0002243/1.768, allocations: 120 kB / 0.5874 GB, free: 7.316 MB / 478.1 MB
Notification: Performance of NFFlatten.collectFunctions: time 0.02794/1.796, allocations: 15.45 MB / 0.6025 GB, free: 7.852 MB / 494.1 MB
Notification: Performance of NFScalarize.scalarize: time 0.0007609/1.797, allocations: 486.6 kB / 0.6029 GB, free: 7.375 MB / 494.1 MB
Notification: Performance of NFVerifyModel.verify: time 0.001113/1.798, allocations: 0.7505 MB / 0.6037 GB, free: 6.621 MB / 494.1 MB
Notification: Performance of NFConvertDAE.convert: time 0.01861/1.817, allocations: 7.904 MB / 0.6114 GB, free: 14.7 MB / 0.4981 GB
Notification: Performance of FrontEnd - DAE generated: time 7.073e-06/1.817, allocations: 0 / 0.6114 GB, free: 14.7 MB / 0.4981 GB
Notification: Performance of FrontEnd: time 1.864e-06/1.817, allocations: 0 / 0.6114 GB, free: 14.7 MB / 0.4981 GB
Notification: Performance of Transformations before backend: time 1.971e-05/1.817, allocations: 4 kB / 0.6114 GB, free: 14.7 MB / 0.4981 GB
Notification: Model statistics after passing the front-end and creating the data structures used by the back-end:
 * Number of equations: 418
 * Number of variables: 418
Notification: Performance of Generate backend data structure: time 0.007781/1.825, allocations: 2.299 MB / 0.6136 GB, free: 12.34 MB / 0.4981 GB
Notification: Performance of prepare preOptimizeDAE: time 5.949e-05/1.825, allocations: 8.031 kB / 0.6137 GB, free: 12.33 MB / 0.4981 GB
Notification: Performance of preOpt normalInlineFunction (simulation): time 0.0002807/1.825, allocations: 135.2 kB / 0.6138 GB, free: 12.2 MB / 0.4981 GB
Notification: Performance of preOpt evaluateParameters (simulation): time 0.0009078/1.826, allocations: 0.577 MB / 0.6144 GB, free: 11.58 MB / 0.4981 GB
Notification: Performance of preOpt simplifyIfEquations (simulation): time 0.0001061/1.826, allocations: 97.98 kB / 0.6144 GB, free: 11.48 MB / 0.4981 GB
Notification: Performance of preOpt expandDerOperator (simulation): time 0.0001981/1.826, allocations: 107.9 kB / 0.6145 GB, free: 11.38 MB / 0.4981 GB
Notification: Performance of preOpt clockPartitioning (simulation): time 0.002989/1.829, allocations: 1.966 MB / 0.6165 GB, free: 9.344 MB / 0.4981 GB
Notification: Performance of preOpt findStateOrder (simulation): time 2.453e-05/1.829, allocations: 3.938 kB / 0.6165 GB, free: 9.34 MB / 0.4981 GB
Notification: Performance of preOpt replaceEdgeChange (simulation): time 0.0001175/1.83, allocations: 40 kB / 0.6165 GB, free: 9.301 MB / 0.4981 GB
Notification: Performance of preOpt inlineArrayEqn (simulation): time 5.401e-05/1.83, allocations: 71.94 kB / 0.6166 GB, free: 9.23 MB / 0.4981 GB
Notification: Performance of preOpt removeEqualRHS (simulation): time 0.003154/1.833, allocations: 1.91 MB / 0.6184 GB, free: 7.316 MB / 0.4981 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 0.07762/1.91, allocations: 39.74 MB / 0.6573 GB, free: 11.67 MB / 0.545 GB
Notification: Performance of preOpt comSubExp (simulation): time 0.002492/1.913, allocations: 1.708 MB / 0.6589 GB, free: 9.957 MB / 0.545 GB
Notification: Performance of preOpt resolveLoops (simulation): time 0.001725/1.915, allocations: 1.197 MB / 0.6601 GB, free: 8.754 MB / 0.545 GB
Notification: Performance of preOpt evalFunc (simulation): time 0.07263/1.987, allocations: 33.84 MB / 0.6931 GB, free: 3.613 MB / 0.5762 GB
Notification: Performance of preOpt encapsulateWhenConditions (simulation): time 3.795e-05/1.987, allocations: 47.86 kB / 0.6932 GB, free: 3.559 MB / 0.5762 GB
Notification: Performance of pre-optimization done (n=292): time 4.458e-06/1.987, allocations: 8 kB / 0.6932 GB, free: 3.551 MB / 0.5762 GB
Notification: Performance of matching and sorting (n=292): time 0.03249/2.02, allocations: 7.31 MB / 0.7003 GB, free: 12.11 MB / 0.5919 GB
Notification: Performance of inlineWhenForInitialization (initialization): time 3.873e-05/2.02, allocations: 64.72 kB / 0.7004 GB, free: 12.04 MB / 0.5919 GB
Notification: Performance of selectInitializationVariablesDAE (initialization): time 0.0004382/2.02, allocations: 365.4 kB / 0.7007 GB, free: 11.67 MB / 0.5919 GB
Notification: Performance of collectPreVariables (initialization): time 0.000106/2.021, allocations: 49.7 kB / 0.7008 GB, free: 11.61 MB / 0.5919 GB
Notification: Performance of collectInitialEqns (initialization): time 0.0001783/2.021, allocations: 275.8 kB / 0.701 GB, free: 11.34 MB / 0.5919 GB
Notification: Performance of collectInitialBindings (initialization): time 0.0007627/2.021, allocations: 0.9504 MB / 0.702 GB, free: 10.37 MB / 0.5919 GB
Notification: Performance of simplifyInitialFunctions (initialization): time 0.0005003/2.022, allocations: 335.9 kB / 0.7023 GB, free: 10.04 MB / 0.5919 GB
Notification: Performance of setup shared object (initialization): time 0.0001158/2.022, allocations: 330 kB / 0.7026 GB, free: 9.707 MB / 0.5919 GB
Notification: Performance of preBalanceInitialSystem (initialization): time 0.001721/2.024, allocations: 1.03 MB / 0.7036 GB, free: 8.676 MB / 0.5919 GB
Notification: Performance of partitionIndependentBlocks (initialization): time 0.001872/2.026, allocations: 1.204 MB / 0.7048 GB, free: 7.441 MB / 0.5919 GB
Notification: Performance of analyzeInitialSystem (initialization): time 0.003913/2.03, allocations: 2.46 MB / 0.7072 GB, free: 4.93 MB / 0.5919 GB
Notification: Performance of solveInitialSystemEqSystem (initialization): time 6.783e-06/2.03, allocations: 0 / 0.7072 GB, free: 4.93 MB / 0.5919 GB
Notification: Performance of matching and sorting (n=316) (initialization): time 0.006433/2.036, allocations: 3.741 MB / 0.7109 GB, free: 1.148 MB / 0.5919 GB
Notification: Performance of prepare postOptimizeDAE: time 2.493e-05/2.036, allocations: 7.938 kB / 0.7109 GB, free: 1.141 MB / 0.5919 GB
Notification: Performance of postOpt simplifyComplexFunction (initialization): time 1.514e-05/2.036, allocations: 4 kB / 0.7109 GB, free: 1.137 MB / 0.5919 GB
Notification: Performance of postOpt tearingSystem (initialization): time 0.2065/2.243, allocations: 4.823 MB / 0.7156 GB, free: 214.2 MB / 0.5919 GB
Notification: Performance of postOpt solveSimpleEquations (initialization): time 0.0001458/2.243, allocations: 39.48 kB / 0.7156 GB, free: 214.2 MB / 0.5919 GB
Notification: Performance of postOpt calculateStrongComponentJacobians (initialization): time 0.007748/2.251, allocations: 4.895 MB / 0.7204 GB, free: 213.7 MB / 0.5919 GB
Notification: Performance of postOpt simplifyAllExpressions (initialization): time 0.001044/2.252, allocations: 195.6 kB / 0.7206 GB, free: 213.6 MB / 0.5919 GB
Notification: Performance of postOpt collapseArrayExpressions (initialization): time 0.0001172/2.252, allocations: 61.83 kB / 0.7206 GB, free: 213.6 MB / 0.5919 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 (puitsP1.C.a,puitsP.C.a,sourceP1.C.b,sourceP.C.b,echangeurAPlaques1D.Sc.b,echangeurAPlaques1D.Sf.b,echangeurAPlaques1D.Ef.a,echangeurAPlaques1D.Ec.a)
 * Number of discrete states: 0 ()
 * Number of clocked states: 0 ()
 * Top-level inputs: 0
Notification: Strong component statistics for initialization (33):
 * Single equations (assignments): 24
 * Array equations: 0
 * Algorithm blocks: 0
 * Record equations: 8
 * 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
   {(22,100)}
Notification: Performance of prepare postOptimizeDAE: time 0.0005144/2.252, allocations: 362.5 kB / 0.721 GB, free: 213.5 MB / 0.5919 GB
Notification: Performance of postOpt lateInlineFunction (simulation): time 0.0001964/2.252, allocations: 102.6 kB / 0.7211 GB, free: 213.5 MB / 0.5919 GB
Notification: Performance of postOpt wrapFunctionCalls (simulation): time 0.01001/2.262, allocations: 10.91 MB / 0.7317 GB, free: 212.7 MB / 0.5919 GB
Notification: Performance of postOpt simplifysemiLinear (simulation): time 1.59e-05/2.263, allocations: 10.39 kB / 0.7317 GB, free: 212.7 MB / 0.5919 GB
Notification: Performance of postOpt simplifyComplexFunction (simulation): time 6.522e-06/2.263, allocations: 0 / 0.7317 GB, free: 212.7 MB / 0.5919 GB
Notification: Performance of postOpt removeConstants (simulation): time 0.0002335/2.263, allocations: 267.3 kB / 0.732 GB, free: 212.4 MB / 0.5919 GB
Notification: Performance of postOpt simplifyTimeIndepFuncCalls (simulation): time 0.000195/2.263, allocations: 45.22 kB / 0.732 GB, free: 212.4 MB / 0.5919 GB
Notification: Performance of postOpt simplifyAllExpressions (simulation): time 0.0009229/2.264, allocations: 55.08 kB / 0.7321 GB, free: 212.4 MB / 0.5919 GB
Notification: Performance of postOpt findZeroCrossings (simulation): time 0.0002477/2.264, allocations: 116.5 kB / 0.7322 GB, free: 212.4 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(echangeurAPlaques1D.Tmc[4], echangeurAPlaques1D.rhoc[4], echangeurAPlaques1D.proc[4].u, echangeurAPlaques1D.proc[4].s, echangeurAPlaques1D.proc[4].cp, echangeurAPlaques1D.proc[4].ddhp, echangeurAPlaques1D.proc[4].ddph, echangeurAPlaques1D.proc[4].duph, echangeurAPlaques1D.proc[4].duhp, echangeurAPlaques1D.proc[4].x) = $cse10

Variables:
1: echangeurAPlaques1D.proc[4].duhp:VARIABLE(unit = "1" )  "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real [5]
2: echangeurAPlaques1D.proc[4].ddph:VARIABLE(unit = "s2/m2" )  "Derivative of density wrt. pressure at constant specific enthalpy" type: Real [5]
3: echangeurAPlaques1D.proc[4].s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific entropy" type: Real [5]
4: echangeurAPlaques1D.proc[4].u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 )  "Specific inner energy" type: Real [5]
5: echangeurAPlaques1D.rhoc[4]:VARIABLE(min = 1e-9 max = 1e5 start = 998.0 unit = "kg/m3" nominal = 998.0 )  "Hot fluid density" type: Real [5]
6: echangeurAPlaques1D.proc[4].ddhp:VARIABLE(unit = "kg.s2/m5" )  "Derivative of density wrt. specific enthalpy at constant pressure" type: Real [5]
7: echangeurAPlaques1D.proc[4].cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific heat capacity at constant presure" type: Real [5]
8: echangeurAPlaques1D.proc[4].x:VARIABLE(min = 0.0 max = 1.0 unit = "1" )  "Vapor mass fraction" type: Real [5]
9: echangeurAPlaques1D.proc[4].duph:VARIABLE(unit = "m3/kg" )  "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real [5]
10: $cse12: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): echangeurAPlaques1D.muc[5] = ThermoSysPro.Properties.WaterSteam.IF97.DynamicViscosity_rhoT(echangeurAPlaques1D.rhoc[5], echangeurAPlaques1D.Tmc[5])
2/2 (1): $cse8 = max(1e-9, echangeurAPlaques1D.muc[5])
3/3 (1): echangeurAPlaques1D.qmc[5] = abs(echangeurAPlaques1D.Qcc[6]) / ($cse8 * echangeurAPlaques1D.M)
4/4 (1): echangeurAPlaques1D.DPc[5] = if noEvent(echangeurAPlaques1D.qmc[5] < 0.001) then 0.0 else echangeurAPlaques1D.c1 * 14423.2 / (echangeurAPlaques1D.rhoc[5] * abs(echangeurAPlaques1D.qmc[5]) ^ 0.097) * echangeurAPlaques1D.quc[5] ^ 2.0 * (1472.47 + 0.77 * (echangeurAPlaques1D.M - 1.0) + 104.97 / abs(echangeurAPlaques1D.qmc[5]) ^ 0.25)
5/5 (10): $cse6 = ThermoSysPro.Properties.WaterSteam.IF97.Water_Ph(echangeurAPlaques1D.Pmc[5], echangeurAPlaques1D.Hmc[5], echangeurAPlaques1D.modec)
6/15 (10): ThermoSysPro.Properties.WaterSteam.Common.ThermoProperties_ph(echangeurAPlaques1D.Tmc[5], echangeurAPlaques1D.rhoc[5], echangeurAPlaques1D.proc[5].u, echangeurAPlaques1D.proc[5].s, echangeurAPlaques1D.proc[5].cp, echangeurAPlaques1D.proc[5].ddhp, echangeurAPlaques1D.proc[5].ddph, echangeurAPlaques1D.proc[5].duph, echangeurAPlaques1D.proc[5].duhp, echangeurAPlaques1D.proc[5].x) = $cse6
7/25 (1): echangeurAPlaques1D.Pmc[5] = 0.5 * (echangeurAPlaques1D.Pcc[5] + puitsP.P0)
8/26 (1): echangeurAPlaques1D.Pcc[5] = if echangeurAPlaques1D.Qcc[6] > 0.0 then echangeurAPlaques1D.Pcc[4] - 0.2 * echangeurAPlaques1D.DPc[4] else echangeurAPlaques1D.Pcc[4] + 0.2 * echangeurAPlaques1D.DPc[4]
9/27 (1): echangeurAPlaques1D.Pcc[4] = if echangeurAPlaques1D.Qcc[6] > 0.0 then echangeurAPlaques1D.Pcc[3] - 0.2 * echangeurAPlaques1D.DPc[3] else echangeurAPlaques1D.Pcc[3] + 0.2 * echangeurAPlaques1D.DPc[3]
10/28 (1): echangeurAPlaques1D.DPc[3] = if noEvent(echangeurAPlaques1D.qmc[3] < 0.001) then 0.0 else echangeurAPlaques1D.c1 * 14423.2 / (echangeurAPlaques1D.rhoc[3] * abs(echangeurAPlaques1D.qmc[3]) ^ 0.097) * echangeurAPlaques1D.quc[3] ^ 2.0 * (1472.47 + 0.77 * (echangeurAPlaques1D.M - 1.0) + 104.97 / abs(echangeurAPlaques1D.qmc[3]) ^ 0.25)
11/29 (1): echangeurAPlaques1D.qmc[3] = abs(echangeurAPlaques1D.Qcc[6]) / ($cse16 * echangeurAPlaques1D.M)
12/30 (1): $cse16 = max(1e-9, echangeurAPlaques1D.muc[3])
13/31 (1): echangeurAPlaques1D.muc[3] = ThermoSysPro.Properties.WaterSteam.IF97.DynamicViscosity_rhoT(echangeurAPlaques1D.rhoc[3], echangeurAPlaques1D.Tmc[3])
14/32 (10): $cse14 = ThermoSysPro.Properties.WaterSteam.IF97.Water_Ph(echangeurAPlaques1D.Pmc[3], echangeurAPlaques1D.Hmc[3], echangeurAPlaques1D.modec)
15/42 (10): ThermoSysPro.Properties.WaterSteam.Common.ThermoProperties_ph(echangeurAPlaques1D.Tmc[3], echangeurAPlaques1D.rhoc[3], echangeurAPlaques1D.proc[3].u, echangeurAPlaques1D.proc[3].s, echangeurAPlaques1D.proc[3].cp, echangeurAPlaques1D.proc[3].ddhp, echangeurAPlaques1D.proc[3].ddph, echangeurAPlaques1D.proc[3].duph, echangeurAPlaques1D.proc[3].duhp, echangeurAPlaques1D.proc[3].x) = $cse14
16/52 (1): echangeurAPlaques1D.Pmc[3] = 0.5 * (echangeurAPlaques1D.Pcc[3] + echangeurAPlaques1D.Pcc[4])
17/53 (1): echangeurAPlaques1D.Pcc[3] = if echangeurAPlaques1D.Qcc[6] > 0.0 then echangeurAPlaques1D.Pcc[2] - 0.2 * echangeurAPlaques1D.DPc[2] else echangeurAPlaques1D.Pcc[2] + 0.2 * echangeurAPlaques1D.DPc[2]
18/54 (1): echangeurAPlaques1D.DPc[2] = if noEvent(echangeurAPlaques1D.qmc[2] < 0.001) then 0.0 else echangeurAPlaques1D.c1 * 14423.2 / (echangeurAPlaques1D.rhoc[2] * abs(echangeurAPlaques1D.qmc[2]) ^ 0.097) * echangeurAPlaques1D.quc[2] ^ 2.0 * (1472.47 + 0.77 * (echangeurAPlaques1D.M - 1.0) + 104.97 / abs(echangeurAPlaques1D.qmc[2]) ^ 0.25)
19/55 (1): echangeurAPlaques1D.qmc[2] = abs(echangeurAPlaques1D.Qcc[6]) / ($cse20 * echangeurAPlaques1D.M)
20/56 (1): $cse20 = max(1e-9, echangeurAPlaques1D.muc[2])
21/57 (1): echangeurAPlaques1D.muc[2] = ThermoSysPro.Properties.WaterSteam.IF97.DynamicViscosity_rhoT(echangeurAPlaques1D.rhoc[2], echangeurAPlaques1D.Tmc[2])
22/58 (10): $cse18 = ThermoSysPro.Properties.WaterSteam.IF97.Water_Ph(echangeurAPlaques1D.Pmc[2], echangeurAPlaques1D.Hmc[2], echangeurAPlaques1D.modec)
23/68 (10): ThermoSysPro.Properties.WaterSteam.Common.ThermoProperties_ph(echangeurAPlaques1D.Tmc[2], echangeurAPlaques1D.rhoc[2], echangeurAPlaques1D.proc[2].u, echangeurAPlaques1D.proc[2].s, echangeurAPlaques1D.proc[2].cp, echangeurAPlaques1D.proc[2].ddhp, echangeurAPlaques1D.proc[2].ddph, echangeurAPlaques1D.proc[2].duph, echangeurAPlaques1D.proc[2].duhp, echangeurAPlaques1D.proc[2].x) = $cse18
24/78 (1): echangeurAPlaques1D.Pmc[2] = 0.5 * (echangeurAPlaques1D.Pcc[2] + echangeurAPlaques1D.Pcc[3])
25/79 (1): echangeurAPlaques1D.Pcc[2] = if echangeurAPlaques1D.Qcc[6] > 0.0 then sourceP.P0 - 0.2 * echangeurAPlaques1D.DPc[1] else sourceP.P0 + 0.2 * echangeurAPlaques1D.DPc[1]
26/80 (1): echangeurAPlaques1D.DPc[1] = if noEvent(echangeurAPlaques1D.qmc[1] < 0.001) then 0.0 else echangeurAPlaques1D.c1 * 14423.2 / (echangeurAPlaques1D.rhoc[1] * abs(echangeurAPlaques1D.qmc[1]) ^ 0.097) * echangeurAPlaques1D.quc[1] ^ 2.0 * (1472.47 + 0.77 * (echangeurAPlaques1D.M - 1.0) + 104.97 / abs(echangeurAPlaques1D.qmc[1]) ^ 0.25)
27/81 (1): echangeurAPlaques1D.quc[1] = abs(echangeurAPlaques1D.Qcc[6]) / echangeurAPlaques1D.M
28/82 (1): echangeurAPlaques1D.qmc[1] = abs(echangeurAPlaques1D.Qcc[6]) / ($cse24 * echangeurAPlaques1D.M)
29/83 (1): echangeurAPlaques1D.quc[2] = abs(echangeurAPlaques1D.Qcc[6]) / echangeurAPlaques1D.M
30/84 (1): echangeurAPlaques1D.quc[3] = abs(echangeurAPlaques1D.Qcc[6]) / echangeurAPlaques1D.M
31/85 (1): echangeurAPlaques1D.qmc[4] = abs(echangeurAPlaques1D.Qcc[6]) / ($cse12 * echangeurAPlaques1D.M)
32/86 (1): echangeurAPlaques1D.DPc[4] = if noEvent(echangeurAPlaques1D.qmc[4] < 0.001) then 0.0 else echangeurAPlaques1D.c1 * 14423.2 / (echangeurAPlaques1D.rhoc[4] * abs(echangeurAPlaques1D.qmc[4]) ^ 0.097) * echangeurAPlaques1D.quc[4] ^ 2.0 * (1472.47 + 0.77 * (echangeurAPlaques1D.M - 1.0) + 104.97 / abs(echangeurAPlaques1D.qmc[4]) ^ 0.25)
33/87 (1): echangeurAPlaques1D.quc[4] = abs(echangeurAPlaques1D.Qcc[6]) / echangeurAPlaques1D.M
34/88 (1): puitsP.P0 = if echangeurAPlaques1D.Qcc[6] > 0.0 then echangeurAPlaques1D.Pcc[5] - 0.2 * echangeurAPlaques1D.DPc[5] else echangeurAPlaques1D.Pcc[5] + 0.2 * echangeurAPlaques1D.DPc[5]
35/89 (1): echangeurAPlaques1D.quc[5] = abs(echangeurAPlaques1D.Qcc[6]) / echangeurAPlaques1D.M
36/90 (1): echangeurAPlaques1D.Pmc[1] = 0.5 * (sourceP.P0 + echangeurAPlaques1D.Pcc[2])
37/91 (10): $cse22 = ThermoSysPro.Properties.WaterSteam.IF97.Water_Ph(echangeurAPlaques1D.Pmc[1], echangeurAPlaques1D.Hmc[1], echangeurAPlaques1D.modec)
38/101 (1): echangeurAPlaques1D.muc[1] = ThermoSysPro.Properties.WaterSteam.IF97.DynamicViscosity_rhoT(echangeurAPlaques1D.rhoc[1], echangeurAPlaques1D.Tmc[1])
39/102 (1): $cse24 = max(1e-9, echangeurAPlaques1D.muc[1])
40/103 (10): ThermoSysPro.Properties.WaterSteam.Common.ThermoProperties_ph(echangeurAPlaques1D.Tmc[1], echangeurAPlaques1D.rhoc[1], echangeurAPlaques1D.proc[1].u, echangeurAPlaques1D.proc[1].s, echangeurAPlaques1D.proc[1].cp, echangeurAPlaques1D.proc[1].ddhp, echangeurAPlaques1D.proc[1].ddph, echangeurAPlaques1D.proc[1].duph, echangeurAPlaques1D.proc[1].duhp, echangeurAPlaques1D.proc[1].x) = $cse22
41/113 (1): echangeurAPlaques1D.Pmc[4] = 0.5 * (echangeurAPlaques1D.Pcc[4] + echangeurAPlaques1D.Pcc[5])
42/114 (10): $cse10 = ThermoSysPro.Properties.WaterSteam.IF97.Water_Ph(echangeurAPlaques1D.Pmc[4], echangeurAPlaques1D.Hmc[4], echangeurAPlaques1D.modec)
43/124 (1): echangeurAPlaques1D.muc[4] = ThermoSysPro.Properties.WaterSteam.IF97.DynamicViscosity_rhoT(echangeurAPlaques1D.rhoc[4], echangeurAPlaques1D.Tmc[4])
44/125 (1): $cse12 = max(1e-9, echangeurAPlaques1D.muc[4])
45/126 (10): ThermoSysPro.Properties.WaterSteam.Common.ThermoProperties_ph(echangeurAPlaques1D.Tmc[4], echangeurAPlaques1D.rhoc[4], echangeurAPlaques1D.proc[4].u, echangeurAPlaques1D.proc[4].s, echangeurAPlaques1D.proc[4].cp, echangeurAPlaques1D.proc[4].ddhp, echangeurAPlaques1D.proc[4].ddph, echangeurAPlaques1D.proc[4].duph, echangeurAPlaques1D.proc[4].duhp, echangeurAPlaques1D.proc[4].x) = $cse10

Variables:
1: echangeurAPlaques1D.proc[4].duhp:VARIABLE(unit = "1" )  "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real [5]
2: echangeurAPlaques1D.proc[4].ddph:VARIABLE(unit = "s2/m2" )  "Derivative of density wrt. pressure at constant specific enthalpy" type: Real [5]
3: echangeurAPlaques1D.proc[4].s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific entropy" type: Real [5]
4: echangeurAPlaques1D.proc[4].u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 )  "Specific inner energy" type: Real [5]
5: echangeurAPlaques1D.rhoc[4]:VARIABLE(min = 1e-9 max = 1e5 start = 998.0 unit = "kg/m3" nominal = 998.0 )  "Hot fluid density" type: Real [5]
6: echangeurAPlaques1D.proc[4].ddhp:VARIABLE(unit = "kg.s2/m5" )  "Derivative of density wrt. specific enthalpy at constant pressure" type: Real [5]
7: echangeurAPlaques1D.proc[4].cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific heat capacity at constant presure" type: Real [5]
8: echangeurAPlaques1D.proc[4].x:VARIABLE(min = 0.0 max = 1.0 unit = "1" )  "Vapor mass fraction" type: Real [5]
9: echangeurAPlaques1D.proc[4].duph:VARIABLE(unit = "m3/kg" )  "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real [5]
10: $cse12:VARIABLE(protected = true )  type: Real unreplaceable
11: echangeurAPlaques1D.muc[4]:VARIABLE(min = 0.0 start = 0.001 unit = "Pa.s" )  "Hot fluid dynamic viscosity" type: Real [5]
12: echangeurAPlaques1D.Tmc[4]:VARIABLE(min = 200.0 max = 6000.0 start = 290.0 unit = "K" nominal = 300.0 )  "Hot fluid average temperature" type: Real [5]
13: $cse10.x:VARIABLE(protected = true )  type: Real unreplaceable
14: $cse10.ddhp:VARIABLE(protected = true )  type: Real unreplaceable
15: $cse10.duph:VARIABLE(protected = true )  type: Real unreplaceable
16: $cse10.cp:VARIABLE(protected = true )  type: Real unreplaceable
17: $cse10.s:VARIABLE(protected = true )  type: Real unreplaceable
18: $cse10.u:VARIABLE(protected = true )  type: Real unreplaceable
19: $cse10.d:VARIABLE(protected = true )  type: Real unreplaceable
20: $cse10.duhp:VARIABLE(protected = true )  type: Real unreplaceable
21: $cse10.T:VARIABLE(protected = true )  type: Real unreplaceable
22: $cse10.ddph:VARIABLE(protected = true )  type: Real unreplaceable
23: echangeurAPlaques1D.Pmc[4]:VARIABLE(min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 )  "Hot fluid average pressure" type: Real [5]
24: echangeurAPlaques1D.proc[1].duph:VARIABLE(unit = "m3/kg" )  "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real [5]
25: echangeurAPlaques1D.proc[1].ddph:VARIABLE(unit = "s2/m2" )  "Derivative of density wrt. pressure at constant specific enthalpy" type: Real [5]
26: echangeurAPlaques1D.proc[1].duhp:VARIABLE(unit = "1" )  "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real [5]
27: echangeurAPlaques1D.proc[1].x:VARIABLE(min = 0.0 max = 1.0 unit = "1" )  "Vapor mass fraction" type: Real [5]
28: echangeurAPlaques1D.rhoc[1]:VARIABLE(min = 1e-9 max = 1e5 start = 998.0 unit = "kg/m3" nominal = 998.0 )  "Hot fluid density" type: Real [5]
29: echangeurAPlaques1D.proc[1].u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 )  "Specific inner energy" type: Real [5]
30: $cse24:VARIABLE(protected = true )  type: Real unreplaceable
31: echangeurAPlaques1D.muc[1]:VARIABLE(min = 0.0 start = 0.001 unit = "Pa.s" )  "Hot fluid dynamic viscosity" type: Real [5]
32: echangeurAPlaques1D.Tmc[1]:VARIABLE(min = 200.0 max = 6000.0 start = 290.0 unit = "K" nominal = 300.0 )  "Hot fluid average temperature" type: Real [5]
33: echangeurAPlaques1D.proc[1].s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific entropy" type: Real [5]
34: echangeurAPlaques1D.proc[1].cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific heat capacity at constant presure" type: Real [5]
35: echangeurAPlaques1D.proc[1].ddhp:VARIABLE(unit = "kg.s2/m5" )  "Derivative of density wrt. specific enthalpy at constant pressure" type: Real [5]
36: $cse22.d:VARIABLE(protected = true )  type: Real unreplaceable
37: $cse22.duph:VARIABLE(protected = true )  type: Real unreplaceable
38: $cse22.ddph:VARIABLE(protected = true )  type: Real unreplaceable
39: $cse22.s:VARIABLE(protected = true )  type: Real unreplaceable
40: $cse22.u:VARIABLE(protected = true )  type: Real unreplaceable
41: $cse22.x:VARIABLE(protected = true )  type: Real unreplaceable
42: $cse22.ddhp:VARIABLE(protected = true )  type: Real unreplaceable
43: $cse22.duhp:VARIABLE(protected = true )  type: Real unreplaceable
44: $cse22.T:VARIABLE(protected = true )  type: Real unreplaceable
45: $cse22.cp:VARIABLE(protected = true )  type: Real unreplaceable
46: echangeurAPlaques1D.Pmc[1]:VARIABLE(min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 )  "Hot fluid average pressure" type: Real [5]
47: echangeurAPlaques1D.quc[5]:VARIABLE()  type: Real [5]
48: echangeurAPlaques1D.DPc[5]:VARIABLE(unit = "Pa" )  "Pressure loss of the hot fluid" type: Real [5]
49: echangeurAPlaques1D.quc[4]:VARIABLE()  type: Real [5]
50: echangeurAPlaques1D.DPc[4]:VARIABLE(unit = "Pa" )  "Pressure loss of the hot fluid" type: Real [5]
51: echangeurAPlaques1D.qmc[4]:VARIABLE()  type: Real [5]
52: echangeurAPlaques1D.quc[3]:VARIABLE()  type: Real [5]
53: echangeurAPlaques1D.quc[2]:VARIABLE()  type: Real [5]
54: echangeurAPlaques1D.qmc[1]:VARIABLE()  type: Real [5]
55: echangeurAPlaques1D.Qcc[6]:VARIABLE(start = 500.0 unit = "kg/s" )  "Hot fluid mass flow rate at the boundary of section i" type: Real [6]
56: echangeurAPlaques1D.quc[1]:VARIABLE()  type: Real [5]
57: echangeurAPlaques1D.DPc[1]:VARIABLE(unit = "Pa" )  "Pressure loss of the hot fluid" type: Real [5]
58: echangeurAPlaques1D.Pcc[2]:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 )  "Hot fluid pressure at the boundary of section i" type: Real [6]
59: echangeurAPlaques1D.proc[2].ddph:VARIABLE(unit = "s2/m2" )  "Derivative of density wrt. pressure at constant specific enthalpy" type: Real [5]
60: echangeurAPlaques1D.proc[2].u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 )  "Specific inner energy" type: Real [5]
61: echangeurAPlaques1D.Tmc[2]:VARIABLE(min = 200.0 max = 6000.0 start = 290.0 unit = "K" nominal = 300.0 )  "Hot fluid average temperature" type: Real [5]
62: echangeurAPlaques1D.proc[2].cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific heat capacity at constant presure" type: Real [5]
63: echangeurAPlaques1D.proc[2].duhp:VARIABLE(unit = "1" )  "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real [5]
64: echangeurAPlaques1D.proc[2].duph:VARIABLE(unit = "m3/kg" )  "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real [5]
65: $cse18.duph:VARIABLE(protected = true )  type: Real unreplaceable
66: $cse18.duhp:VARIABLE(protected = true )  type: Real unreplaceable
67: $cse18.ddph:VARIABLE(protected = true )  type: Real unreplaceable
68: $cse18.x:VARIABLE(protected = true )  type: Real unreplaceable
69: $cse18.u:VARIABLE(protected = true )  type: Real unreplaceable
70: echangeurAPlaques1D.Pmc[2]:VARIABLE(min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 )  "Hot fluid average pressure" type: Real [5]
71: $cse18.cp:VARIABLE(protected = true )  type: Real unreplaceable
72: $cse18.s:VARIABLE(protected = true )  type: Real unreplaceable
73: $cse18.d:VARIABLE(protected = true )  type: Real unreplaceable
74: $cse18.T:VARIABLE(protected = true )  type: Real unreplaceable
75: $cse18.ddhp:VARIABLE(protected = true )  type: Real unreplaceable
76: echangeurAPlaques1D.proc[2].ddhp:VARIABLE(unit = "kg.s2/m5" )  "Derivative of density wrt. specific enthalpy at constant pressure" type: Real [5]
77: echangeurAPlaques1D.proc[2].x:VARIABLE(min = 0.0 max = 1.0 unit = "1" )  "Vapor mass fraction" type: Real [5]
78: echangeurAPlaques1D.proc[2].s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific entropy" type: Real [5]
79: echangeurAPlaques1D.rhoc[2]:VARIABLE(min = 1e-9 max = 1e5 start = 998.0 unit = "kg/m3" nominal = 998.0 )  "Hot fluid density" type: Real [5]
80: echangeurAPlaques1D.muc[2]:VARIABLE(min = 0.0 start = 0.001 unit = "Pa.s" )  "Hot fluid dynamic viscosity" type: Real [5]
81: $cse20:VARIABLE(protected = true )  type: Real unreplaceable
82: echangeurAPlaques1D.qmc[2]:VARIABLE()  type: Real [5]
83: echangeurAPlaques1D.DPc[2]:VARIABLE(unit = "Pa" )  "Pressure loss of the hot fluid" type: Real [5]
84: echangeurAPlaques1D.Pcc[3]:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 )  "Hot fluid pressure at the boundary of section i" type: Real [6]
85: echangeurAPlaques1D.proc[3].ddph:VARIABLE(unit = "s2/m2" )  "Derivative of density wrt. pressure at constant specific enthalpy" type: Real [5]
86: $cse14.s:VARIABLE(protected = true )  type: Real unreplaceable
87: $cse14.duhp:VARIABLE(protected = true )  type: Real unreplaceable
88: echangeurAPlaques1D.Pmc[3]:VARIABLE(min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 )  "Hot fluid average pressure" type: Real [5]
89: $cse14.d:VARIABLE(protected = true )  type: Real unreplaceable
90: $cse14.ddph:VARIABLE(protected = true )  type: Real unreplaceable
91: $cse14.T:VARIABLE(protected = true )  type: Real unreplaceable
92: $cse14.cp:VARIABLE(protected = true )  type: Real unreplaceable
93: $cse14.u:VARIABLE(protected = true )  type: Real unreplaceable
94: $cse14.ddhp:VARIABLE(protected = true )  type: Real unreplaceable
95: $cse14.duph:VARIABLE(protected = true )  type: Real unreplaceable
96: $cse14.x:VARIABLE(protected = true )  type: Real unreplaceable
97: echangeurAPlaques1D.proc[3].ddhp:VARIABLE(unit = "kg.s2/m5" )  "Derivative of density wrt. specific enthalpy at constant pressure" type: Real [5]
98: echangeurAPlaques1D.proc[3].s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific entropy" type: Real [5]
99: echangeurAPlaques1D.proc[3].x:VARIABLE(min = 0.0 max = 1.0 unit = "1" )  "Vapor mass fraction" type: Real [5]
100: echangeurAPlaques1D.proc[3].duhp:VARIABLE(unit = "1" )  "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real [5]
101: echangeurAPlaques1D.proc[3].u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 )  "Specific inner energy" type: Real [5]
102: echangeurAPlaques1D.Tmc[3]:VARIABLE(min = 200.0 max = 6000.0 start = 290.0 unit = "K" nominal = 300.0 )  "Hot fluid average temperature" type: Real [5]
103: echangeurAPlaques1D.proc[3].duph:VARIABLE(unit = "m3/kg" )  "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real [5]
104: echangeurAPlaques1D.proc[3].cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific heat capacity at constant presure" type: Real [5]
105: echangeurAPlaques1D.rhoc[3]:VARIABLE(min = 1e-9 max = 1e5 start = 998.0 unit = "kg/m3" nominal = 998.0 )  "Hot fluid density" type: Real [5]
106: echangeurAPlaques1D.muc[3]:VARIABLE(min = 0.0 start = 0.001 unit = "Pa.s" )  "Hot fluid dynamic viscosity" type: Real [5]
107: $cse16:VARIABLE(protected = true )  type: Real unreplaceable
108: echangeurAPlaques1D.qmc[3]:VARIABLE()  type: Real [5]
109: echangeurAPlaques1D.DPc[3]:VARIABLE(unit = "Pa" )  "Pressure loss of the hot fluid" type: Real [5]
110: echangeurAPlaques1D.Pcc[4]:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 )  "Hot fluid pressure at the boundary of section i" type: Real [6]
111: echangeurAPlaques1D.Pcc[5]:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 )  "Hot fluid pressure at the boundary of section i" type: Real [6]
112: echangeurAPlaques1D.proc[5].ddhp:VARIABLE(unit = "kg.s2/m5" )  "Derivative of density wrt. specific enthalpy at constant pressure" type: Real [5]
113: $cse6.ddph:VARIABLE(protected = true )  type: Real unreplaceable
114: echangeurAPlaques1D.Pmc[5]:VARIABLE(min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 )  "Hot fluid average pressure" type: Real [5]
115: $cse6.d:VARIABLE(protected = true )  type: Real unreplaceable
116: $cse6.u:VARIABLE(protected = true )  type: Real unreplaceable
117: $cse6.ddhp:VARIABLE(protected = true )  type: Real unreplaceable
118: $cse6.duhp:VARIABLE(protected = true )  type: Real unreplaceable
119: $cse6.cp:VARIABLE(protected = true )  type: Real unreplaceable
120: $cse6.s:VARIABLE(protected = true )  type: Real unreplaceable
121: $cse6.T:VARIABLE(protected = true )  type: Real unreplaceable
122: $cse6.duph:VARIABLE(protected = true )  type: Real unreplaceable
123: $cse6.x:VARIABLE(protected = true )  type: Real unreplaceable
124: echangeurAPlaques1D.proc[5].duhp:VARIABLE(unit = "1" )  "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real [5]
125: echangeurAPlaques1D.proc[5].u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 )  "Specific inner energy" type: Real [5]
126: echangeurAPlaques1D.proc[5].s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific entropy" type: Real [5]
127: echangeurAPlaques1D.proc[5].x:VARIABLE(min = 0.0 max = 1.0 unit = "1" )  "Vapor mass fraction" type: Real [5]
128: echangeurAPlaques1D.proc[5].cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific heat capacity at constant presure" type: Real [5]
129: echangeurAPlaques1D.rhoc[5]:VARIABLE(min = 1e-9 max = 1e5 start = 998.0 unit = "kg/m3" nominal = 998.0 )  "Hot fluid density" type: Real [5]
130: echangeurAPlaques1D.qmc[5]:VARIABLE()  type: Real [5]
131: $cse8:VARIABLE(protected = true )  type: Real unreplaceable
132: echangeurAPlaques1D.muc[5]:VARIABLE(min = 0.0 start = 0.001 unit = "Pa.s" )  "Hot fluid dynamic viscosity" type: Real [5]
133: echangeurAPlaques1D.Tmc[5]:VARIABLE(min = 200.0 max = 6000.0 start = 290.0 unit = "K" nominal = 300.0 )  "Hot fluid average temperature" type: Real [5]
134: echangeurAPlaques1D.proc[5].duph:VARIABLE(unit = "m3/kg" )  "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real [5]
135: echangeurAPlaques1D.proc[5].ddph:VARIABLE(unit = "s2/m2" )  "Derivative of density wrt. pressure at constant specific enthalpy" type: Real [5]
[/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 0.003084/2.267, allocations: 6.747 MB / 0.7388 GB, free: 205.7 MB / 0.5919 GB
Error: post-optimization module createDAEmodeBDAE (simulation) failed.
Error: Internal error SimCode DAEmode: The model ThermoSysPro.Examples.SimpleExamples.TestDynamicWaterWaterExchanger could not be translated