Running: ./testmodel.py --libraries=/home/hudson/saved_omc/libraries/.openmodelica/libraries --ompython_omhome=/usr ThermoSysPro_ThermoSysPro.Fluid.Examples.SimpleExamples.TestDynamicPlateHeatExchanger.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.TestDynamicPlateHeatExchanger,tolerance=1e-06,outputFormat="empty",numberOfIntervals=5000,variableFilter="",fileNamePrefix="ThermoSysPro_ThermoSysPro.Fluid.Examples.SimpleExamples.TestDynamicPlateHeatExchanger")
translateModel(ThermoSysPro.Fluid.Examples.SimpleExamples.TestDynamicPlateHeatExchanger,tolerance=1e-06,outputFormat="empty",numberOfIntervals=5000,variableFilter="",fileNamePrefix="ThermoSysPro_ThermoSysPro.Fluid.Examples.SimpleExamples.TestDynamicPlateHeatExchanger")
Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermoSysPro 4.0.0-master/package.mo): time 0.9344/0.9344, allocations: 150.9 MB / 167.2 MB, free: 14.53 MB / 142.1 MB
Notification: Performance of FrontEnd - loaded program: time 0.000369/0.000369, allocations: 15.98 kB / 237.8 MB, free: 1.77 MB / 190.1 MB
Notification: Performance of FrontEnd - Absyn->SCode: time 0.06413/0.06451, 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.Fluid.Examples.SimpleExamples.TestDynamicPlateHeatExchanger): time 1.721/1.786, allocations: 299.8 MB / 0.5556 GB, free: 8.234 MB / 446.1 MB
Notification: Performance of NFInst.instExpressions: time 0.5674/2.353, allocations: 195.7 MB / 0.7466 GB, free: 108 kB / 0.5919 GB
Notification: Performance of NFInst.updateImplicitVariability: time 0.001569/2.355, allocations: 35.69 kB / 0.7467 GB, free: 108 kB / 0.5919 GB
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermoSysPro 4.0.0-master/Fluid/HeatExchangers/DynamicPlateHeatExchanger.mo:227:3-228:54: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/DynamicPlateHeatExchanger.mo:229:3-230:54: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/DynamicPlateHeatExchanger.mo:231:3-232:52: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/DynamicPlateHeatExchanger.mo:233:3-234:52: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/SourcePQ.mo:74:3-75:65:writable] Warning: Connector C is not balanced: The number of potential variables (9) is not equal to the number of flow variables (0).
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermoSysPro 4.0.0-master/Fluid/BoundaryConditions/Sink.mo:39:3-40:67:writable] Warning: Connector C is not balanced: The number of potential variables (9) is not equal to the number of flow variables (0).
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermoSysPro 4.0.0-master/Fluid/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/SourcePQ.mo:74:3-75:65:writable] Warning: Connector C is not balanced: The number of potential variables (9) is not equal to the number of flow variables (0).
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermoSysPro 4.0.0-master/Fluid/BoundaryConditions/Sink.mo:39:3-40:67:writable] Warning: Connector C is not balanced: The number of potential variables (9) is not equal to the number of flow variables (0).
Notification: Performance of NFTyping.typeComponents: time 0.0009525/2.356, allocations: 343 kB / 0.747 GB, free: 100 kB / 0.5919 GB
Notification: Performance of NFTyping.typeBindings: time 0.002021/2.358, allocations: 0.8382 MB / 0.7478 GB, free: 64 kB / 0.5919 GB
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermoSysPro 4.0.0-master/Properties/WaterSteam/IF97_packages.mo:783:9-783:27:writable] Warning: cv was used before it was defined (given a value). Additional such uses may exist for the variable, but some messages were suppressed.
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermoSysPro 4.0.0-master/Properties/WaterSteam/IF97_packages.mo:850:9-850:27:writable] Warning: cv was used before it was defined (given a value). Additional such uses may exist for the variable, but some messages were suppressed.
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermoSysPro 4.0.0-master/Properties/WaterSteam/IF97_packages.mo:1088:9-1088:27:writable] Warning: cv was used before it was defined (given a value). Additional such uses may exist for the variable, but some messages were suppressed.
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermoSysPro 4.0.0-master/Properties/WaterSteamSimple/prop4_Ph.mo:69:3-69:60:writable] Warning: dh1satp was used before it was defined (given a value). Additional such uses may exist for the variable, but some messages were suppressed.
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermoSysPro 4.0.0-master/Properties/WaterSteamSimple/prop4_Ph.mo:69:3-69:60:writable] Warning: dh2satp was used before it was defined (given a value). Additional such uses may exist for the variable, but some messages were suppressed.
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermoSysPro 4.0.0-master/Properties/WaterSteamSimple/prop4_Ph_der.mo:167:3-170:49:writable] Warning: du1satp_der was used before it was defined (given a value). Additional such uses may exist for the variable, but some messages were suppressed.
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermoSysPro 4.0.0-master/Properties/WaterSteamSimple/prop4_Ph_der.mo:167:3-170:49:writable] Warning: du2satp_der was used before it was defined (given a value). Additional such uses may exist for the variable, but some messages were suppressed.
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermoSysPro 4.0.0-master/Properties/Fluid/derDensity_derP_derh.mo:63:5-63:84:writable] Warning: T was used before it was defined (given a value). Additional such uses may exist for the variable, but some messages were suppressed.
Notification: Performance of NFTyping.typeClassSections: time 0.03752/2.395, allocations: 13.76 MB / 0.7612 GB, free: 15.67 MB / 0.6075 GB
Notification: Performance of NFFlatten.flatten: time 0.008572/2.404, allocations: 8.77 MB / 0.7698 GB, free: 15.65 MB / 0.6075 GB
Notification: Performance of NFFlatten.resolveConnections: time 0.005519/2.41, allocations: 2.819 MB / 0.7726 GB, free: 14.77 MB / 0.6075 GB
Notification: Performance of NFEvalConstants.evaluate: time 0.005151/2.415, allocations: 2.699 MB / 0.7752 GB, free: 14.4 MB / 0.6075 GB
Notification: Performance of NFSimplifyModel.simplify: time 0.005797/2.421, allocations: 3.457 MB / 0.7786 GB, free: 13.55 MB / 0.6075 GB
Notification: Performance of NFPackage.collectConstants: time 0.002906/2.424, allocations: 0.6258 MB / 0.7792 GB, free: 13.55 MB / 0.6075 GB
Notification: Performance of NFFlatten.collectFunctions: time 0.04846/2.472, allocations: 22.89 MB / 0.8015 GB, free: 3.367 MB / 0.6075 GB
Notification: Performance of NFScalarize.scalarize: time 0.00356/2.476, allocations: 2.135 MB / 0.8036 GB, free: 1.422 MB / 0.6075 GB
Notification: Performance of NFVerifyModel.verify: time 0.006417/2.482, allocations: 2.68 MB / 0.8062 GB, free: 14.81 MB / 0.6231 GB
Notification: Performance of NFConvertDAE.convert: time 0.03995/2.522, allocations: 17.33 MB / 0.8232 GB, free: 14.75 MB / 0.6387 GB
Notification: Performance of FrontEnd - DAE generated: time 6.903e-06/2.522, allocations: 0 / 0.8232 GB, free: 14.75 MB / 0.6387 GB
Notification: Performance of FrontEnd: time 2.204e-06/2.522, allocations: 4 kB / 0.8232 GB, free: 14.75 MB / 0.6387 GB
Notification: Performance of Transformations before backend: time 0.0002084/2.522, allocations: 0 / 0.8232 GB, free: 14.75 MB / 0.6387 GB
Notification: Model statistics after passing the front-end and creating the data structures used by the back-end:
 * Number of equations: 1134
 * Number of variables: 1134
Notification: Performance of Generate backend data structure: time 0.02271/2.545, allocations: 6.619 MB / 0.8296 GB, free: 8.066 MB / 0.6387 GB
Notification: Performance of prepare preOptimizeDAE: time 4.969e-05/2.545, allocations: 12.03 kB / 0.8296 GB, free: 8.055 MB / 0.6387 GB
Notification: Performance of preOpt normalInlineFunction (simulation): time 0.001418/2.547, allocations: 439 kB / 0.8301 GB, free: 7.621 MB / 0.6387 GB
Notification: Performance of preOpt evaluateParameters (simulation): time 0.004871/2.551, allocations: 2.161 MB / 0.8322 GB, free: 5.535 MB / 0.6387 GB
Notification: Performance of preOpt simplifyIfEquations (simulation): time 0.0005077/2.552, allocations: 460.1 kB / 0.8326 GB, free: 5.066 MB / 0.6387 GB
Notification: Performance of preOpt expandDerOperator (simulation): time 0.0009887/2.553, allocations: 404 kB / 0.833 GB, free: 4.672 MB / 0.6387 GB
Notification: Performance of preOpt clockPartitioning (simulation): time 0.01514/2.568, allocations: 7.603 MB / 0.8404 GB, free: 12.97 MB / 0.6544 GB
Notification: Performance of preOpt findStateOrder (simulation): time 8.098e-05/2.568, allocations: 10.47 kB / 0.8404 GB, free: 12.96 MB / 0.6544 GB
Notification: Performance of preOpt replaceEdgeChange (simulation): time 0.0005173/2.569, allocations: 172 kB / 0.8406 GB, free: 12.79 MB / 0.6544 GB
Notification: Performance of preOpt inlineArrayEqn (simulation): time 9.553e-05/2.569, allocations: 116 kB / 0.8407 GB, free: 12.68 MB / 0.6544 GB
Notification: Performance of preOpt removeEqualRHS (simulation): time 0.02594/2.595, allocations: 18.34 MB / 0.8586 GB, free: 10.34 MB / 0.67 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 0.2034/2.798, allocations: 92.5 MB / 0.9489 GB, free: 7.238 MB / 0.7637 GB
Notification: Performance of preOpt comSubExp (simulation): time 0.01385/2.812, allocations: 7.841 MB / 0.9566 GB, free: 15.4 MB / 0.7794 GB
Notification: Performance of preOpt resolveLoops (simulation): time 0.007795/2.82, allocations: 4.075 MB / 0.9606 GB, free: 11.3 MB / 0.7794 GB
Notification: Performance of preOpt evalFunc (simulation): time 0.7815/3.602, allocations: 345.3 MB / 1.298 GB, free: 149.9 MB / 0.8262 GB
Notification: Performance of preOpt encapsulateWhenConditions (simulation): time 0.0001561/3.602, allocations: 92.81 kB / 1.298 GB, free: 149.8 MB / 0.8262 GB
Notification: Performance of pre-optimization done (n=676): time 8.677e-06/3.602, allocations: 0 / 1.298 GB, free: 149.8 MB / 0.8262 GB
Notification: Performance of matching and sorting (n=676): time 0.04184/3.644, allocations: 16.89 MB / 1.314 GB, free: 133.7 MB / 0.8262 GB
Notification: Performance of inlineWhenForInitialization (initialization): time 5.487e-05/3.644, allocations: 137.7 kB / 1.314 GB, free: 133.6 MB / 0.8262 GB
Notification: Performance of selectInitializationVariablesDAE (initialization): time 0.001593/3.645, allocations: 1.436 MB / 1.316 GB, free: 132.2 MB / 0.8262 GB
Notification: Performance of collectPreVariables (initialization): time 0.0008792/3.646, allocations: 125.7 kB / 1.316 GB, free: 132 MB / 0.8262 GB
Notification: Performance of collectInitialEqns (initialization): time 0.0004762/3.647, allocations: 1.036 MB / 1.317 GB, free: 131 MB / 0.8262 GB
Notification: Performance of collectInitialBindings (initialization): time 0.001659/3.648, allocations: 2.27 MB / 1.319 GB, free: 128.8 MB / 0.8262 GB
Notification: Performance of simplifyInitialFunctions (initialization): time 0.00163/3.65, allocations: 1.227 MB / 1.32 GB, free: 127.5 MB / 0.8262 GB
Notification: Performance of setup shared object (initialization): time 4.381e-05/3.65, allocations: 309 kB / 1.321 GB, free: 127.2 MB / 0.8262 GB
Notification: Performance of preBalanceInitialSystem (initialization): time 0.00592/3.656, allocations: 3.596 MB / 1.324 GB, free: 123.6 MB / 0.8262 GB
Notification: Performance of partitionIndependentBlocks (initialization): time 0.007203/3.663, allocations: 4.522 MB / 1.329 GB, free: 118.8 MB / 0.8262 GB
Notification: Performance of analyzeInitialSystem (initialization): time 0.01511/3.678, allocations: 8.646 MB / 1.337 GB, free: 109.9 MB / 0.8262 GB
Notification: Performance of solveInitialSystemEqSystem (initialization): time 3.032e-05/3.678, allocations: 8 kB / 1.337 GB, free: 109.9 MB / 0.8262 GB
Notification: Performance of matching and sorting (n=806) (initialization): time 0.02914/3.708, allocations: 13.52 MB / 1.35 GB, free: 96.42 MB / 0.8262 GB
Notification: Performance of prepare postOptimizeDAE: time 4.706e-05/3.708, allocations: 16.84 kB / 1.35 GB, free: 96.4 MB / 0.8262 GB
Notification: Performance of postOpt simplifyComplexFunction (initialization): time 4.466e-05/3.708, allocations: 20 kB / 1.35 GB, free: 96.38 MB / 0.8262 GB
Notification: Performance of postOpt tearingSystem (initialization): time 0.08058/3.788, allocations: 23.37 MB / 1.373 GB, free: 73.12 MB / 0.8262 GB
Notification: Performance of postOpt solveSimpleEquations (initialization): time 0.001302/3.79, allocations: 370.2 kB / 1.374 GB, free: 72.78 MB / 0.8262 GB
Notification: Performance of postOpt calculateStrongComponentJacobians (initialization): time 0.03004/3.82, allocations: 15.67 MB / 1.389 GB, free: 56.93 MB / 0.8262 GB
Notification: Performance of postOpt simplifyAllExpressions (initialization): time 0.004715/3.824, allocations: 0.6891 MB / 1.39 GB, free: 56.23 MB / 0.8262 GB
Notification: Performance of postOpt collapseArrayExpressions (initialization): time 0.001194/3.826, allocations: 307.8 kB / 1.39 GB, free: 55.93 MB / 0.8262 GB
Notification: Model statistics after passing the back-end for initialization:
 * Number of independent subsystems: 93
 * Number of states: 0 ()
 * Number of discrete variables: 20 (sourceP3.C.ftype,sourceP2.C.ftype,echangeurAPlaques.fluid_c,echangeurAPlaques.fluid_f,puitsP2.fluid,puitsP3.fluid,sourceP3.fluid1,sourceP2.fluid1,sourceP1.C.ftype,sourceP.C.ftype,echangeurAPlaques1D.fluid_c,echangeurAPlaques1D.fluid_f,puitsP.fluid,puitsP1.fluid,sourceP1.fluid1,sourceP.fluid1,echangeurAPlaques1D.Ef.diff_on_2,echangeurAPlaques1D.Sf.diff_on_1,echangeurAPlaques1D.Ec.diff_on_2,echangeurAPlaques1D.Sc.diff_on_1)
 * Number of discrete states: 0 ()
 * Number of clocked states: 0 ()
 * Top-level inputs: 0
Notification: Strong component statistics for initialization (197):
 * Single equations (assignments): 192
 * Array equations: 0
 * Algorithm blocks: 0
 * Record equations: 2
 * When equations: 0
 * If-equations: 0
 * Equation systems (not torn): 0
 * Torn equation systems: 3
 * Mixed (continuous/discrete) equation systems: 0
Notification: Torn system details for strict tearing set:
 * Linear torn systems (#iteration vars, #inner vars, density): 0 systems
 * Non-linear torn systems (#iteration vars, #inner vars): 3 systems
   {(4,23), (60,460), (2,9)}
Notification: Performance of prepare postOptimizeDAE: time 0.002153/3.828, allocations: 0.8975 MB / 1.391 GB, free: 55.05 MB / 0.8262 GB
Notification: Performance of postOpt lateInlineFunction (simulation): time 0.0008902/3.829, allocations: 359 kB / 1.391 GB, free: 54.7 MB / 0.8262 GB
Notification: Performance of postOpt wrapFunctionCalls (simulation): time 0.02903/3.858, allocations: 15.12 MB / 1.406 GB, free: 39.6 MB / 0.8262 GB
Notification: Performance of postOpt simplifysemiLinear (simulation): time 0.0001125/3.858, allocations: 27.89 kB / 1.406 GB, free: 39.57 MB / 0.8262 GB
Notification: Performance of postOpt simplifyComplexFunction (simulation): time 1.327e-05/3.858, allocations: 1.438 kB / 1.406 GB, free: 39.57 MB / 0.8262 GB
Notification: Performance of postOpt removeConstants (simulation): time 0.00329/3.861, allocations: 1.334 MB / 1.407 GB, free: 38.21 MB / 0.8262 GB
Notification: Performance of postOpt simplifyTimeIndepFuncCalls (simulation): time 0.0007145/3.862, allocations: 115.8 kB / 1.407 GB, free: 38.1 MB / 0.8262 GB
Notification: Performance of postOpt simplifyAllExpressions (simulation): time 0.003127/3.865, allocations: 275.8 kB / 1.407 GB, free: 37.83 MB / 0.8262 GB
Notification: Performance of postOpt findZeroCrossings (simulation): time 0.0007128/3.866, allocations: 409.2 kB / 1.408 GB, free: 37.43 MB / 0.8262 GB
[/var/lib/jenkins1/ws/OpenModelicaLibraryTestingWork/OpenModelica/OMCompiler/Compiler/BackEnd/DAEMode.mo:528:7-530:90:writable] Error: Internal error DAEMode.traverserStrongComponents failed on equation:
1/1 (10): ThermoSysPro.Properties.WaterSteam.Common.ThermoProperties_ph(echangeurAPlaques.Tmc, echangeurAPlaques.rhoc, echangeurAPlaques.proc.u, echangeurAPlaques.proc.s, echangeurAPlaques.proc.cp, echangeurAPlaques.proc.ddhp, echangeurAPlaques.proc.ddph, echangeurAPlaques.proc.duph, echangeurAPlaques.proc.duhp, echangeurAPlaques.proc.x) = $cse23

Variables:
1: echangeurAPlaques.proc.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific heat capacity at constant presure" type: Real
2: echangeurAPlaques.proc.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 )  "Specific inner energy" type: Real
3: $cse23.u:VARIABLE(protected = true )  type: Real unreplaceable
4: $cse23.s:VARIABLE(protected = true )  type: Real unreplaceable
5: $cse23.ddhp:VARIABLE(protected = true )  type: Real unreplaceable
6: echangeurAPlaques.Pmc:VARIABLE(min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 )  "Hot fluid average pressure" type: Real
7: $cse23.d:VARIABLE(protected = true )  type: Real unreplaceable
8: $cse23.duhp:VARIABLE(protected = true )  type: Real unreplaceable
9: $cse23.T:VARIABLE(protected = true )  type: Real unreplaceable
10: $cse23.x: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): puitsP2.P = if sourceP2.Q0 > 0.0 then sourceP2.P0 - echangeurAPlaques.DPc else sourceP2.P0 + echangeurAPlaques.DPc
2/2 (1): echangeurAPlaques.DPc = if noEvent(echangeurAPlaques.qmc < 0.001) then 0.0 else echangeurAPlaques.c1 * 14423.2 / (echangeurAPlaques.rhoc * echangeurAPlaques.qmc ^ 0.097) * echangeurAPlaques.quc ^ 2.0 * (1472.47 + 0.77 * (echangeurAPlaques.N - 1.0) + 104.97 / echangeurAPlaques.qmc ^ 0.25)
3/3 (1): echangeurAPlaques.muc = ThermoSysPro.Properties.Fluid.DynamicViscosity_rhoT(echangeurAPlaques.rhoc, echangeurAPlaques.Tmc, echangeurAPlaques.fluid_c)
4/4 (1): echangeurAPlaques.hc = if noEvent(echangeurAPlaques.qmc < 0.001) then 0.0 else 11.245 * echangeurAPlaques.qmc ^ 0.8 * abs(echangeurAPlaques.muc * echangeurAPlaques.proc.cp / echangeurAPlaques.lambdac) ^ 0.4 * echangeurAPlaques.lambdac
5/5 (1): echangeurAPlaques.K = echangeurAPlaques.hc * echangeurAPlaques.hf / (echangeurAPlaques.hc + echangeurAPlaques.hf + echangeurAPlaques.hc * echangeurAPlaques.hf * echangeurAPlaques.emetal / echangeurAPlaques.lambdam)
6/6 (1): echangeurAPlaques.W = echangeurAPlaques.K * echangeurAPlaques.S * echangeurAPlaques.DTm
7/7 (1): echangeurAPlaques.DTm = if noEvent(echangeurAPlaques.DT1 > echangeurAPlaques.DT2) and noEvent(echangeurAPlaques.DT2 > 0.0) or noEvent(echangeurAPlaques.DT1 < echangeurAPlaques.DT2) and noEvent(echangeurAPlaques.DT2 < 0.0) then (echangeurAPlaques.DT1 - echangeurAPlaques.DT2) / log(echangeurAPlaques.DT1 / echangeurAPlaques.DT2) else 0.5 * (echangeurAPlaques.DT1 + echangeurAPlaques.DT2)
8/8 (1): echangeurAPlaques.DT1 = echangeurAPlaques.Tec - echangeurAPlaques.Tsf
9/9 (10): $cse28 = ThermoSysPro.Properties.Fluid.Ph(puitsP3.P, echangeurAPlaques.Sf.h, echangeurAPlaques.mode_f, echangeurAPlaques.fluid_f)
10/19 (10): ThermoSysPro.Properties.WaterSteam.Common.ThermoProperties_ph(echangeurAPlaques.Tsf, echangeurAPlaques.profs.d, echangeurAPlaques.profs.u, echangeurAPlaques.profs.s, echangeurAPlaques.profs.cp, echangeurAPlaques.profs.ddhp, echangeurAPlaques.profs.ddph, echangeurAPlaques.profs.duph, echangeurAPlaques.profs.duhp, echangeurAPlaques.profs.x) = $cse28
11/29 (1): echangeurAPlaques.Hmf = 0.5 * (1e5 + echangeurAPlaques.Sf.h)
12/30 (10): $cse24 = ThermoSysPro.Properties.Fluid.Ph(echangeurAPlaques.Pmf, echangeurAPlaques.Hmf, echangeurAPlaques.mode_f, echangeurAPlaques.fluid_f)
13/40 (1): echangeurAPlaques.muf = ThermoSysPro.Properties.Fluid.DynamicViscosity_rhoT(echangeurAPlaques.rhof, echangeurAPlaques.Tmf, echangeurAPlaques.fluid_f)
14/41 (1): echangeurAPlaques.lambdaf = ThermoSysPro.Properties.Fluid.ThermalConductivity_rhoT(echangeurAPlaques.rhof, echangeurAPlaques.Tmf, echangeurAPlaques.Pmf, 0, echangeurAPlaques.fluid_f)
15/42 (1): echangeurAPlaques.hf = if noEvent(echangeurAPlaques.qmf < 0.001) then 0.0 else 11.245 * echangeurAPlaques.qmf ^ 0.8 * abs(echangeurAPlaques.muf * echangeurAPlaques.prof.cp / echangeurAPlaques.lambdaf) ^ 0.4 * echangeurAPlaques.lambdaf
16/43 (10): ThermoSysPro.Properties.WaterSteam.Common.ThermoProperties_ph(echangeurAPlaques.Tmf, echangeurAPlaques.rhof, echangeurAPlaques.prof.u, echangeurAPlaques.prof.s, echangeurAPlaques.prof.cp, echangeurAPlaques.prof.ddhp, echangeurAPlaques.prof.ddph, echangeurAPlaques.prof.duph, echangeurAPlaques.prof.duhp, echangeurAPlaques.prof.x) = $cse24
17/53 (1): 0.0 = if abs(sourceP3.Q0) > 0.001 then echangeurAPlaques.W - sourceP3.Q0 * echangeurAPlaques.prof.cp * (echangeurAPlaques.Tsf - echangeurAPlaques.Tef) else echangeurAPlaques.Tef - echangeurAPlaques.Tsf
18/54 (1): 0.0 = if abs(sourceP2.Q0) > 0.001 then echangeurAPlaques.W - sourceP2.Q0 * echangeurAPlaques.proc.cp * (echangeurAPlaques.Tec - echangeurAPlaques.Tsc) else echangeurAPlaques.Tec - echangeurAPlaques.Tsc
19/55 (10): $cse26 = ThermoSysPro.Properties.Fluid.Ph(puitsP2.P, echangeurAPlaques.Sc.h, echangeurAPlaques.mode_c, echangeurAPlaques.fluid_f)
20/65 (10): ThermoSysPro.Properties.WaterSteam.Common.ThermoProperties_ph(echangeurAPlaques.Tsc, echangeurAPlaques.procs.d, echangeurAPlaques.procs.u, echangeurAPlaques.procs.s, echangeurAPlaques.procs.cp, echangeurAPlaques.procs.ddhp, echangeurAPlaques.procs.ddph, echangeurAPlaques.procs.duph, echangeurAPlaques.procs.duhp, echangeurAPlaques.procs.x) = $cse26
21/75 (1): echangeurAPlaques.Hmc = 0.5 * (sourceP2.C.h + echangeurAPlaques.Sc.h)
22/76 (10): $cse23 = ThermoSysPro.Properties.Fluid.Ph(echangeurAPlaques.Pmc, echangeurAPlaques.Hmc, echangeurAPlaques.mode_c, echangeurAPlaques.fluid_c)
23/86 (1): echangeurAPlaques.lambdac = ThermoSysPro.Properties.Fluid.ThermalConductivity_rhoT(echangeurAPlaques.rhoc, echangeurAPlaques.Tmc, echangeurAPlaques.Pmc, 0, echangeurAPlaques.fluid_c)
24/87 (10): ThermoSysPro.Properties.WaterSteam.Common.ThermoProperties_ph(echangeurAPlaques.Tmc, echangeurAPlaques.rhoc, echangeurAPlaques.proc.u, echangeurAPlaques.proc.s, echangeurAPlaques.proc.cp, echangeurAPlaques.proc.ddhp, echangeurAPlaques.proc.ddph, echangeurAPlaques.proc.duph, echangeurAPlaques.proc.duhp, echangeurAPlaques.proc.x) = $cse23
25/97 (1): echangeurAPlaques.Pmc = 0.5 * (sourceP2.P0 + puitsP2.P)
26/98 (1): echangeurAPlaques.DT2 = echangeurAPlaques.Tsc - echangeurAPlaques.Tef
27/99 (1): echangeurAPlaques.DPf = if noEvent(echangeurAPlaques.qmf < 0.001) then 0.0 else 14423.2 / (echangeurAPlaques.rhof * echangeurAPlaques.qmf ^ 0.097) * echangeurAPlaques.quf ^ 2.0 * (1472.47 + 0.77 * (echangeurAPlaques.N - 1.0) + 104.97 / echangeurAPlaques.qmf ^ 0.25)
28/100 (1): echangeurAPlaques.qmf = abs(sourceP3.Q0) / (echangeurAPlaques.muf * echangeurAPlaques.N)
29/101 (1): echangeurAPlaques.Pmf = 0.5 * (sourceP3.P0 + puitsP3.P)
30/102 (1): puitsP3.P = if sourceP3.Q0 > 0.0 then sourceP3.P0 - echangeurAPlaques.DPf else sourceP3.P0 + echangeurAPlaques.DPf
31/103 (1): echangeurAPlaques.qmc = abs(sourceP2.Q0) / (echangeurAPlaques.muc * echangeurAPlaques.N)

Variables:
1: echangeurAPlaques.qmc:VARIABLE()  type: Real
2: echangeurAPlaques.DPf:VARIABLE(unit = "Pa" )  "Pressure loss of the cold fluid" type: Real
3: puitsP3.P:VARIABLE(min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 )  "Fluid pressure" type: Real
4: echangeurAPlaques.muf:VARIABLE(min = 0.0 start = 0.001 unit = "Pa.s" )  "Cold fluid dynamic viscosity" type: Real
5: echangeurAPlaques.qmf:VARIABLE()  type: Real
6: echangeurAPlaques.DT2:VARIABLE(unit = "K" )  "Temperature difference at the outlet of the exchanger" type: Real
7: puitsP2.P:VARIABLE(min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 )  "Fluid pressure" type: Real
8: echangeurAPlaques.proc.ddhp:VARIABLE(unit = "kg.s2/m5" )  "Derivative of density wrt. specific enthalpy at constant pressure" type: Real
9: $cse23.duph:VARIABLE(protected = true )  type: Real unreplaceable
10: echangeurAPlaques.proc.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific entropy" type: Real
11: echangeurAPlaques.proc.duph:VARIABLE(unit = "m3/kg" )  "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real
12: echangeurAPlaques.proc.x:VARIABLE(min = 0.0 max = 1.0 unit = "1" )  "Vapor mass fraction" type: Real
13: echangeurAPlaques.lambdac:VARIABLE(start = 0.602698 unit = "W/(m.K)" )  "Hot fluid thermal conductivity" type: Real
14: echangeurAPlaques.Tmc:VARIABLE(min = 200.0 max = 6000.0 start = 290.0 unit = "K" nominal = 300.0 )  "Hot fluid average temperature" type: Real
15: echangeurAPlaques.proc.ddph:VARIABLE(unit = "s2/m2" )  "Derivative of density wrt. pressure at constant specific enthalpy" type: Real
16: echangeurAPlaques.proc.duhp:VARIABLE(unit = "1" )  "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real
17: echangeurAPlaques.proc.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific heat capacity at constant presure" type: Real
18: echangeurAPlaques.proc.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 )  "Specific inner energy" type: Real
19: $cse23.u:VARIABLE(protected = true )  type: Real unreplaceable
20: $cse23.s:VARIABLE(protected = true )  type: Real unreplaceable
21: $cse23.ddhp:VARIABLE(protected = true )  type: Real unreplaceable
22: echangeurAPlaques.Pmc:VARIABLE(min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 )  "Hot fluid average pressure" type: Real
23: $cse23.d:VARIABLE(protected = true )  type: Real unreplaceable
24: $cse23.duhp:VARIABLE(protected = true )  type: Real unreplaceable
25: $cse23.T:VARIABLE(protected = true )  type: Real unreplaceable
26: $cse23.x:VARIABLE(protected = true )  type: Real unreplaceable
27: $cse23.cp:VARIABLE(protected = true )  type: Real unreplaceable
28: $cse23.ddph:VARIABLE(protected = true )  type: Real unreplaceable
29: echangeurAPlaques.Hmc:VARIABLE(start = 1e5 unit = "J/kg" )  "Hot fluid average specific enthalpy" type: Real
30: echangeurAPlaques.procs.x:VARIABLE(min = 0.0 max = 1.0 unit = "1" )  "Vapor mass fraction" type: Real
31: echangeurAPlaques.procs.ddhp:VARIABLE(unit = "kg.s2/m5" )  "Derivative of density wrt. specific enthalpy at constant pressure" type: Real
32: echangeurAPlaques.procs.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific entropy" type: Real
33: echangeurAPlaques.procs.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 )  "Specific inner energy" type: Real
34: echangeurAPlaques.procs.duph:VARIABLE(unit = "m3/kg" )  "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real
35: $cse26.d:VARIABLE(protected = true )  type: Real unreplaceable
36: $cse26.u:VARIABLE(protected = true )  type: Real unreplaceable
37: $cse26.duph:VARIABLE(protected = true )  type: Real unreplaceable
38: $cse26.x:VARIABLE(protected = true )  type: Real unreplaceable
39: $cse26.ddhp:VARIABLE(protected = true )  type: Real unreplaceable
40: $cse26.cp:VARIABLE(protected = true )  type: Real unreplaceable
41: $cse26.duhp:VARIABLE(protected = true )  type: Real unreplaceable
42: echangeurAPlaques.Sc.h:VARIABLE(flow=false start = 1e5 unit = "J/kg" )  "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real
43: $cse26.ddph:VARIABLE(protected = true )  type: Real unreplaceable
44: $cse26.s:VARIABLE(protected = true )  type: Real unreplaceable
45: $cse26.T:VARIABLE(protected = true )  type: Real unreplaceable
46: echangeurAPlaques.procs.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 )  "Density" type: Real
47: echangeurAPlaques.procs.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific heat capacity at constant presure" type: Real
48: echangeurAPlaques.procs.ddph:VARIABLE(unit = "s2/m2" )  "Derivative of density wrt. pressure at constant specific enthalpy" type: Real
49: echangeurAPlaques.procs.duhp:VARIABLE(unit = "1" )  "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real
50: echangeurAPlaques.Tsc:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 300.0 )  "Fluid temperature at the hot outlet" type: Real
51: echangeurAPlaques.W:VARIABLE(unit = "W" )  "Thermal power exchanged between the two sides" type: Real
52: echangeurAPlaques.prof.x:VARIABLE(min = 0.0 max = 1.0 unit = "1" )  "Vapor mass fraction" type: Real
53: $cse24.duhp:VARIABLE(protected = true )  type: Real unreplaceable
54: echangeurAPlaques.prof.ddph:VARIABLE(unit = "s2/m2" )  "Derivative of density wrt. pressure at constant specific enthalpy" type: Real
55: echangeurAPlaques.prof.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific entropy" type: Real
56: echangeurAPlaques.prof.duhp:VARIABLE(unit = "1" )  "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real
57: echangeurAPlaques.prof.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific heat capacity at constant presure" type: Real
58: echangeurAPlaques.prof.ddhp:VARIABLE(unit = "kg.s2/m5" )  "Derivative of density wrt. specific enthalpy at constant pressure" type: Real
59: echangeurAPlaques.hf:VARIABLE(unit = "W/(m2.K)" )  "Heat transfer coefficient of the cold fluid" type: Real
60: echangeurAPlaques.lambdaf:VARIABLE(start = 0.597928 unit = "W/(m.K)" )  "Cold fluid thermal conductivity" type: Real
61: echangeurAPlaques.Tmf:VARIABLE(min = 200.0 max = 6000.0 start = 290.0 unit = "K" nominal = 300.0 )  "Cold fluid average temperature" type: Real
62: echangeurAPlaques.rhof:VARIABLE(min = 1e-9 max = 1e5 start = 998.0 unit = "kg/m3" nominal = 998.0 )  "Cold fluid density" type: Real
63: echangeurAPlaques.prof.duph:VARIABLE(unit = "m3/kg" )  "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real
64: echangeurAPlaques.prof.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 )  "Specific inner energy" type: Real
65: $cse24.ddph:VARIABLE(protected = true )  type: Real unreplaceable
66: $cse24.cp:VARIABLE(protected = true )  type: Real unreplaceable
67: echangeurAPlaques.Pmf:VARIABLE(min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 )  "Cold fluid average pressure" type: Real
68: $cse24.ddhp:VARIABLE(protected = true )  type: Real unreplaceable
69: $cse24.d:VARIABLE(protected = true )  type: Real unreplaceable
70: $cse24.duph:VARIABLE(protected = true )  type: Real unreplaceable
71: $cse24.T:VARIABLE(protected = true )  type: Real unreplaceable
72: $cse24.s:VARIABLE(protected = true )  type: Real unreplaceable
73: $cse24.x:VARIABLE(protected = true )  type: Real unreplaceable
74: $cse24.u:VARIABLE(protected = true )  type: Real unreplaceable
75: echangeurAPlaques.Hmf:VARIABLE(start = 1e5 unit = "J/kg" )  "Cold fluid average specific enthalpy" type: Real
76: echangeurAPlaques.profs.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific heat capacity at constant presure" type: Real
77: echangeurAPlaques.profs.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 )  "Specific inner energy" type: Real
78: echangeurAPlaques.profs.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific entropy" type: Real
79: echangeurAPlaques.profs.x:VARIABLE(min = 0.0 max = 1.0 unit = "1" )  "Vapor mass fraction" type: Real
80: $cse28.duph:VARIABLE(protected = true )  type: Real unreplaceable
81: $cse28.ddph:VARIABLE(protected = true )  type: Real unreplaceable
82: echangeurAPlaques.Sf.h:VARIABLE(flow=false start = 1e5 unit = "J/kg" )  "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real
83: $cse28.duhp:VARIABLE(protected = true )  type: Real unreplaceable
84: $cse28.ddhp:VARIABLE(protected = true )  type: Real unreplaceable
85: $cse28.s:VARIABLE(protected = true )  type: Real unreplaceable
86: $cse28.cp:VARIABLE(protected = true )  type: Real unreplaceable
87: $cse28.d:VARIABLE(protected = true )  type: Real unreplaceable
88: $cse28.T:VARIABLE(protected = true )  type: Real unreplaceable
89: $cse28.u:VARIABLE(protected = true )  type: Real unreplaceable
90: $cse28.x:VARIABLE(protected = true )  type: Real unreplaceable
91: echangeurAPlaques.profs.duph:VARIABLE(unit = "m3/kg" )  "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real
92: echangeurAPlaques.profs.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 )  "Density" type: Real
93: echangeurAPlaques.profs.duhp:VARIABLE(unit = "1" )  "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real
94: echangeurAPlaques.profs.ddph:VARIABLE(unit = "s2/m2" )  "Derivative of density wrt. pressure at constant specific enthalpy" type: Real
95: echangeurAPlaques.profs.ddhp:VARIABLE(unit = "kg.s2/m5" )  "Derivative of density wrt. specific enthalpy at constant pressure" type: Real
96: echangeurAPlaques.Tsf:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 300.0 )  "Fluid temperature at the cold outlet" type: Real
97: echangeurAPlaques.DT1:VARIABLE(unit = "K" )  "Temperature difference at the inlet of the exchanger" type: Real
98: echangeurAPlaques.DTm:VARIABLE(unit = "K" )  "Difference in average temperature" type: Real
99: echangeurAPlaques.K:VARIABLE(unit = "W/(m2.K)" )  "Global heat transfer coefficient" type: Real
100: echangeurAPlaques.hc:VARIABLE(unit = "W/(m2.K)" )  "Heat transfer coefficient of the hot fluid" type: Real
101: echangeurAPlaques.muc:VARIABLE(min = 0.0 start = 0.001 unit = "Pa.s" )  "Hot fluid dynamic viscosity" type: Real
102: echangeurAPlaques.rhoc:VARIABLE(min = 1e-9 max = 1e5 start = 998.0 unit = "kg/m3" nominal = 998.0 )  "Hot fluid density" type: Real
103: echangeurAPlaques.DPc:VARIABLE(unit = "Pa" )  "Pressure loss of the hot fluid" 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 0.002619/3.868, allocations: 3.993 MB / 1.412 GB, free: 32.52 MB / 0.8262 GB
Error: post-optimization module createDAEmodeBDAE (simulation) failed.
Error: Internal error SimCode DAEmode: The model ThermoSysPro.Fluid.Examples.SimpleExamples.TestDynamicPlateHeatExchanger could not be translated