Running: ./testmodel.py --libraries=/home/hudson/saved_omc/libraries/.openmodelica/libraries --ompython_omhome=/usr ThermoSysPro_ThermoSysPro.Fluid.Examples.SimpleExamples.TestStaticCondenserHEI.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.TestStaticCondenserHEI,tolerance=1e-06,outputFormat="empty",numberOfIntervals=5000,variableFilter="",fileNamePrefix="ThermoSysPro_ThermoSysPro.Fluid.Examples.SimpleExamples.TestStaticCondenserHEI")
translateModel(ThermoSysPro.Fluid.Examples.SimpleExamples.TestStaticCondenserHEI,tolerance=1e-06,outputFormat="empty",numberOfIntervals=5000,variableFilter="",fileNamePrefix="ThermoSysPro_ThermoSysPro.Fluid.Examples.SimpleExamples.TestStaticCondenserHEI")
Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermoSysPro 4.0.0-master/package.mo): time 0.8264/0.8264, allocations: 150.9 MB / 167.2 MB, free: 14.53 MB / 142.1 MB
Notification: Performance of FrontEnd - loaded program: time 0.0003532/0.0003532, allocations: 16 kB / 237.8 MB, free: 1.766 MB / 190.1 MB
Notification: Performance of FrontEnd - Absyn->SCode: time 0.05331/0.05368, allocations: 31.35 MB / 269.1 MB, free: 7.027 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.TestStaticCondenserHEI): time 1.654/1.708, allocations: 300.8 MB / 0.5566 GB, free: 7.059 MB / 446.1 MB
Notification: Performance of NFInst.instExpressions: time 0.5386/2.247, allocations: 193 MB / 0.7451 GB, free: 1.75 MB / 0.5919 GB
Notification: Performance of NFInst.updateImplicitVariability: time 0.001047/2.248, allocations: 31.75 kB / 0.7451 GB, free: 1.75 MB / 0.5919 GB
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermoSysPro 4.0.0-master/Fluid/BoundaryConditions/SourceQ.mo:62:3-63:65: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).
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermoSysPro 4.0.0-master/Fluid/HeatExchangers/StaticCondenserHEI.mo:171:3-173:24:writable] Warning: Connector Cee 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/StaticCondenserHEI.mo:174:3-176:38:writable] Warning: Connector Cse 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/StaticCondenserHEI.mo:177:3-179:66:writable] Warning: Connector Cex 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/StaticCondenserHEI.mo:180:3-182:57:writable] Warning: Connector Cvt 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/StaticCondenserHEI.mo:202:3-203:83:writable] Warning: Connector Cep 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/StaticCondenserHEI.mo:205:3-207:17:writable] Warning: Connector Cev 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/PressureLosses/SingularPressureLoss.mo:27:3-28:67:writable] Warning: Connector C1 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/PressureLosses/SingularPressureLoss.mo:29:3-30:65:writable] Warning: Connector C2 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/PressureLosses/SingularPressureLoss.mo:27:3-28:67:writable] Warning: Connector C1 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/PressureLosses/SingularPressureLoss.mo:29:3-30:65:writable] Warning: Connector C2 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/PressureLosses/SingularPressureLoss.mo:27:3-28:67:writable] Warning: Connector C1 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/PressureLosses/SingularPressureLoss.mo:29:3-30:65:writable] Warning: Connector C2 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/PressureLosses/SingularPressureLoss.mo:27:3-28:67:writable] Warning: Connector C1 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/PressureLosses/SingularPressureLoss.mo:29:3-30:65:writable] Warning: Connector C2 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/PressureLosses/SingularPressureLoss.mo:27:3-28:67:writable] Warning: Connector C1 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/PressureLosses/SingularPressureLoss.mo:29:3-30:65:writable] Warning: Connector C2 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/PressureLosses/SingularPressureLoss.mo:27:3-28:67:writable] Warning: Connector C1 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/PressureLosses/SingularPressureLoss.mo:29:3-30:65:writable] Warning: Connector C2 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 0.0009058/2.249, allocations: 355.1 kB / 0.7455 GB, free: 1.75 MB / 0.5919 GB
Notification: Performance of NFTyping.typeBindings: time 0.001524/2.25, allocations: 0.6942 MB / 0.7462 GB, free: 1.746 MB / 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 0.03268/2.283, allocations: 12.73 MB / 0.7586 GB, free: 1.473 MB / 0.5919 GB
Notification: Performance of NFFlatten.flatten: time 0.002854/2.286, allocations: 2.533 MB / 0.7611 GB, free: 1.465 MB / 0.5919 GB
Notification: Performance of NFFlatten.resolveConnections: time 0.001282/2.287, allocations: 1.275 MB / 0.7623 GB, free: 1.289 MB / 0.5919 GB
Notification: Performance of NFEvalConstants.evaluate: time 0.001437/2.288, allocations: 1.032 MB / 0.7633 GB, free: 1.285 MB / 0.5919 GB
Notification: Performance of NFSimplifyModel.simplify: time 0.0009418/2.289, allocations: 1.083 MB / 0.7644 GB, free: 1.207 MB / 0.5919 GB
Notification: Performance of NFPackage.collectConstants: time 0.0002291/2.29, allocations: 215.6 kB / 0.7646 GB, free: 1.207 MB / 0.5919 GB
Notification: Performance of NFFlatten.collectFunctions: time 0.04081/2.33, allocations: 21.52 MB / 0.7856 GB, free: 14.05 MB / 0.6075 GB
Notification: Performance of NFScalarize.scalarize: time 0.0009769/2.331, allocations: 476.5 kB / 0.786 GB, free: 13.89 MB / 0.6075 GB
Notification: Performance of NFVerifyModel.verify: time 0.002198/2.334, allocations: 1.143 MB / 0.7872 GB, free: 13.49 MB / 0.6075 GB
Notification: Performance of NFConvertDAE.convert: time 0.04481/2.378, allocations: 12.6 MB / 0.7995 GB, free: 6.84 MB / 0.6075 GB
Notification: Performance of FrontEnd - DAE generated: time 7.153e-06/2.379, allocations: 0 / 0.7995 GB, free: 6.84 MB / 0.6075 GB
Notification: Performance of FrontEnd: time 2.314e-06/2.379, allocations: 1.031 kB / 0.7995 GB, free: 6.84 MB / 0.6075 GB
Notification: Performance of Transformations before backend: time 0.0001333/2.379, allocations: 0 / 0.7995 GB, free: 6.84 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: 569
 * Number of variables: 569
Notification: Performance of Generate backend data structure: time 0.01542/2.394, allocations: 3.568 MB / 0.803 GB, free: 3.629 MB / 0.6075 GB
Notification: Performance of prepare preOptimizeDAE: time 4.934e-05/2.394, allocations: 8.031 kB / 0.803 GB, free: 3.621 MB / 0.6075 GB
Notification: Performance of preOpt normalInlineFunction (simulation): time 0.0007577/2.395, allocations: 250.1 kB / 0.8032 GB, free: 3.375 MB / 0.6075 GB
Notification: Performance of preOpt evaluateParameters (simulation): time 0.002219/2.397, allocations: 0.9239 MB / 0.8041 GB, free: 2.484 MB / 0.6075 GB
Notification: Performance of preOpt simplifyIfEquations (simulation): time 0.0002941/2.397, allocations: 208.4 kB / 0.8043 GB, free: 2.266 MB / 0.6075 GB
Notification: Performance of preOpt expandDerOperator (simulation): time 0.0003681/2.398, allocations: 192.9 kB / 0.8045 GB, free: 2.078 MB / 0.6075 GB
Notification: Performance of preOpt clockPartitioning (simulation): time 0.005206/2.403, allocations: 2.126 MB / 0.8066 GB, free: 15.81 MB / 0.6231 GB
Notification: Performance of preOpt findStateOrder (simulation): time 6.018e-05/2.403, allocations: 7.438 kB / 0.8066 GB, free: 15.8 MB / 0.6231 GB
Notification: Performance of preOpt replaceEdgeChange (simulation): time 0.0002615/2.403, allocations: 87.94 kB / 0.8067 GB, free: 15.72 MB / 0.6231 GB
Notification: Performance of preOpt inlineArrayEqn (simulation): time 8.763e-05/2.404, allocations: 64.78 kB / 0.8067 GB, free: 15.66 MB / 0.6231 GB
Notification: Performance of preOpt removeEqualRHS (simulation): time 0.004232/2.408, allocations: 1.566 MB / 0.8082 GB, free: 14.12 MB / 0.6231 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 0.2667/2.675, allocations: 138.1 MB / 0.9431 GB, free: 3.934 MB / 0.7637 GB
Notification: Performance of preOpt comSubExp (simulation): time 0.001261/2.676, allocations: 0.8067 MB / 0.9439 GB, free: 3.098 MB / 0.7637 GB
Notification: Performance of preOpt resolveLoops (simulation): time 0.0006202/2.676, allocations: 442.7 kB / 0.9443 GB, free: 2.648 MB / 0.7637 GB
Notification: Performance of preOpt evalFunc (simulation): time 0.8001/3.477, allocations: 241.1 MB / 1.18 GB, free: 70.96 MB / 0.8262 GB
Notification: Performance of preOpt encapsulateWhenConditions (simulation): time 3.814e-05/3.477, allocations: 56.3 kB / 1.18 GB, free: 70.91 MB / 0.8262 GB
Notification: Performance of pre-optimization done (n=132): time 3.136e-06/3.477, allocations: 0 / 1.18 GB, free: 70.91 MB / 0.8262 GB
Notification: Performance of matching and sorting (n=132): time 0.0113/3.488, allocations: 3.605 MB / 1.183 GB, free: 67.84 MB / 0.8262 GB
Notification: Performance of inlineWhenForInitialization (initialization): time 3.272e-05/3.488, allocations: 168.2 kB / 1.183 GB, free: 67.64 MB / 0.8262 GB
Notification: Performance of selectInitializationVariablesDAE (initialization): time 0.001292/3.489, allocations: 1.172 MB / 1.185 GB, free: 66.82 MB / 0.8262 GB
Notification: Performance of collectPreVariables (initialization): time 4.163e-05/3.489, allocations: 42.64 kB / 1.185 GB, free: 66.78 MB / 0.8262 GB
Notification: Performance of collectInitialEqns (initialization): time 0.0003752/3.49, allocations: 0.918 MB / 1.186 GB, free: 66.18 MB / 0.8262 GB
Notification: Performance of collectInitialBindings (initialization): time 0.0002159/3.49, allocations: 457.6 kB / 1.186 GB, free: 65.8 MB / 0.8262 GB
Notification: Performance of simplifyInitialFunctions (initialization): time 0.0004052/3.49, allocations: 377.5 kB / 1.186 GB, free: 65.55 MB / 0.8262 GB
Notification: Performance of setup shared object (initialization): time 4.664e-05/3.49, allocations: 301.7 kB / 1.187 GB, free: 65.26 MB / 0.8262 GB
Notification: Performance of preBalanceInitialSystem (initialization): time 0.0007547/3.491, allocations: 469.2 kB / 1.187 GB, free: 64.97 MB / 0.8262 GB
Notification: Performance of partitionIndependentBlocks (initialization): time 0.0009577/3.492, allocations: 1.018 MB / 1.188 GB, free: 63.92 MB / 0.8262 GB
Notification: Performance of analyzeInitialSystem (initialization): time 0.001674/3.494, allocations: 1.543 MB / 1.19 GB, free: 62.64 MB / 0.8262 GB
Notification: Performance of solveInitialSystemEqSystem (initialization): time 1.033e-05/3.494, allocations: 8 kB / 1.19 GB, free: 62.63 MB / 0.8262 GB
Notification: Performance of matching and sorting (n=259) (initialization): time 0.003618/3.497, allocations: 2.182 MB / 1.192 GB, free: 61.14 MB / 0.8262 GB
Notification: Performance of prepare postOptimizeDAE: time 2.363e-05/3.498, allocations: 12.97 kB / 1.192 GB, free: 61.12 MB / 0.8262 GB
Notification: Performance of postOpt simplifyComplexFunction (initialization): time 2.815e-05/3.498, allocations: 20 kB / 1.192 GB, free: 61.11 MB / 0.8262 GB
Notification: Performance of postOpt tearingSystem (initialization): time 0.005025/3.503, allocations: 1.652 MB / 1.193 GB, free: 59.61 MB / 0.8262 GB
Notification: Performance of postOpt solveSimpleEquations (initialization): time 0.0007411/3.503, allocations: 240 kB / 1.194 GB, free: 59.4 MB / 0.8262 GB
Notification: Performance of postOpt calculateStrongComponentJacobians (initialization): time 0.002554/3.506, allocations: 4.6 MB / 1.198 GB, free: 55.04 MB / 0.8262 GB
Notification: Performance of postOpt simplifyAllExpressions (initialization): time 0.001259/3.507, allocations: 217.5 kB / 1.198 GB, free: 54.85 MB / 0.8262 GB
Notification: Performance of postOpt collapseArrayExpressions (initialization): time 9.17e-05/3.507, allocations: 82.3 kB / 1.198 GB, free: 54.78 MB / 0.8262 GB
Notification: Model statistics after passing the back-end for initialization:
 * Number of independent subsystems: 81
 * Number of states: 0 ()
 * Number of discrete variables: 36 (condenseur.Cex.ftype,Source_condenseur.C.ftype,sourceP.C.ftype,sourceP2.C.ftype,sourceP1.C.ftype,Puit_condenseur.fluid,condenseur.fluid_p,singularPressureLoss.fluid,singularPressureLoss1.fluid,singularPressureLoss2.fluid,singularPressureLoss3.fluid,Puit_condenseur1.fluid,singularPressureLoss4.fluid,singularPressureLoss5.fluid,condenseur.HEI,sourceP2.fluid1,sourceP1.fluid1,sourceP.fluid1,Source_condenseur.fluid1,singularPressureLoss5.C1.diff_on_2,condenseur.Cex.diff_on_1,singularPressureLoss5.C2.diff_on_1,condenseur.Cee.diff_on_2,Source_condenseur.C.diff_on_2,condenseur.Cse.diff_on_1,singularPressureLoss4.C2.diff_on_1,condenseur.Cvt.diff_on_2,sourceP.C.diff_on_2,singularPressureLoss3.C2.diff_on_1,condenseur.Cep.diff_on_2,sourceP2.C.diff_on_2,singularPressureLoss1.C2.diff_on_1,condenseur.Cev.diff_on_2,sourceP1.C.diff_on_2,singularPressureLoss.C2.diff_on_1,condenseur.fluids[1])
 * Number of discrete states: 0 ()
 * Number of clocked states: 0 ()
 * Top-level inputs: 0
Notification: Strong component statistics for initialization (157):
 * Single equations (assignments): 148
 * Array equations: 0
 * Algorithm blocks: 0
 * Record equations: 2
 * When equations: 0
 * If-equations: 0
 * Equation systems (not torn): 0
 * Torn equation systems: 7
 * 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): 7 systems
   {(1,3), (1,2), (1,3), (1,3), (1,3), (1,3), (4,24)}
Notification: Performance of prepare postOptimizeDAE: time 0.0005086/3.508, allocations: 364.7 kB / 1.199 GB, free: 54.55 MB / 0.8262 GB
Notification: Performance of postOpt lateInlineFunction (simulation): time 0.0002273/3.508, allocations: 139.2 kB / 1.199 GB, free: 54.42 MB / 0.8262 GB
Notification: Performance of postOpt wrapFunctionCalls (simulation): time 0.00248/3.511, allocations: 1.934 MB / 1.201 GB, free: 53.18 MB / 0.8262 GB
Notification: Performance of postOpt simplifysemiLinear (simulation): time 1.067e-05/3.511, allocations: 7.984 kB / 1.201 GB, free: 53.18 MB / 0.8262 GB
Notification: Performance of postOpt simplifyComplexFunction (simulation): time 7.645e-06/3.511, allocations: 4 kB / 1.201 GB, free: 53.17 MB / 0.8262 GB
Notification: Performance of postOpt removeConstants (simulation): time 0.0003995/3.511, allocations: 316.1 kB / 1.201 GB, free: 52.89 MB / 0.8262 GB
Notification: Performance of postOpt simplifyTimeIndepFuncCalls (simulation): time 0.0001312/3.511, allocations: 22.17 kB / 1.201 GB, free: 52.88 MB / 0.8262 GB
Notification: Performance of postOpt simplifyAllExpressions (simulation): time 0.0006795/3.512, allocations: 23.08 kB / 1.201 GB, free: 52.86 MB / 0.8262 GB
Notification: Performance of postOpt findZeroCrossings (simulation): time 0.0001233/3.512, allocations: 64.2 kB / 1.201 GB, free: 52.81 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(condenseur.Tef, condenseur.profe.d, condenseur.profe.u, condenseur.profe.s, condenseur.profe.cp, condenseur.profe.ddhp, condenseur.profe.ddph, condenseur.profe.duph, condenseur.profe.duhp, condenseur.profe.x) = $cse4

Variables:
1: condenseur.profe.duhp:VARIABLE(unit = "1" )  "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real
2: condenseur.profe.duph:VARIABLE(unit = "m3/kg" )  "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real
3: condenseur.profe.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific entropy" type: Real
4: condenseur.Fw:VARIABLE()  "Correction factor for water" type: Real
5: condenseur.Tcut_off:VARIABLE(min = 0.0 start = 288.15 unit = "K" nominal = 300.0 )  "Saturation temperature at pressure cut-off" type: Real
6: condenseur.Pcut_off:VARIABLE(unit = "Pa" )  "Pressure cut-off" type: Real
7: condenseur.Pzero_load:VARIABLE(unit = "Pa" )  "Zero-load pressure " type: Real
8: singularPressureLoss.Pm:VARIABLE(min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 )  "Average fluid pressure" type: Real
9: singularPressureLoss1.deltaP:VARIABLE(unit = "Pa" )  "Singular pressure loss" type: Real
10: singularPressureLoss1.Pm:VARIABLE(min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 )  "Average fluid pressure" type: Real
[/var/lib/jenkins1/ws/OpenModelicaLibraryTestingWork/OpenModelica/OMCompiler/Compiler/BackEnd/DAEMode.mo:528:7-530:90:writable] Error: Internal error DAEMode.traverserStrongComponents failed on equation:
1/1 (10): $cse4 = ThermoSysPro.Properties.Fluid.Ph(singularPressureLoss2.C2.P, singularPressureLoss2.h, condenseur.mode_f, condenseur.fluid_p)
2/11 (1): condenseur.Tcut_off = condenseur.Tef + condenseur.Wcut_off / (Source_condenseur.Q0 * condenseur.Cpmf * (1.0 - $cse7))
3/12 (1): condenseur.Pcond = if condenseur.Psat_att < condenseur.Pcut_off then (condenseur.Pcut_off - condenseur.Pzero_load) * condenseur.W / condenseur.Wcut_off + condenseur.Pzero_load + condenseur.Poffset else condenseur.Psat_att + condenseur.Poffset
4/13 (1): condenseur.Psat_att = ThermoSysPro.Properties.Fluid.P_sat(condenseur.Tsat_att, condenseur.fluid)
5/14 (1): condenseur.Tsat_att = condenseur.Tef + condenseur.W / (Source_condenseur.Q0 * condenseur.Cpmf * (1.0 - $cse7))
6/15 (1): condenseur.W = Source_condenseur.Q0 * (singularPressureLoss4.h - singularPressureLoss2.h)
7/16 (10): $cse6 = ThermoSysPro.Properties.Fluid.Ph(0.5 * (singularPressureLoss2.C2.P + condenseur.Cse.P), 0.5 * (singularPressureLoss2.h + singularPressureLoss4.h), condenseur.mode_f, condenseur.fluid_p)
8/26 (1): singularPressureLoss2.C2.P - condenseur.Cse.P = condenseur.DPf
9/27 (1): condenseur.DPf = condenseur.DPff + condenseur.DPgf
10/28 (1): condenseur.DPgf = 9.80665 * condenseur.rhof * (condenseur.z2f - condenseur.z1f)
11/29 (1): condenseur.Vf = Source_condenseur.Q0 / (condenseur.rhof * condenseur.S_pass)
12/30 (1): condenseur.U1 = ThermoSysPro.Correlations.Thermal.Function_U1(condenseur.D_tubes, condenseur.Vf)
13/31 (1): condenseur.U = condenseur.Ucorr * condenseur.U1 * condenseur.FM * condenseur.FC * condenseur.Fw
14/32 (1): $cse7 = exp((-condenseur.U) * condenseur.S_ech / (Source_condenseur.Q0 * condenseur.Cpmf))
15/33 (10): ThermoSysPro.Properties.WaterSteam.Common.ThermoProperties_ph(condenseur.promf.T, condenseur.rhof, condenseur.promf.u, condenseur.promf.s, condenseur.Cpmf, condenseur.promf.ddhp, condenseur.promf.ddph, condenseur.promf.duph, condenseur.promf.duhp, condenseur.promf.x) = $cse6
16/43 (1): condenseur.DPff = condenseur.Kf * $cse1 / condenseur.rhof
17/44 (1): singularPressureLoss4.rho = ThermoSysPro.Properties.Fluid.Density_Ph(singularPressureLoss4.Pm, singularPressureLoss4.h, singularPressureLoss4.fluid, singularPressureLoss4.mode, 0.0, 0.0, 0.0, 0.0)
18/45 (1): singularPressureLoss4.Pm = 0.5 * (condenseur.Cse.P + Puit_condenseur.P0)
19/46 (1): singularPressureLoss4.deltaP = condenseur.Cse.P - Puit_condenseur.P0
20/47 (1): singularPressureLoss4.deltaP = singularPressureLoss4.K * $cse12 / singularPressureLoss4.rho
21/48 (1): 0.0 = singularPressureLoss3.Q * singularPressureLoss3.h + singularPressureLoss.Q * singularPressureLoss.h + singularPressureLoss1.Q * singularPressureLoss1.h + (-condenseur.W) - singularPressureLoss5.Q * singularPressureLoss5.h
22/49 (1): singularPressureLoss5.h = if singularPressureLoss5.Q > 0.0 then condenseur.Hml else 1e5
23/50 (1): 0.0 = singularPressureLoss3.Q + singularPressureLoss.Q + singularPressureLoss1.Q - singularPressureLoss5.Q
24/51 (1): $cse8 = ThermoSysPro.Functions.ThermoSquare(singularPressureLoss.Q, singularPressureLoss.eps)
25/52 (1): singularPressureLoss.deltaP = singularPressureLoss.K * $cse8 / singularPressureLoss.rho
26/53 (1): singularPressureLoss.deltaP = sourceP1.P0 - condenseur.Pcond
27/54 (14): (ThermoSysPro.Properties.WaterSteam.Common.PropThermoSat(condenseur.lsat.P, condenseur.lsat.T, condenseur.lsat.rho, condenseur.Hml, condenseur.lsat.cp, condenseur.lsat.pt, condenseur.lsat.cv), condenseur.vsat) = ThermoSysPro.Properties.Fluid.Water_sat_P(condenseur.Pcond, condenseur.fluid)
28/68 (1): singularPressureLoss1.h = if singularPressureLoss1.Q > 0.0 then 2.5055e6 else condenseur.Hml
29/69 (1): singularPressureLoss1.rho = ThermoSysPro.Properties.Fluid.Density_Ph(singularPressureLoss1.Pm, singularPressureLoss1.h, singularPressureLoss1.fluid, singularPressureLoss1.mode, 0.0, 0.0, 0.0, 0.0)
30/70 (1): singularPressureLoss1.deltaP = singularPressureLoss1.K * $cse9 / singularPressureLoss1.rho
31/71 (1): $cse9 = ThermoSysPro.Functions.ThermoSquare(singularPressureLoss1.Q, singularPressureLoss1.eps)
32/72 (1): singularPressureLoss.h = if singularPressureLoss.Q > 0.0 then 2.5481e6 else condenseur.Hml
33/73 (1): singularPressureLoss.rho = ThermoSysPro.Properties.Fluid.Density_Ph(singularPressureLoss.Pm, singularPressureLoss.h, singularPressureLoss.fluid, singularPressureLoss.mode, 0.0, 0.0, 0.0, 0.0)
34/74 (1): singularPressureLoss3.h = if singularPressureLoss3.Q > 0.0 then 2.5817e6 else condenseur.Hml
35/75 (1): singularPressureLoss3.rho = ThermoSysPro.Properties.Fluid.Density_Ph(singularPressureLoss3.Pm, singularPressureLoss3.h, singularPressureLoss3.fluid, singularPressureLoss3.mode, 0.0, 0.0, 0.0, 0.0)
36/76 (1): singularPressureLoss3.deltaP = singularPressureLoss3.K * $cse11 / singularPressureLoss3.rho
37/77 (1): $cse11 = ThermoSysPro.Functions.ThermoSquare(singularPressureLoss3.Q, singularPressureLoss3.eps)
38/78 (1): singularPressureLoss3.Pm = 0.5 * (sourceP.P0 + condenseur.Pcond)
39/79 (1): singularPressureLoss3.deltaP = sourceP.P0 - condenseur.Pcond
40/80 (1): singularPressureLoss1.Pm = 0.5 * (sourceP2.P0 + condenseur.Pcond)
41/81 (1): singularPressureLoss1.deltaP = sourceP2.P0 - condenseur.Pcond
42/82 (1): singularPressureLoss.Pm = 0.5 * (sourceP1.P0 + condenseur.Pcond)
43/83 (1): condenseur.Pzero_load = 100.0 * (10.27824 + 5.008e-4 * (-273.15 + condenseur.Tef) ^ 3.0 + 0.02039549 * (-273.15 + condenseur.Tef) ^ 2.0 + 0.2277566 * (-273.15 + condenseur.Tef))
44/84 (1): condenseur.Pcut_off = 100.0 * (21.09159 + 5.752433e-4 * (-273.15 + condenseur.Tef) ^ 3.0 + 0.01735162 * (-273.15 + condenseur.Tef) ^ 2.0 + 0.08052739 * (-273.15 + condenseur.Tef))
45/85 (1): condenseur.Tcut_off = ThermoSysPro.Properties.Fluid.T_sat(condenseur.Pcut_off, condenseur.fluid)
46/86 (1): condenseur.Fw = 0.6639699 + 0.01974994 * (-273.15 + condenseur.Tef) + (-2.104072e-4) * (-273.15 + condenseur.Tef) ^ 2.0
47/87 (10): ThermoSysPro.Properties.WaterSteam.Common.ThermoProperties_ph(condenseur.Tef, condenseur.profe.d, condenseur.profe.u, condenseur.profe.s, condenseur.profe.cp, condenseur.profe.ddhp, condenseur.profe.ddph, condenseur.profe.duph, condenseur.profe.duhp, condenseur.profe.x) = $cse4

Variables:
1: condenseur.profe.duhp:VARIABLE(unit = "1" )  "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real
2: condenseur.profe.duph:VARIABLE(unit = "m3/kg" )  "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real
3: condenseur.profe.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific entropy" type: Real
4: condenseur.Fw:VARIABLE()  "Correction factor for water" type: Real
5: condenseur.Tcut_off:VARIABLE(min = 0.0 start = 288.15 unit = "K" nominal = 300.0 )  "Saturation temperature at pressure cut-off" type: Real
6: condenseur.Pcut_off:VARIABLE(unit = "Pa" )  "Pressure cut-off" type: Real
7: condenseur.Pzero_load:VARIABLE(unit = "Pa" )  "Zero-load pressure " type: Real
8: singularPressureLoss.Pm:VARIABLE(min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 )  "Average fluid pressure" type: Real
9: singularPressureLoss1.deltaP:VARIABLE(unit = "Pa" )  "Singular pressure loss" type: Real
10: singularPressureLoss1.Pm:VARIABLE(min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 )  "Average fluid pressure" type: Real
11: singularPressureLoss3.deltaP:VARIABLE(unit = "Pa" )  "Singular pressure loss" type: Real
12: singularPressureLoss3.Pm:VARIABLE(min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 )  "Average fluid pressure" type: Real
13: singularPressureLoss3.Q:VARIABLE(start = 100.0 unit = "kg/s" fixed = true )  "Mass flow rate" type: Real
14: $cse11:VARIABLE(protected = true )  type: Real unreplaceable
15: singularPressureLoss3.rho:VARIABLE(min = 0.0 start = 998.0 unit = "kg/m3" )  "Fluid density" type: Real
16: singularPressureLoss3.h:VARIABLE(start = 1e5 unit = "J/kg" )  "Fluid specific enthalpy" type: Real
17: singularPressureLoss.rho:VARIABLE(min = 0.0 start = 998.0 unit = "kg/m3" )  "Fluid density" type: Real
18: singularPressureLoss.h:VARIABLE(start = 1e5 unit = "J/kg" )  "Fluid specific enthalpy" type: Real
19: singularPressureLoss1.Q:VARIABLE(start = 1e-5 unit = "kg/s" fixed = true )  "Mass flow rate" type: Real
20: $cse9:VARIABLE(protected = true )  type: Real unreplaceable
21: singularPressureLoss1.rho:VARIABLE(min = 0.0 start = 998.0 unit = "kg/m3" )  "Fluid density" type: Real
22: singularPressureLoss1.h:VARIABLE(start = 1e5 unit = "J/kg" )  "Fluid specific enthalpy" type: Real
23: condenseur.lsat.cv:VARIABLE(unit = "J/(kg.K)" )  "Specific heat capacity at constant volume" type: Real
24: condenseur.lsat.rho:VARIABLE(min = 0.0 unit = "kg/m3" )  "Density" type: Real
25: condenseur.lsat.P:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 )  "Pressure" type: Real
26: condenseur.vsat.P:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 )  "Pressure" type: Real
27: condenseur.vsat.T:VARIABLE(min = 0.0 start = 288.15 unit = "K" nominal = 300.0 )  "Temperature" type: Real
28: condenseur.vsat.pt:VARIABLE()  "Derivative of pressure wrt. temperature" type: Real
29: condenseur.lsat.cp:VARIABLE(unit = "J/(kg.K)" )  "Specific heat capacity at constant pressure" type: Real
30: condenseur.vsat.cv:VARIABLE(unit = "J/(kg.K)" )  "Specific heat capacity at constant volume" type: Real
31: condenseur.Hml:VARIABLE(start = 1e5 unit = "J/kg" )  "Extraction water average specific enthalpy" type: Real
32: condenseur.lsat.pt:VARIABLE()  "Derivative of pressure wrt. temperature" type: Real
33: condenseur.lsat.T:VARIABLE(min = 0.0 start = 288.15 unit = "K" nominal = 300.0 )  "Temperature" type: Real
34: condenseur.vsat.h:VARIABLE(unit = "J/kg" )  "Specific enthalpy" type: Real
35: condenseur.vsat.rho:VARIABLE(min = 0.0 unit = "kg/m3" )  "Density" type: Real
36: condenseur.vsat.cp:VARIABLE(unit = "J/(kg.K)" )  "Specific heat capacity at constant pressure" type: Real
37: condenseur.Pcond:VARIABLE(start = 2154.77 unit = "Pa" fixed = false )  "Expected corrected HEI saturation pressure" type: Real
38: singularPressureLoss.deltaP:VARIABLE(unit = "Pa" )  "Singular pressure loss" type: Real
39: $cse8:VARIABLE(protected = true )  type: Real unreplaceable
40: singularPressureLoss.Q:VARIABLE(start = 1e-5 unit = "kg/s" fixed = true )  "Mass flow rate" type: Real
41: singularPressureLoss5.h:VARIABLE(start = 1e5 unit = "J/kg" )  "Fluid specific enthalpy" type: Real
42: singularPressureLoss5.Q:VARIABLE(start = 100.0 unit = "kg/s" )  "Mass flow rate" type: Real
43: singularPressureLoss4.rho:VARIABLE(min = 0.0 start = 995.9727926518547 unit = "kg/m3" )  "Fluid density" type: Real
44: singularPressureLoss4.deltaP:VARIABLE(unit = "Pa" )  "Singular pressure loss" type: Real
45: condenseur.Cse.P:VARIABLE(flow=false start = 1e5 unit = "Pa" )  "Fluid pressure in the control volume" type: Real
46: singularPressureLoss4.Pm:VARIABLE(min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 )  "Average fluid pressure" type: Real
47: condenseur.DPff:VARIABLE(start = 1000.0 unit = "Pa" )  "Friction pressure loss in the cold side" type: Real
48: $cse6.x:VARIABLE(protected = true )  type: Real unreplaceable
49: condenseur.promf.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 )  "Specific inner energy" type: Real
50: condenseur.promf.duph:VARIABLE(unit = "m3/kg" )  "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real
51: condenseur.promf.ddhp:VARIABLE(unit = "kg.s2/m5" )  "Derivative of density wrt. specific enthalpy at constant pressure" type: Real
52: condenseur.promf.x:VARIABLE(min = 0.0 max = 1.0 unit = "1" )  "Vapor mass fraction" type: Real
53: condenseur.promf.T:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 320.0 )  "Temperature" type: Real
54: condenseur.promf.duhp:VARIABLE(unit = "1" )  "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real
55: condenseur.promf.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific entropy" type: Real
56: condenseur.promf.ddph:VARIABLE(unit = "s2/m2" )  "Derivative of density wrt. pressure at constant specific enthalpy" type: Real
57: condenseur.Cpmf:VARIABLE(min = 1e-9 max = 1e60 start = 950.0 unit = "J/(kg.K)" nominal = 1000.0 )  "Average specific heat capacity of the cold water" type: Real
58: $cse7:VARIABLE(protected = true )  type: Real unreplaceable
59: condenseur.U:VARIABLE(unit = "W/(m2.K)" )  "Heat transfert coefficient" type: Real
60: condenseur.U1:VARIABLE(unit = "W/(m2.K)" )  "Uncorrected heat transfert coefficient" type: Real
61: condenseur.Vf:VARIABLE(unit = "m/s" )  "Velocity of the cold water" type: Real
62: condenseur.rhof:VARIABLE(min = 1e-9 max = 1e5 start = 998.0 unit = "kg/m3" nominal = 998.0 )  "Density of the fluid in the cold side" type: Real
63: condenseur.DPgf:VARIABLE(start = 100.0 unit = "Pa" )  "Gravity pressure loss in the cold side" type: Real
64: condenseur.DPf:VARIABLE(start = -7.816453667652961e-26 unit = "Pa" )  "Total pressure loss in the cold side" type: Real
65: singularPressureLoss2.C2.P:VARIABLE(flow=false start = 1e5 unit = "Pa" )  "Fluid pressure in the control volume" type: Real
66: $cse6.s:VARIABLE(protected = true )  type: Real unreplaceable
67: $cse6.ddph:VARIABLE(protected = true )  type: Real unreplaceable
68: $cse6.T:VARIABLE(protected = true )  type: Real unreplaceable
69: $cse6.duph:VARIABLE(protected = true )  type: Real unreplaceable
70: $cse6.u:VARIABLE(protected = true )  type: Real unreplaceable
71: $cse6.duhp:VARIABLE(protected = true )  type: Real unreplaceable
72: $cse6.d:VARIABLE(protected = true )  type: Real unreplaceable
73: $cse6.ddhp:VARIABLE(protected = true )  type: Real unreplaceable
74: $cse6.cp:VARIABLE(protected = true )  type: Real unreplaceable
75: singularPressureLoss4.h:VARIABLE(start = 1e5 unit = "J/kg" )  "Fluid specific enthalpy" type: Real
76: condenseur.W:VARIABLE(start = 1e6 unit = "W" )  "Power exchanged from the hot side to the cold side" type: Real
77: condenseur.Tsat_att:VARIABLE(min = 0.0 start = 310.0 unit = "K" nominal = 300.0 )  "Expected HEI saturation temperature" type: Real
78: condenseur.Psat_att:VARIABLE(start = 6000.0 unit = "Pa" )  "Expected HEI saturation pressure" type: Real
79: condenseur.Wcut_off:VARIABLE(start = 1.1680480525936648e8 unit = "W" )  "Power exchanged from the hot side to the cold side at Pcut_off" type: Real
80: condenseur.Tef:VARIABLE(min = 200.0 max = 6000.0 start = 350.0 unit = "K" nominal = 300.0 )  "Fluid temperature at the inlet of the cold side" type: Real
81: condenseur.profe.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 )  "Density" type: Real
82: condenseur.profe.x:VARIABLE(min = 0.0 max = 1.0 unit = "1" )  "Vapor mass fraction" type: Real
83: condenseur.profe.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific heat capacity at constant presure" type: Real
84: condenseur.profe.ddhp:VARIABLE(unit = "kg.s2/m5" )  "Derivative of density wrt. specific enthalpy at constant pressure" type: Real
85: condenseur.profe.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 )  "Specific inner energy" type: Real
86: condenseur.profe.ddph:VARIABLE(unit = "s2/m2" )  "Derivative of density wrt. pressure at constant specific enthalpy" type: Real
87: $cse4.duph:VARIABLE(protected = true )  type: Real unreplaceable
88: $cse4.x:VARIABLE(protected = true )  type: Real unreplaceable
89: $cse4.s:VARIABLE(protected = true )  type: Real unreplaceable
90: $cse4.d:VARIABLE(protected = true )  type: Real unreplaceable
91: $cse4.cp:VARIABLE(protected = true )  type: Real unreplaceable
92: $cse4.ddph:VARIABLE(protected = true )  type: Real unreplaceable
93: $cse4.ddhp:VARIABLE(protected = true )  type: Real unreplaceable
94: $cse4.duhp:VARIABLE(protected = true )  type: Real unreplaceable
95: $cse4.u:VARIABLE(protected = true )  type: Real unreplaceable
96: $cse4.T:VARIABLE(protected = true )  type: Real unreplaceable
[/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 0.001906/3.514, allocations: 3.981 MB / 1.205 GB, free: 47.92 MB / 0.8262 GB
Error: post-optimization module createDAEmodeBDAE (simulation) failed.
Error: Internal error SimCode DAEmode: The model ThermoSysPro.Fluid.Examples.SimpleExamples.TestStaticCondenserHEI could not be translated