Running: ./testmodel.py --libraries=/home/hudson/saved_omc/libraries/.openmodelica/libraries --ompython_omhome=/usr ThermoSysPro_ThermoSysPro.Properties.WaterSteamSimple.Validation.Bench.Test1_polynomial.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.Properties.WaterSteamSimple.Validation.Bench.Test1_polynomial,tolerance=1e-06,outputFormat="empty",numberOfIntervals=5000,variableFilter="",fileNamePrefix="ThermoSysPro_ThermoSysPro.Properties.WaterSteamSimple.Validation.Bench.Test1_polynomial")
translateModel(ThermoSysPro.Properties.WaterSteamSimple.Validation.Bench.Test1_polynomial,tolerance=1e-06,outputFormat="empty",numberOfIntervals=5000,variableFilter="",fileNamePrefix="ThermoSysPro_ThermoSysPro.Properties.WaterSteamSimple.Validation.Bench.Test1_polynomial")
Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermoSysPro 4.0.0-master/package.mo): time 0.8012/0.8012, allocations: 150.9 MB / 167.2 MB, free: 14.51 MB / 142.1 MB
Notification: Performance of FrontEnd - loaded program: time 0.0003341/0.0003341, allocations: 17.03 kB / 237.8 MB, free: 1.789 MB / 190.1 MB
Notification: Performance of FrontEnd - Absyn->SCode: time 0.05501/0.05535, allocations: 31.34 MB / 269.1 MB, free: 7.051 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.Properties.WaterSteamSimple.Validation.Bench.Test1_polynomial): time 1.592/1.648, allocations: 297.8 MB / 0.5536 GB, free: 10.1 MB / 446.1 MB
Notification: Performance of NFInst.instExpressions: time 0.4663/2.114, allocations: 187.3 MB / 0.7365 GB, free: 15.82 MB / 0.6075 GB
Notification: Performance of NFInst.updateImplicitVariability: time 0.0006626/2.115, allocations: 6.531 kB / 0.7365 GB, free: 15.82 MB / 0.6075 GB
[/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).
[/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/Machines/StaticCentrifugalPump.mo:60:3-62:42:writable] Warning: Connector C1 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/Machines/StaticCentrifugalPump.mo:63:3-65:37:writable] Warning: Connector C2 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/Machines/StaticCentrifugalPump.mo:60:3-62:42:writable] Warning: Connector C1 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/Machines/StaticCentrifugalPump.mo:63:3-65:37:writable] Warning: Connector C2 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/Volumes/VolumeD.mo:29:3-31:42:writable] Warning: Connector Ce 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/Volumes/VolumeD.mo:32:3-34:37:writable] Warning: Connector Cs1 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/Volumes/VolumeD.mo:35:3-37:43:writable] Warning: Connector Cs2 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/Volumes/VolumeD.mo:38:3-40:37:writable] Warning: Connector Cs3 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/PressureLosses/IdealCheckValve.mo:22:3-23:46:writable] Warning: Connector C2 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/PressureLosses/IdealCheckValve.mo:24:3-25:48:writable] Warning: Connector C1 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/PressureLosses/IdealCheckValve.mo:22:3-23:46:writable] Warning: Connector C2 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/PressureLosses/IdealCheckValve.mo:24:3-25:48:writable] Warning: Connector C1 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/Volumes/VolumeC.mo:29:3-31:42:writable] Warning: Connector Ce1 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/Volumes/VolumeC.mo:32:3-34:37:writable] Warning: Connector Ce2 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/Volumes/VolumeC.mo:35:3-37:37:writable] Warning: Connector Cs 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/Volumes/VolumeC.mo:38:3-40:43:writable] Warning: Connector Ce3 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/PressureLosses/LumpedStraightPipe.mo:49:3-50:42:writable] Warning: Connector C1 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/PressureLosses/LumpedStraightPipe.mo:51:3-53:37:writable] Warning: Connector C2 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/PressureLosses/LumpedStraightPipe.mo:49:3-50:42:writable] Warning: Connector C1 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/PressureLosses/LumpedStraightPipe.mo:51:3-53:37:writable] Warning: Connector C2 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 0.0006981/2.115, allocations: 234.5 kB / 0.7367 GB, free: 15.82 MB / 0.6075 GB
Notification: Performance of NFTyping.typeBindings: time 0.0009683/2.116, allocations: 372.1 kB / 0.737 GB, free: 15.81 MB / 0.6075 GB
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermoSysPro 4.0.0-master/Properties/WaterSteam/IF97_packages.mo:783:9-783:27:writable] Warning: cv was used before it was defined (given a value). Additional such uses may exist for the variable, but some messages were suppressed.
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermoSysPro 4.0.0-master/Properties/WaterSteam/IF97_packages.mo:850:9-850:27:writable] Warning: cv was used before it was defined (given a value). Additional such uses may exist for the variable, but some messages were suppressed.
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermoSysPro 4.0.0-master/Properties/WaterSteam/IF97_packages.mo:1088:9-1088:27:writable] Warning: cv was used before it was defined (given a value). Additional such uses may exist for the variable, but some messages were suppressed.
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermoSysPro 4.0.0-master/Properties/WaterSteamSimple/prop4_Ph.mo:69:3-69:60:writable] Warning: dh1satp was used before it was defined (given a value). Additional such uses may exist for the variable, but some messages were suppressed.
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermoSysPro 4.0.0-master/Properties/WaterSteamSimple/prop4_Ph.mo:69:3-69:60:writable] Warning: dh2satp was used before it was defined (given a value). Additional such uses may exist for the variable, but some messages were suppressed.
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermoSysPro 4.0.0-master/Properties/WaterSteamSimple/prop4_Ph_der.mo:167:3-170:49:writable] Warning: du1satp_der was used before it was defined (given a value). Additional such uses may exist for the variable, but some messages were suppressed.
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermoSysPro 4.0.0-master/Properties/WaterSteamSimple/prop4_Ph_der.mo:167:3-170:49:writable] Warning: du2satp_der was used before it was defined (given a value). Additional such uses may exist for the variable, but some messages were suppressed.
Notification: Performance of NFTyping.typeClassSections: time 0.02492/2.141, allocations: 11.55 MB / 0.7483 GB, free: 15.59 MB / 0.6075 GB
Notification: Performance of NFFlatten.flatten: time 0.00151/2.143, allocations: 1.456 MB / 0.7497 GB, free: 15.58 MB / 0.6075 GB
Notification: Performance of NFFlatten.resolveConnections: time 0.000533/2.143, allocations: 0.5436 MB / 0.7503 GB, free: 15.5 MB / 0.6075 GB
Notification: Performance of NFEvalConstants.evaluate: time 0.0005635/2.144, allocations: 0.5612 MB / 0.7508 GB, free: 15.5 MB / 0.6075 GB
Notification: Performance of NFSimplifyModel.simplify: time 0.0004514/2.144, allocations: 0.5295 MB / 0.7513 GB, free: 15.5 MB / 0.6075 GB
Notification: Performance of NFPackage.collectConstants: time 0.0001081/2.144, allocations: 95.16 kB / 0.7514 GB, free: 15.5 MB / 0.6075 GB
Notification: Performance of NFFlatten.collectFunctions: time 0.03084/2.175, allocations: 20.14 MB / 0.7711 GB, free: 12.53 MB / 0.6075 GB
Notification: Performance of NFScalarize.scalarize: time 0.0003201/2.176, allocations: 227 kB / 0.7713 GB, free: 12.49 MB / 0.6075 GB
Notification: Performance of NFVerifyModel.verify: time 0.0008195/2.176, allocations: 0.5839 MB / 0.7719 GB, free: 12.45 MB / 0.6075 GB
Notification: Performance of NFConvertDAE.convert: time 0.0213/2.198, allocations: 10.59 MB / 0.7822 GB, free: 8.539 MB / 0.6075 GB
Notification: Performance of FrontEnd - DAE generated: time 3.967e-06/2.198, allocations: 0 / 0.7822 GB, free: 8.539 MB / 0.6075 GB
Notification: Performance of FrontEnd: time 1.372e-06/2.198, allocations: 0 / 0.7822 GB, free: 8.539 MB / 0.6075 GB
Notification: Performance of Transformations before backend: time 1.299e-05/2.198, allocations: 0 / 0.7822 GB, free: 8.539 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: 301
 * Number of variables: 301
Notification: Performance of Generate backend data structure: time 0.005872/2.204, allocations: 2.528 MB / 0.7847 GB, free: 7.016 MB / 0.6075 GB
Notification: Performance of prepare preOptimizeDAE: time 3.664e-05/2.204, allocations: 14.61 kB / 0.7847 GB, free: 7.012 MB / 0.6075 GB
Notification: Performance of preOpt normalInlineFunction (simulation): time 0.0001935/2.204, allocations: 130.1 kB / 0.7848 GB, free: 6.945 MB / 0.6075 GB
Notification: Performance of preOpt evaluateParameters (simulation): time 0.0005666/2.205, allocations: 0.4921 MB / 0.7853 GB, free: 6.602 MB / 0.6075 GB
Notification: Performance of preOpt simplifyIfEquations (simulation): time 9.418e-05/2.205, allocations: 128.4 kB / 0.7854 GB, free: 6.531 MB / 0.6075 GB
Notification: Performance of preOpt expandDerOperator (simulation): time 0.0001086/2.205, allocations: 89 kB / 0.7855 GB, free: 6.527 MB / 0.6075 GB
Notification: Performance of preOpt clockPartitioning (simulation): time 0.001487/2.206, allocations: 1.199 MB / 0.7867 GB, free: 6.023 MB / 0.6075 GB
Notification: Performance of preOpt findStateOrder (simulation): time 2.22e-05/2.206, allocations: 4.281 kB / 0.7867 GB, free: 6.023 MB / 0.6075 GB
Notification: Performance of preOpt replaceEdgeChange (simulation): time 6.968e-05/2.206, allocations: 43.19 kB / 0.7867 GB, free: 6.023 MB / 0.6075 GB
Notification: Performance of preOpt inlineArrayEqn (simulation): time 3.043e-05/2.206, allocations: 43.62 kB / 0.7868 GB, free: 6.016 MB / 0.6075 GB
Notification: Performance of preOpt removeEqualRHS (simulation): time 0.001275/2.208, allocations: 0.8087 MB / 0.7876 GB, free: 5.906 MB / 0.6075 GB
Warning: The model contains alias variables with redundant start and/or conflicting nominal values. It is recommended to resolve the conflicts, because otherwise the system could be hard to solve. To print the conflicting alias sets and the chosen candidates please use -d=aliasConflicts.
Notification: Performance of preOpt removeSimpleEquations (simulation): time 0.02319/2.231, allocations: 15.44 MB / 0.8027 GB, free: 9.543 MB / 0.6231 GB
Notification: Performance of preOpt comSubExp (simulation): time 0.001521/2.232, allocations: 0.7536 MB / 0.8034 GB, free: 9.191 MB / 0.6231 GB
Notification: Performance of preOpt resolveLoops (simulation): time 0.0008286/2.233, allocations: 489.9 kB / 0.8039 GB, free: 8.906 MB / 0.6231 GB
Notification: Performance of preOpt evalFunc (simulation): time 0.3029/2.536, allocations: 151.4 MB / 0.9517 GB, free: 1.242 MB / 0.7794 GB
Notification: Performance of preOpt encapsulateWhenConditions (simulation): time 0.001114/2.537, allocations: 0.523 MB / 0.9522 GB, free: 0.707 MB / 0.7794 GB
Notification: Performance of pre-optimization done (n=141): time 4.208e-06/2.537, allocations: 0 / 0.9522 GB, free: 0.707 MB / 0.7794 GB
Notification: Performance of matching and sorting (n=141): time 0.02141/2.559, allocations: 4.316 MB / 0.9564 GB, free: 12.38 MB / 0.795 GB
Notification: Performance of inlineWhenForInitialization (initialization): time 9.379e-05/2.559, allocations: 142.2 kB / 0.9565 GB, free: 12.21 MB / 0.795 GB
Notification: Performance of selectInitializationVariablesDAE (initialization): time 0.0009017/2.56, allocations: 0.582 MB / 0.9571 GB, free: 11.62 MB / 0.795 GB
Notification: Performance of collectPreVariables (initialization): time 7.82e-05/2.56, allocations: 37.7 kB / 0.9571 GB, free: 11.58 MB / 0.795 GB
Notification: Performance of collectInitialEqns (initialization): time 0.0003996/2.56, allocations: 421.6 kB / 0.9575 GB, free: 11.16 MB / 0.795 GB
Notification: Performance of collectInitialBindings (initialization): time 0.0004624/2.561, allocations: 456.7 kB / 0.958 GB, free: 10.73 MB / 0.795 GB
Notification: Performance of simplifyInitialFunctions (initialization): time 0.0003745/2.561, allocations: 220.8 kB / 0.9582 GB, free: 10.5 MB / 0.795 GB
Notification: Performance of setup shared object (initialization): time 0.0001525/2.561, allocations: 345.9 kB / 0.9585 GB, free: 10.16 MB / 0.795 GB
Notification: Performance of preBalanceInitialSystem (initialization): time 0.0007461/2.562, allocations: 338.8 kB / 0.9588 GB, free: 9.828 MB / 0.795 GB
Notification: Performance of partitionIndependentBlocks (initialization): time 0.0009574/2.563, allocations: 0.6261 MB / 0.9595 GB, free: 9.09 MB / 0.795 GB
Notification: Performance of analyzeInitialSystem (initialization): time 0.001699/2.565, allocations: 1.035 MB / 0.9605 GB, free: 7.977 MB / 0.795 GB
Notification: Performance of solveInitialSystemEqSystem (initialization): time 6.723e-06/2.565, allocations: 1.203 kB / 0.9605 GB, free: 7.977 MB / 0.795 GB
Notification: Performance of matching and sorting (n=186) (initialization): time 0.002709/2.567, allocations: 1.447 MB / 0.9619 GB, free: 6.566 MB / 0.795 GB
Notification: Performance of prepare postOptimizeDAE: time 2.555e-05/2.568, allocations: 8 kB / 0.9619 GB, free: 6.559 MB / 0.795 GB
Notification: Performance of postOpt simplifyComplexFunction (initialization): time 1.961e-05/2.568, allocations: 8 kB / 0.9619 GB, free: 6.551 MB / 0.795 GB
Notification: Performance of postOpt tearingSystem (initialization): time 0.003783/2.571, allocations: 1.442 MB / 0.9633 GB, free: 5.113 MB / 0.795 GB
Notification: Performance of postOpt solveSimpleEquations (initialization): time 0.0002669/2.572, allocations: 72.8 kB / 0.9634 GB, free: 5.051 MB / 0.795 GB
Notification: Performance of postOpt calculateStrongComponentJacobians (initialization): time 0.002705/2.574, allocations: 1.648 MB / 0.965 GB, free: 3.383 MB / 0.795 GB
Notification: Performance of postOpt simplifyAllExpressions (initialization): time 0.0008284/2.575, allocations: 126.6 kB / 0.9651 GB, free: 3.258 MB / 0.795 GB
Notification: Performance of postOpt collapseArrayExpressions (initialization): time 8.526e-05/2.575, allocations: 51.98 kB / 0.9651 GB, free: 3.207 MB / 0.795 GB
Notification: Model statistics after passing the back-end for initialization:
 * Number of independent subsystems: 37
 * Number of states: 0 ()
 * Number of discrete variables: 40 ($PRE.idealCheckValve2.touvert,$whenCondition4,$PRE.idealCheckValve2.tferme,$whenCondition3,$PRE.idealCheckValve1.touvert,$whenCondition2,$PRE.idealCheckValve1.tferme,$whenCondition1,idealCheckValve2.tferme,idealCheckValve2.touvert,idealCheckValve2.ouvert,$PRE.idealCheckValve2.ouvert,idealCheckValve1.tferme,idealCheckValve1.touvert,idealCheckValve1.ouvert,$PRE.idealCheckValve1.ouvert,perteDP1.C2.b,perteDP1.C1.a,perteDP.C2.b,perteDP.C1.a,volumeC.Ce3.a,volumeC.Cs.b,volumeC.Ce2.a,volumeC.Ce1.a,idealCheckValve2.C1.a,idealCheckValve2.C2.b,idealCheckValve1.C1.a,idealCheckValve1.C2.b,volumeD.Cs3.b,volumeD.Cs2.b,volumeD.Cs1.b,volumeD.Ce.a,staticCentrifugalPump2.C2.b,staticCentrifugalPump2.C1.a,staticCentrifugalPump1.C2.b,staticCentrifugalPump1.C1.a,sourceP.C.b,puitsP.C.a,volumeC.Ce1.b,volumeD.Cs3.a)
 * Number of discrete states: 0 ()
 * Number of clocked states: 0 ()
 * Top-level inputs: 0
Notification: Strong component statistics for initialization (67):
 * Single equations (assignments): 64
 * Array equations: 0
 * Algorithm blocks: 0
 * Record equations: 2
 * 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
   {(14,34)}
Notification: Performance of prepare postOptimizeDAE: time 0.0004097/2.576, allocations: 263.8 kB / 0.9654 GB, free: 2.949 MB / 0.795 GB
Notification: Performance of postOpt lateInlineFunction (simulation): time 0.00018/2.576, allocations: 91.98 kB / 0.9655 GB, free: 2.859 MB / 0.795 GB
Notification: Performance of postOpt wrapFunctionCalls (simulation): time 0.004051/2.58, allocations: 2.139 MB / 0.9676 GB, free: 0.6836 MB / 0.795 GB
Notification: Performance of postOpt simplifysemiLinear (simulation): time 1.017e-05/2.58, allocations: 3.984 kB / 0.9676 GB, free: 0.6797 MB / 0.795 GB
Notification: Performance of postOpt simplifyComplexFunction (simulation): time 3.576e-06/2.58, allocations: 0 / 0.9676 GB, free: 0.6797 MB / 0.795 GB
Notification: Performance of postOpt removeConstants (simulation): time 0.0003953/2.58, allocations: 271.1 kB / 0.9678 GB, free: 404 kB / 0.795 GB
Notification: Performance of postOpt simplifyTimeIndepFuncCalls (simulation): time 0.0001174/2.58, allocations: 20 kB / 0.9679 GB, free: 384 kB / 0.795 GB
Notification: Performance of postOpt simplifyAllExpressions (simulation): time 0.0004574/2.581, allocations: 31.97 kB / 0.9679 GB, free: 352 kB / 0.795 GB
Notification: Performance of postOpt findZeroCrossings (simulation): time 0.0001334/2.581, allocations: 52.58 kB / 0.9679 GB, free: 300 kB / 0.795 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(perteDP1.T, perteDP1.rho, perteDP1.pro.u, perteDP1.pro.s, perteDP1.pro.cp, perteDP1.pro.ddhp, perteDP1.pro.ddph, perteDP1.pro.duph, perteDP1.pro.duhp, perteDP1.pro.x) = $cse1

Variables:
1: perteDP1.pro.ddhp:VARIABLE(unit = "kg.s2/m5" )  "Derivative of density wrt. specific enthalpy at constant pressure" type: Real
2: perteDP1.pro.ddph:VARIABLE(unit = "s2/m2" )  "Derivative of density wrt. pressure at constant specific enthalpy" type: Real
3: perteDP1.pro.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific entropy" type: Real
4: perteDP1.pro.x:VARIABLE(min = 0.0 max = 1.0 unit = "1" )  "Vapor mass fraction" type: Real
5: perteDP1.pro.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific heat capacity at constant presure" type: Real
6: $cse1.ddhp:VARIABLE(protected = true )  type: Real unreplaceable
7: $cse1.duhp:VARIABLE(protected = true )  type: Real unreplaceable
8: $cse1.u:VARIABLE(protected = true )  type: Real unreplaceable
9: $cse1.s:VARIABLE(protected = true )  type: Real unreplaceable
10: $cse1.cp: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): 0.0 = if idealCheckValve1.ouvert then idealCheckValve1.deltaP else idealCheckValve1.Q - idealCheckValve1.Qmin
2/2 (1): idealCheckValve1.Q = staticCentrifugalPump1.Qv * staticCentrifugalPump1.rho
3/3 (1): staticCentrifugalPump1.rh = max(if noEvent(abs(staticCentrifugalPump1.R) > staticCentrifugalPump1.eps) then staticCentrifugalPump1.b1 * staticCentrifugalPump1.Qv * abs(staticCentrifugalPump1.Qv) / staticCentrifugalPump1.R ^ 2.0 + staticCentrifugalPump1.b2 * staticCentrifugalPump1.Qv / staticCentrifugalPump1.R + staticCentrifugalPump1.b3 else staticCentrifugalPump1.b3, staticCentrifugalPump1.rhmin)
4/4 (1): staticCentrifugalPump1.deltaH = 9.80665 * staticCentrifugalPump1.hn / staticCentrifugalPump1.rh
5/5 (1): staticCentrifugalPump1.deltaH = idealCheckValve1.C1.h - volumeD.Cs1.h
6/6 (1): 0.0 = if idealCheckValve1.Q > 0.0 then volumeD.Cs1.h - volumeD.h else idealCheckValve1.C1.h - staticCentrifugalPump1.C2.h_vol
7/7 (1): staticCentrifugalPump1.h = 0.5 * (volumeD.Cs1.h + idealCheckValve1.C1.h)
8/8 (10): $cse8 = ThermoSysPro.Properties.Fluid.Ph(staticCentrifugalPump1.Pm, staticCentrifugalPump1.h, staticCentrifugalPump1.mode, staticCentrifugalPump1.fluid)
9/18 (10): ThermoSysPro.Properties.WaterSteam.Common.ThermoProperties_ph(staticCentrifugalPump1.pro.T, staticCentrifugalPump1.rho, staticCentrifugalPump1.pro.u, staticCentrifugalPump1.pro.s, staticCentrifugalPump1.pro.cp, staticCentrifugalPump1.pro.ddhp, staticCentrifugalPump1.pro.ddph, staticCentrifugalPump1.pro.duph, staticCentrifugalPump1.pro.duhp, staticCentrifugalPump1.pro.x) = $cse8
10/28 (1): staticCentrifugalPump1.Pm = 0.5 * (volumeD.P + staticCentrifugalPump1.C2.P)
11/29 (1): staticCentrifugalPump1.deltaP = staticCentrifugalPump1.C2.P - volumeD.P
12/30 (1): staticCentrifugalPump1.deltaP = 9.80665 * staticCentrifugalPump1.rho * staticCentrifugalPump1.hn
13/31 (1): 0.0 = idealCheckValve1.deltaP + staticCentrifugalPump2.deltaP + (-idealCheckValve2.deltaP) - staticCentrifugalPump1.deltaP
14/32 (1): staticCentrifugalPump2.deltaP = staticCentrifugalPump2.C2.P - volumeD.P
15/33 (1): staticCentrifugalPump2.Pm = 0.5 * (volumeD.P + staticCentrifugalPump2.C2.P)
16/34 (10): $cse7 = ThermoSysPro.Properties.Fluid.Ph(staticCentrifugalPump2.Pm, staticCentrifugalPump2.h, staticCentrifugalPump2.mode, staticCentrifugalPump2.fluid)
17/44 (10): ThermoSysPro.Properties.WaterSteam.Common.ThermoProperties_ph(staticCentrifugalPump2.pro.T, staticCentrifugalPump2.rho, staticCentrifugalPump2.pro.u, staticCentrifugalPump2.pro.s, staticCentrifugalPump2.pro.cp, staticCentrifugalPump2.pro.ddhp, staticCentrifugalPump2.pro.ddph, staticCentrifugalPump2.pro.duph, staticCentrifugalPump2.pro.duhp, staticCentrifugalPump2.pro.x) = $cse7
18/54 (1): staticCentrifugalPump2.h = 0.5 * (volumeD.Cs2.h + idealCheckValve2.C1.h)
19/55 (1): staticCentrifugalPump2.deltaH = idealCheckValve2.C1.h - volumeD.Cs2.h
20/56 (1): staticCentrifugalPump2.deltaH = 9.80665 * staticCentrifugalPump2.hn / staticCentrifugalPump2.rh
21/57 (1): staticCentrifugalPump2.rh = max(if noEvent(abs(staticCentrifugalPump2.R) > staticCentrifugalPump2.eps) then staticCentrifugalPump2.b1 * staticCentrifugalPump2.Qv * abs(staticCentrifugalPump2.Qv) / staticCentrifugalPump2.R ^ 2.0 + staticCentrifugalPump2.b2 * staticCentrifugalPump2.Qv / staticCentrifugalPump2.R + staticCentrifugalPump2.b3 else staticCentrifugalPump2.b3, staticCentrifugalPump2.rhmin)
22/58 (1): idealCheckValve2.Q = staticCentrifugalPump2.Qv * staticCentrifugalPump2.rho
23/59 (1): 0.0 = if idealCheckValve2.Q > 0.0 then volumeD.Cs2.h - volumeD.h else idealCheckValve2.C1.h - staticCentrifugalPump2.C2.h_vol
24/60 (1): 0.0 = if idealCheckValve2.Q > 0.0 then idealCheckValve2.C1.h - staticCentrifugalPump2.C2.h_vol else idealCheckValve2.C1.h - volumeC.h
25/61 (1): 0.0 = perteDP.Q + (-idealCheckValve2.Q) - idealCheckValve1.Q
26/62 (1): $cse4 = ThermoSysPro.Functions.ThermoSquare(perteDP.Q, perteDP.eps)
27/63 (1): perteDP.deltaPf = 0.5 * perteDP.khi * $cse4 / (perteDP.A ^ 2.0 * perteDP.rho)
28/64 (1): perteDP.deltaP = perteDP.deltaPf + 9.80665 * perteDP.rho * (perteDP.z2 - perteDP.z1)
29/65 (10): $cse3 = ThermoSysPro.Properties.Fluid.Ph(perteDP.Pm, perteDP.h, perteDP.mode, perteDP.fluid)
30/75 (10): ThermoSysPro.Properties.WaterSteam.Common.ThermoProperties_ph(perteDP.T, perteDP.rho, perteDP.pro.u, perteDP.pro.s, perteDP.pro.cp, perteDP.pro.ddhp, perteDP.pro.ddph, perteDP.pro.duph, perteDP.pro.duhp, perteDP.pro.x) = $cse3
31/85 (1): perteDP.Pm = 0.5 * (sourceP.P0 + volumeD.P)
32/86 (1): sourceP.P0 - volumeD.P = perteDP.deltaP
33/87 (1): 0.0 = perteDP.Q - perteDP1.Q
34/88 (1): $cse2 = ThermoSysPro.Functions.ThermoSquare(perteDP1.Q, perteDP1.eps)
35/89 (1): perteDP1.deltaPf = 0.5 * perteDP1.khi * $cse2 / (perteDP1.A ^ 2.0 * perteDP1.rho)
36/90 (1): perteDP1.deltaP = perteDP1.deltaPf + 9.80665 * perteDP1.rho * (perteDP1.z2 - perteDP1.z1)
37/91 (10): $cse1 = ThermoSysPro.Properties.Fluid.Ph(perteDP1.Pm, perteDP1.h, perteDP1.mode, perteDP1.fluid)
38/101 (10): ThermoSysPro.Properties.WaterSteam.Common.ThermoProperties_ph(perteDP1.T, perteDP1.rho, perteDP1.pro.u, perteDP1.pro.s, perteDP1.pro.cp, perteDP1.pro.ddhp, perteDP1.pro.ddph, perteDP1.pro.duph, perteDP1.pro.duhp, perteDP1.pro.x) = $cse1
39/111 (1): perteDP1.Pm = 0.5 * (volumeC.P + puitsP.P0)
40/112 (1): idealCheckValve1.deltaP = staticCentrifugalPump1.C2.P - volumeC.P
41/113 (1): volumeC.P - puitsP.P0 = perteDP1.deltaP
42/114 (1): 0.0 = if perteDP1.Q > 0.0 then perteDP1.h - volumeC.h else perteDP1.h - puitsP.h
43/115 (1): 0.0 = if perteDP.Q > 0.0 then perteDP.h - sourceP.h else perteDP.h - volumeD.h
44/116 (1): 0.0 = if idealCheckValve2.ouvert then idealCheckValve2.deltaP else idealCheckValve2.Q - idealCheckValve2.Qmin
45/117 (1): staticCentrifugalPump2.hn = (staticCentrifugalPump2.a1 * abs(staticCentrifugalPump2.Qv) + staticCentrifugalPump2.a2 * staticCentrifugalPump2.R) * staticCentrifugalPump2.Qv + staticCentrifugalPump2.a3 * staticCentrifugalPump2.R ^ 2.0
46/118 (1): staticCentrifugalPump2.deltaP = 9.80665 * staticCentrifugalPump2.rho * staticCentrifugalPump2.hn
47/119 (1): 0.0 = if idealCheckValve1.Q > 0.0 then idealCheckValve1.C1.h - staticCentrifugalPump1.C2.h_vol else idealCheckValve1.C1.h - volumeC.h
48/120 (1): staticCentrifugalPump1.hn = (staticCentrifugalPump1.a1 * abs(staticCentrifugalPump1.Qv) + staticCentrifugalPump1.a2 * staticCentrifugalPump1.R) * staticCentrifugalPump1.Qv + staticCentrifugalPump1.a3 * staticCentrifugalPump1.R ^ 2.0

Variables:
1: staticCentrifugalPump1.hn:VARIABLE(min = 0.0 start = 10.0 unit = "m" )  "Pump head" type: Real
2: staticCentrifugalPump1.C2.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" )  "Fluid specific enthalpy in the control volume" type: Real
3: staticCentrifugalPump2.rho:VARIABLE(min = 1e-9 max = 1e5 start = 998.0 unit = "kg/m3" nominal = 998.0 )  "Fluid density" type: Real
4: staticCentrifugalPump2.hn:VARIABLE(min = 0.0 start = 10.0 unit = "m" )  "Pump head" type: Real
5: idealCheckValve2.deltaP:VARIABLE(unit = "Pa" )  "Pressure difference between the inlet and the outlet" type: Real
6: perteDP.h:VARIABLE(start = 1e5 unit = "J/kg" )  "Fluid specific enthalpy" type: Real
7: perteDP1.h:VARIABLE(start = 1e5 unit = "J/kg" )  "Fluid specific enthalpy" type: Real
8: perteDP1.deltaP:VARIABLE(unit = "Pa" )  "Total pressure loss" type: Real
9: idealCheckValve1.deltaP:VARIABLE(unit = "Pa" )  "Pressure difference between the inlet and the outlet" type: Real
10: volumeC.P:VARIABLE(min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 )  "Fluid pressure" type: Real
11: perteDP1.pro.ddhp:VARIABLE(unit = "kg.s2/m5" )  "Derivative of density wrt. specific enthalpy at constant pressure" type: Real
12: perteDP1.pro.ddph:VARIABLE(unit = "s2/m2" )  "Derivative of density wrt. pressure at constant specific enthalpy" type: Real
13: perteDP1.pro.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific entropy" type: Real
14: perteDP1.pro.x:VARIABLE(min = 0.0 max = 1.0 unit = "1" )  "Vapor mass fraction" type: Real
15: perteDP1.pro.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific heat capacity at constant presure" type: Real
16: $cse1.ddhp:VARIABLE(protected = true )  type: Real unreplaceable
17: $cse1.duhp:VARIABLE(protected = true )  type: Real unreplaceable
18: $cse1.u:VARIABLE(protected = true )  type: Real unreplaceable
19: $cse1.s:VARIABLE(protected = true )  type: Real unreplaceable
20: $cse1.cp:VARIABLE(protected = true )  type: Real unreplaceable
21: $cse1.T:VARIABLE(protected = true )  type: Real unreplaceable
22: $cse1.x:VARIABLE(protected = true )  type: Real unreplaceable
23: $cse1.d:VARIABLE(protected = true )  type: Real unreplaceable
24: $cse1.duph:VARIABLE(protected = true )  type: Real unreplaceable
25: perteDP1.Pm:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 )  "Fluid average pressure" type: Real
26: $cse1.ddph:VARIABLE(protected = true )  type: Real unreplaceable
27: perteDP1.pro.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 )  "Specific inner energy" type: Real
28: perteDP1.pro.duhp:VARIABLE(unit = "1" )  "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real
29: perteDP1.pro.duph:VARIABLE(unit = "m3/kg" )  "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real
30: perteDP1.T:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 300.0 )  "Fluid temperature" type: Real
31: perteDP1.deltaPf:VARIABLE(unit = "Pa" )  "Friction pressure loss" type: Real
32: perteDP1.rho:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 )  "Fluid density" type: Real
33: $cse2:VARIABLE(protected = true )  type: Real unreplaceable
34: perteDP1.Q:VARIABLE(start = 100.0 unit = "kg/s" )  "Mass flow rate" type: Real
35: perteDP.deltaP:VARIABLE(unit = "Pa" )  "Total pressure loss" type: Real
36: volumeD.P:VARIABLE(min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 )  "Fluid pressure" type: Real
37: perteDP.pro.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 )  "Specific inner energy" type: Real
38: perteDP.pro.duph:VARIABLE(unit = "m3/kg" )  "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real
39: perteDP.pro.x:VARIABLE(min = 0.0 max = 1.0 unit = "1" )  "Vapor mass fraction" type: Real
40: perteDP.pro.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific entropy" type: Real
41: perteDP.pro.ddhp:VARIABLE(unit = "kg.s2/m5" )  "Derivative of density wrt. specific enthalpy at constant pressure" type: Real
42: perteDP.T:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 300.0 )  "Fluid temperature" type: Real
43: perteDP.pro.ddph:VARIABLE(unit = "s2/m2" )  "Derivative of density wrt. pressure at constant specific enthalpy" type: Real
44: perteDP.pro.duhp:VARIABLE(unit = "1" )  "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real
45: perteDP.pro.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific heat capacity at constant presure" type: Real
46: $cse3.cp:VARIABLE(protected = true )  type: Real unreplaceable
47: $cse3.s:VARIABLE(protected = true )  type: Real unreplaceable
48: $cse3.duhp:VARIABLE(protected = true )  type: Real unreplaceable
49: $cse3.duph:VARIABLE(protected = true )  type: Real unreplaceable
50: $cse3.u:VARIABLE(protected = true )  type: Real unreplaceable
51: perteDP.Pm:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 )  "Fluid average pressure" type: Real
52: $cse3.x:VARIABLE(protected = true )  type: Real unreplaceable
53: $cse3.d:VARIABLE(protected = true )  type: Real unreplaceable
54: $cse3.ddph:VARIABLE(protected = true )  type: Real unreplaceable
55: $cse3.T:VARIABLE(protected = true )  type: Real unreplaceable
56: $cse3.ddhp:VARIABLE(protected = true )  type: Real unreplaceable
57: perteDP.rho:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 )  "Fluid density" type: Real
58: perteDP.deltaPf:VARIABLE(unit = "Pa" )  "Friction pressure loss" type: Real
59: $cse4:VARIABLE(protected = true )  type: Real unreplaceable
60: perteDP.Q:VARIABLE(start = 100.0 unit = "kg/s" )  "Mass flow rate" type: Real
61: staticCentrifugalPump2.C2.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" )  "Fluid specific enthalpy in the control volume" type: Real
62: idealCheckValve2.C1.h:VARIABLE(flow=false start = 1e5 unit = "J/kg" )  "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real
63: idealCheckValve2.Q:VARIABLE(start = 500.0 unit = "kg/s" )  "Mass flow rate" type: Real
64: staticCentrifugalPump2.Qv:VARIABLE(start = 0.5 unit = "m3/s" )  "Volume flow rate" type: Real
65: staticCentrifugalPump2.rh:VARIABLE()  "Hydraulic efficiency" type: Real
66: staticCentrifugalPump2.deltaH:VARIABLE(unit = "J/kg" )  "Specific enthalpy variation between the outlet and the inlet" type: Real
67: volumeD.Cs2.h:VARIABLE(flow=false start = 1e5 unit = "J/kg" )  "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real
68: staticCentrifugalPump2.pro.x:VARIABLE(min = 0.0 max = 1.0 unit = "1" )  "Vapor mass fraction" type: Real
69: staticCentrifugalPump2.pro.ddph:VARIABLE(unit = "s2/m2" )  "Derivative of density wrt. pressure at constant specific enthalpy" type: Real
70: staticCentrifugalPump2.pro.duph:VARIABLE(unit = "m3/kg" )  "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real
71: $cse7.duhp:VARIABLE(protected = true )  type: Real unreplaceable
72: staticCentrifugalPump2.pro.T:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 320.0 )  "Temperature" type: Real
73: staticCentrifugalPump2.pro.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 )  "Specific inner energy" type: Real
74: staticCentrifugalPump2.pro.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific entropy" type: Real
75: staticCentrifugalPump2.pro.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific heat capacity at constant presure" type: Real
76: staticCentrifugalPump2.pro.ddhp:VARIABLE(unit = "kg.s2/m5" )  "Derivative of density wrt. specific enthalpy at constant pressure" type: Real
77: staticCentrifugalPump2.pro.duhp:VARIABLE(unit = "1" )  "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real
78: $cse7.cp:VARIABLE(protected = true )  type: Real unreplaceable
79: $cse7.u:VARIABLE(protected = true )  type: Real unreplaceable
80: $cse7.ddhp:VARIABLE(protected = true )  type: Real unreplaceable
81: $cse7.x:VARIABLE(protected = true )  type: Real unreplaceable
82: $cse7.T:VARIABLE(protected = true )  type: Real unreplaceable
83: staticCentrifugalPump2.h:VARIABLE(start = 1e5 unit = "J/kg" )  "Fluid average specific enthalpy" type: Real
84: $cse7.s:VARIABLE(protected = true )  type: Real unreplaceable
85: $cse7.d:VARIABLE(protected = true )  type: Real unreplaceable
86: $cse7.duph:VARIABLE(protected = true )  type: Real unreplaceable
87: $cse7.ddph:VARIABLE(protected = true )  type: Real unreplaceable
88: staticCentrifugalPump2.Pm:VARIABLE(min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 )  "Fluid average pressure" type: Real
89: staticCentrifugalPump2.C2.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 )  "Fluid pressure in the control volume" type: Real
90: staticCentrifugalPump2.deltaP:VARIABLE(unit = "Pa" )  "Pressure variation between the outlet and the inlet" type: Real
91: staticCentrifugalPump1.rho:VARIABLE(min = 1e-9 max = 1e5 start = 998.0 unit = "kg/m3" nominal = 998.0 )  "Fluid density" type: Real
92: staticCentrifugalPump1.deltaP:VARIABLE(unit = "Pa" )  "Pressure variation between the outlet and the inlet" type: Real
93: staticCentrifugalPump1.C2.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 )  "Fluid pressure in the control volume" type: Real
94: staticCentrifugalPump1.pro.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 )  "Specific inner energy" type: Real
95: staticCentrifugalPump1.pro.duhp:VARIABLE(unit = "1" )  "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real
96: staticCentrifugalPump1.pro.T:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 320.0 )  "Temperature" type: Real
97: $cse8.d:VARIABLE(protected = true )  type: Real unreplaceable
98: staticCentrifugalPump1.pro.x:VARIABLE(min = 0.0 max = 1.0 unit = "1" )  "Vapor mass fraction" type: Real
99: staticCentrifugalPump1.pro.ddph:VARIABLE(unit = "s2/m2" )  "Derivative of density wrt. pressure at constant specific enthalpy" type: Real
100: staticCentrifugalPump1.pro.ddhp:VARIABLE(unit = "kg.s2/m5" )  "Derivative of density wrt. specific enthalpy at constant pressure" type: Real
101: staticCentrifugalPump1.pro.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific entropy" type: Real
102: staticCentrifugalPump1.pro.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific heat capacity at constant presure" type: Real
103: staticCentrifugalPump1.pro.duph:VARIABLE(unit = "m3/kg" )  "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real
104: $cse8.s:VARIABLE(protected = true )  type: Real unreplaceable
105: $cse8.ddhp:VARIABLE(protected = true )  type: Real unreplaceable
106: $cse8.ddph:VARIABLE(protected = true )  type: Real unreplaceable
107: $cse8.duph:VARIABLE(protected = true )  type: Real unreplaceable
108: staticCentrifugalPump1.Pm:VARIABLE(min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 )  "Fluid average pressure" type: Real
109: $cse8.x:VARIABLE(protected = true )  type: Real unreplaceable
110: $cse8.T:VARIABLE(protected = true )  type: Real unreplaceable
111: $cse8.u:VARIABLE(protected = true )  type: Real unreplaceable
112: $cse8.cp:VARIABLE(protected = true )  type: Real unreplaceable
113: $cse8.duhp:VARIABLE(protected = true )  type: Real unreplaceable
114: staticCentrifugalPump1.h:VARIABLE(start = 1e5 unit = "J/kg" )  "Fluid average specific enthalpy" type: Real
115: volumeD.Cs1.h:VARIABLE(flow=false start = 1e5 unit = "J/kg" )  "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real
116: idealCheckValve1.C1.h:VARIABLE(flow=false start = 1e5 unit = "J/kg" )  "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real
117: staticCentrifugalPump1.deltaH:VARIABLE(unit = "J/kg" )  "Specific enthalpy variation between the outlet and the inlet" type: Real
118: staticCentrifugalPump1.rh:VARIABLE()  "Hydraulic efficiency" type: Real
119: staticCentrifugalPump1.Qv:VARIABLE(start = 0.5 unit = "m3/s" )  "Volume flow rate" type: Real
120: idealCheckValve1.Q:VARIABLE(start = 500.0 unit = "kg/s" )  "Mass flow rate" 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 0.004076/2.585, allocations: 5.28 MB / 0.9731 GB, free: 9.797 MB / 0.8106 GB
Error: post-optimization module createDAEmodeBDAE (simulation) failed.
Error: Internal error SimCode DAEmode: The model ThermoSysPro.Properties.WaterSteamSimple.Validation.Bench.Test1_polynomial could not be translated