Running: ./testmodel.py --libraries=/home/hudson/saved_omc/libraries/.openmodelica/libraries --ompython_omhome=/usr ThermoSysPro_ThermoSysPro.Fluid.Examples.SimpleExamples.TestSimpleDynamicCondenser1.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.TestSimpleDynamicCondenser1,tolerance=1e-06,outputFormat="empty",numberOfIntervals=5000,variableFilter="",fileNamePrefix="ThermoSysPro_ThermoSysPro.Fluid.Examples.SimpleExamples.TestSimpleDynamicCondenser1") translateModel(ThermoSysPro.Fluid.Examples.SimpleExamples.TestSimpleDynamicCondenser1,tolerance=1e-06,outputFormat="empty",numberOfIntervals=5000,variableFilter="",fileNamePrefix="ThermoSysPro_ThermoSysPro.Fluid.Examples.SimpleExamples.TestSimpleDynamicCondenser1") Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermoSysPro 4.0.0-master/package.mo): time 0.8572/0.8572, allocations: 150.9 MB / 167.2 MB, free: 14.47 MB / 142.1 MB Notification: Performance of FrontEnd - loaded program: time 0.0005677/0.0005679, allocations: 16.56 kB / 237.8 MB, free: 1.797 MB / 190.1 MB Notification: Performance of FrontEnd - Absyn->SCode: time 0.06963/0.07021, allocations: 31.34 MB / 269.1 MB, free: 7.039 MB / 222.1 MB Notification: Automatically loaded package Complex 4.0.0 due to uses annotation from Modelica. Notification: Automatically loaded package ModelicaServices 4.0.0 due to uses annotation from Modelica. Notification: Automatically loaded package Modelica 4.0.0 due to usage. Notification: Performance of NFInst.instantiate(ThermoSysPro.Fluid.Examples.SimpleExamples.TestSimpleDynamicCondenser1): time 1.689/1.759, allocations: 299.3 MB / 0.5551 GB, free: 8.844 MB / 446.1 MB Notification: Performance of NFInst.instExpressions: time 0.5166/2.276, allocations: 207.8 MB / 0.758 GB, free: 168 kB / 0.5919 GB Notification: Performance of NFInst.updateImplicitVariability: time 0.000737/2.277, allocations: 19.28 kB / 0.758 GB, free: 168 kB / 0.5919 GB [/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermoSysPro 4.0.0-master/Fluid/Machines/StaticCentrifugalPump.mo:63:3-64:67: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/Machines/StaticCentrifugalPump.mo:65:3-66:65: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/Machines/StodolaTurbine.mo:65:3-66:54:writable] Warning: Connector Ce 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/Machines/StodolaTurbine.mo:67:3-68:52:writable] Warning: Connector Cs 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/Machines/StodolaTurbine.mo:72:3-76:23:writable] Warning: Connector M is not balanced: The number of potential variables (2) is not equal to the number of flow variables (0). [/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermoSysPro 4.0.0-master/Fluid/HeatExchangers/SimpleDynamicCondenser.mo:119:3-120:52:writable] Warning: Connector Cv 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/SimpleDynamicCondenser.mo:121:3-122:53:writable] Warning: Connector Cl 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/SimpleDynamicCondenser.mo:129:3-130:55: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/SimpleDynamicCondenser.mo:131:3-132:53: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/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/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/Volumes/VolumeATh.mo:104:3-105:67:writable] Warning: Connector Ce1 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/Volumes/VolumeATh.mo:106:3-108:57:writable] Warning: Connector Ce2 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/Volumes/VolumeATh.mo:109:3-110:73:writable] Warning: Connector Cs1 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/Volumes/VolumeATh.mo:111:3-112:75:writable] Warning: Connector Cs2 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 0.0007585/2.278, allocations: 402 kB / 0.7584 GB, free: 156 kB / 0.5919 GB Notification: Performance of NFTyping.typeBindings: time 0.000935/2.279, allocations: 0.5701 MB / 0.759 GB, free: 144 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. [/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermoSysPro 4.0.0-master/Properties/WaterSteam/IF97_packages.mo:1445:9-1445:35:writable] Warning: h 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_Ps.mo:71:3-71:60: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_Ps.mo:71:3-71:60: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. Notification: Performance of NFTyping.typeClassSections: time 0.04056/2.319, allocations: 17.66 MB / 0.7762 GB, free: 15.51 MB / 0.6075 GB Notification: Performance of NFFlatten.flatten: time 0.002303/2.321, allocations: 2.052 MB / 0.7782 GB, free: 15.3 MB / 0.6075 GB Notification: Performance of NFFlatten.resolveConnections: time 0.000842/2.322, allocations: 0.842 MB / 0.779 GB, free: 14.98 MB / 0.6075 GB Notification: Performance of NFEvalConstants.evaluate: time 0.0009943/2.323, allocations: 0.8162 MB / 0.7798 GB, free: 14.89 MB / 0.6075 GB Notification: Performance of NFSimplifyModel.simplify: time 0.0007436/2.324, allocations: 0.7693 MB / 0.7806 GB, free: 14.75 MB / 0.6075 GB Notification: Performance of NFPackage.collectConstants: time 0.0001596/2.324, allocations: 145.8 kB / 0.7807 GB, free: 14.75 MB / 0.6075 GB Notification: Performance of NFFlatten.collectFunctions: time 0.07665/2.401, allocations: 29.04 MB / 0.8091 GB, free: 2.281 MB / 0.6075 GB Notification: Performance of NFScalarize.scalarize: time 0.0006087/2.402, allocations: 364 kB / 0.8094 GB, free: 1.977 MB / 0.6075 GB Notification: Performance of NFVerifyModel.verify: time 0.001565/2.403, allocations: 0.819 MB / 0.8102 GB, free: 1.156 MB / 0.6075 GB Notification: Performance of NFConvertDAE.convert: time 0.03634/2.439, allocations: 15.36 MB / 0.8252 GB, free: 2.668 MB / 0.6231 GB Notification: Performance of FrontEnd - DAE generated: time 5.871e-06/2.44, allocations: 0 / 0.8252 GB, free: 2.668 MB / 0.6231 GB Notification: Performance of FrontEnd: time 1.693e-06/2.44, allocations: 0 / 0.8252 GB, free: 2.668 MB / 0.6231 GB Notification: Performance of Transformations before backend: time 6.526e-05/2.44, allocations: 0 / 0.8252 GB, free: 2.668 MB / 0.6231 GB Notification: Model statistics after passing the front-end and creating the data structures used by the back-end: * Number of equations: 424 * Number of variables: 424 Notification: Performance of Generate backend data structure: time 0.0109/2.45, allocations: 3.743 MB / 0.8289 GB, free: 14.86 MB / 0.6387 GB Notification: Performance of prepare preOptimizeDAE: time 5.474e-05/2.451, allocations: 12.03 kB / 0.8289 GB, free: 14.84 MB / 0.6387 GB Notification: Performance of preOpt normalInlineFunction (simulation): time 0.0004623/2.451, allocations: 190.8 kB / 0.8291 GB, free: 14.66 MB / 0.6387 GB Notification: Performance of preOpt evaluateParameters (simulation): time 0.001339/2.452, allocations: 0.6927 MB / 0.8297 GB, free: 13.93 MB / 0.6387 GB Notification: Performance of preOpt simplifyIfEquations (simulation): time 0.0002178/2.453, allocations: 174 kB / 0.8299 GB, free: 13.75 MB / 0.6387 GB Notification: Performance of preOpt expandDerOperator (simulation): time 0.0002353/2.453, allocations: 128 kB / 0.83 GB, free: 13.62 MB / 0.6387 GB Notification: Performance of preOpt clockPartitioning (simulation): time 0.002869/2.456, allocations: 1.722 MB / 0.8317 GB, free: 11.76 MB / 0.6387 GB Notification: Performance of preOpt findStateOrder (simulation): time 3.11e-05/2.456, allocations: 7.938 kB / 0.8317 GB, free: 11.75 MB / 0.6387 GB Notification: Performance of preOpt replaceEdgeChange (simulation): time 0.0001168/2.456, allocations: 64 kB / 0.8318 GB, free: 11.69 MB / 0.6387 GB Notification: Performance of preOpt inlineArrayEqn (simulation): time 5.467e-05/2.456, allocations: 51.97 kB / 0.8318 GB, free: 11.64 MB / 0.6387 GB Notification: Performance of preOpt removeEqualRHS (simulation): time 0.002563/2.459, allocations: 1.324 MB / 0.8331 GB, free: 10.31 MB / 0.6387 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 0.0161/2.475, allocations: 13.28 MB / 0.8461 GB, free: 11.81 MB / 0.6544 GB Notification: Performance of preOpt comSubExp (simulation): time 0.001431/2.476, allocations: 0.8037 MB / 0.8469 GB, free: 10.98 MB / 0.6544 GB Notification: Performance of preOpt resolveLoops (simulation): time 0.0009199/2.477, allocations: 0.5429 MB / 0.8474 GB, free: 10.44 MB / 0.6544 GB Notification: Performance of preOpt evalFunc (simulation): time 0.8855/3.363, allocations: 378.2 MB / 1.217 GB, free: 240.5 MB / 0.8262 GB Notification: Performance of preOpt encapsulateWhenConditions (simulation): time 5.423e-05/3.363, allocations: 42.92 kB / 1.217 GB, free: 240.4 MB / 0.8262 GB Notification: Performance of pre-optimization done (n=146): time 3.817e-06/3.363, allocations: 0 / 1.217 GB, free: 240.4 MB / 0.8262 GB Notification: Performance of matching and sorting (n=147): time 0.01347/3.376, allocations: 4.919 MB / 1.222 GB, free: 236.6 MB / 0.8262 GB Notification: Performance of inlineWhenForInitialization (initialization): time 2.328e-05/3.376, allocations: 59.97 kB / 1.222 GB, free: 236.5 MB / 0.8262 GB Notification: Performance of selectInitializationVariablesDAE (initialization): time 0.0009982/3.377, allocations: 0.8232 MB / 1.222 GB, free: 235.9 MB / 0.8262 GB Notification: Performance of collectPreVariables (initialization): time 5.973e-05/3.377, allocations: 41.52 kB / 1.222 GB, free: 235.8 MB / 0.8262 GB [/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermoSysPro 4.0.0-master/Thermal/BoundaryConditions/HeatSource.mo:5:3-6:72:writable] Warning: The parameter heatSource.W0[1] has fixed = false and a binding equation heatSource.W0[1] = 2e6, which is probably redundant. Setting fixed = false usually means there is an additional initial equation to determine the parameter value. The binding was ignored by old Modelica tools, but this is not according to the Modelica specification. Please remove the parameter binding, or bind the parameter to another parameter with fixed = false and no binding. [/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermoSysPro 4.0.0-master/Fluid/Machines/StaticCentrifugalPump.mo:24:3-25:69:writable] Warning: The parameter staticCentrifugalPump.a1 has fixed = false and a binding equation staticCentrifugalPump.a1 = -88.67, which is probably redundant. Setting fixed = false usually means there is an additional initial equation to determine the parameter value. The binding was ignored by old Modelica tools, but this is not according to the Modelica specification. Please remove the parameter binding, or bind the parameter to another parameter with fixed = false and no binding. Notification: Performance of collectInitialEqns (initialization): time 0.0004126/3.378, allocations: 0.6763 MB / 1.223 GB, free: 235.4 MB / 0.8262 GB Notification: Performance of collectInitialBindings (initialization): time 0.0003226/3.378, allocations: 0.5124 MB / 1.224 GB, free: 235 MB / 0.8262 GB Notification: Performance of simplifyInitialFunctions (initialization): time 0.0004686/3.379, allocations: 309.3 kB / 1.224 GB, free: 234.8 MB / 0.8262 GB Notification: Performance of setup shared object (initialization): time 7.958e-05/3.379, allocations: 355.4 kB / 1.224 GB, free: 234.5 MB / 0.8262 GB Notification: Performance of preBalanceInitialSystem (initialization): time 0.0008329/3.379, allocations: 475.5 kB / 1.225 GB, free: 234.2 MB / 0.8262 GB Notification: Performance of partitionIndependentBlocks (initialization): time 0.0009877/3.38, allocations: 1.024 MB / 1.226 GB, free: 233 MB / 0.8262 GB Notification: It was not possible to check the given initialization system for consistency symbolically, because the relevant equations are part of an algebraic loop. This is not supported yet. Notification: Performance of analyzeInitialSystem (initialization): time 0.01102/3.392, allocations: 4.68 MB / 1.23 GB, free: 228.1 MB / 0.8262 GB Notification: Performance of solveInitialSystemEqSystem (initialization): time 2.072e-05/3.392, allocations: 8 kB / 1.23 GB, free: 228.1 MB / 0.8262 GB Notification: Performance of matching and sorting (n=243) (initialization): time 0.004079/3.396, allocations: 2.137 MB / 1.232 GB, free: 226 MB / 0.8262 GB Notification: Performance of prepare postOptimizeDAE: time 2.987e-05/3.396, allocations: 15.98 kB / 1.232 GB, free: 226 MB / 0.8262 GB Notification: Performance of postOpt simplifyComplexFunction (initialization): time 3.902e-05/3.396, allocations: 20 kB / 1.232 GB, free: 226 MB / 0.8262 GB Notification: Performance of postOpt tearingSystem (initialization): time 0.003021/3.399, allocations: 1.043 MB / 1.233 GB, free: 225 MB / 0.8262 GB Notification: Performance of postOpt solveSimpleEquations (initialization): time 0.000645/3.399, allocations: 211.4 kB / 1.234 GB, free: 224.8 MB / 0.8262 GB Notification: Performance of postOpt calculateStrongComponentJacobians (initialization): time 0.004258/3.404, allocations: 4.877 MB / 1.238 GB, free: 219.7 MB / 0.8262 GB Notification: Performance of postOpt simplifyAllExpressions (initialization): time 0.001048/3.405, allocations: 59.97 kB / 1.238 GB, free: 219.6 MB / 0.8262 GB Notification: Performance of postOpt collapseArrayExpressions (initialization): time 0.0001469/3.405, allocations: 71.98 kB / 1.239 GB, free: 219.6 MB / 0.8262 GB Warning: The initial conditions are over specified. The following 2 initial equations are redundant, so they are removed from the initialization system: volumeA.P = $START.volumeA.P stodolaTurbine.proe.x = $START.stodolaTurbine.proe.x. Notification: Model statistics after passing the back-end for initialization: * Number of independent subsystems: 82 * Number of states: 0 () * Number of discrete variables: 24 (volumeA.fluid1,sourcePCaloporteur.fluid1,volumeA.Cs2.ftype,volumeA.Cs1.ftype,volumeA.Ce1.ftype,Condenseur.Cl.ftype,volumeA.fluids[1],sourcePCaloporteur.C.ftype,staticCentrifugalPump.fluid,stodolaTurbine.fluid,Condenseur.fluid_p,puitsPCaloporteur.fluid,volumeA.Cs2.diff_on_1,Condenseur.Cv.diff_on_1,volumeA.Cs1.diff_on_1,volumeA.Ce2.diff_on_2,Condenseur.Cl.diff_on_2,volumeA.Ce1.diff_on_2,volumeA.Cs1.diff_on_2,volumeA.Ce1.diff_on_1,Condenseur.Cl.diff_on_1,staticCentrifugalPump.C2.diff_on_1,Condenseur.Cv.diff_on_2,volumeA.Cs2.diff_on_2) * Number of discrete states: 0 () * Number of clocked states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for initialization (131): * Single equations (assignments): 122 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 4 * When equations: 0 * If-equations: 0 * Equation systems (not torn): 0 * Torn equation systems: 5 * Mixed (continuous/discrete) equation systems: 0 Notification: Torn system details for strict tearing set: * Linear torn systems (#iteration vars, #inner vars, density): 1 system {(4,1,62.5%)} * Non-linear torn systems (#iteration vars, #inner vars): 4 systems {(1,5), (1,2), (1,2), (5,12)} Notification: Performance of prepare postOptimizeDAE: time 0.0006434/3.406, allocations: 327.6 kB / 1.239 GB, free: 219.3 MB / 0.8262 GB Notification: Performance of postOpt lateInlineFunction (simulation): time 0.0002307/3.406, allocations: 123.2 kB / 1.239 GB, free: 219.1 MB / 0.8262 GB Notification: Performance of postOpt wrapFunctionCalls (simulation): time 0.003374/3.409, allocations: 2.231 MB / 1.241 GB, free: 216.9 MB / 0.8262 GB Notification: Performance of postOpt simplifysemiLinear (simulation): time 1.052e-05/3.409, allocations: 11.92 kB / 1.241 GB, free: 216.9 MB / 0.8262 GB Notification: Performance of postOpt simplifyComplexFunction (simulation): time 9.568e-06/3.409, allocations: 0.5625 kB / 1.241 GB, free: 216.9 MB / 0.8262 GB Notification: Performance of postOpt removeConstants (simulation): time 0.0004222/3.41, allocations: 288.6 kB / 1.241 GB, free: 216.6 MB / 0.8262 GB Notification: Performance of postOpt simplifyTimeIndepFuncCalls (simulation): time 0.0001655/3.41, allocations: 12 kB / 1.241 GB, free: 216.6 MB / 0.8262 GB Notification: Performance of postOpt simplifyAllExpressions (simulation): time 0.0005967/3.41, allocations: 35.97 kB / 1.241 GB, free: 216.6 MB / 0.8262 GB Notification: Performance of postOpt findZeroCrossings (simulation): time 0.0001348/3.411, allocations: 52.42 kB / 1.242 GB, free: 216.5 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(stodolaTurbine.Te, stodolaTurbine.proe.d, stodolaTurbine.proe.u, stodolaTurbine.proe.s, stodolaTurbine.proe.cp, stodolaTurbine.proe.ddhp, stodolaTurbine.proe.ddph, stodolaTurbine.proe.duph, stodolaTurbine.proe.duhp, stodolaTurbine.proe.x) = $cse1 Variables: 1: volumeA.P:VARIABLE(min = 0.0 start = 7e5 unit = "Pa" fixed = true nominal = 1e5 ) "Fluid pressure" type: Real 2: $cse1.T:VARIABLE(protected = true ) type: Real unreplaceable 3: volumeA.Cs2.h:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real 4: volumeA.h:VARIABLE(start = 2e6 unit = "J/kg" ) "Fluid specific enthalpy" type: Real 5: Condenseur.Cl.h:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real 6: Condenseur.prod.T:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 320.0 ) "Temperature" type: Real 7: Condenseur.prod.duph:VARIABLE(unit = "m3/kg" ) "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real 8: Condenseur.prod.ddhp:VARIABLE(unit = "kg.s2/m5" ) "Derivative of density wrt. specific enthalpy at constant pressure" type: Real 9: Condenseur.prod.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific heat capacity at constant presure" type: Real 10: Condenseur.prod.x:VARIABLE(min = 0.0 max = 1.0 unit = "1" ) "Vapor mass fraction" type: Real [/var/lib/jenkins1/ws/OpenModelicaLibraryTestingWork/OpenModelica/OMCompiler/Compiler/BackEnd/DAEMode.mo:528:7-530:90:writable] Error: Internal error DAEMode.traverserStrongComponents failed on equation: 1/1 (1): staticCentrifugalPump.deltaP = volumeA.P - Condenseur.Pfond 2/2 (1): Condenseur.Cl.h = ThermoSysPro.Functions.SmoothCond(staticCentrifugalPump.Q / Condenseur.gamma0, Condenseur.hl, volumeA.h, 1.0) 3/3 (1): volumeA.Cs2.h = if staticCentrifugalPump.Q > 0.0 then volumeA.h else Condenseur.hv 4/4 (10): $cse1 = ThermoSysPro.Properties.Fluid.Ph(volumeA.P, volumeA.Cs2.h, stodolaTurbine.mode_e, stodolaTurbine.fluid) 5/14 (10): ThermoSysPro.Properties.WaterSteam.Common.ThermoProperties_ph(stodolaTurbine.Te, stodolaTurbine.proe.d, stodolaTurbine.proe.u, stodolaTurbine.proe.s, stodolaTurbine.proe.cp, stodolaTurbine.proe.ddhp, stodolaTurbine.proe.ddph, stodolaTurbine.proe.duph, stodolaTurbine.proe.duhp, stodolaTurbine.proe.x) = $cse1 6/24 (1): staticCentrifugalPump.Q = if noEvent(volumeA.P > stodolaTurbine.pcrit) or noEvent(stodolaTurbine.Te > stodolaTurbine.Tcrit) then sqrt((volumeA.P ^ 2.0 - Condenseur.P ^ 2.0) / (stodolaTurbine.Cst * stodolaTurbine.Te)) else sqrt((volumeA.P ^ 2.0 - Condenseur.P ^ 2.0) / (stodolaTurbine.Cst * stodolaTurbine.Te * stodolaTurbine.proe.x)) 7/25 (1): staticCentrifugalPump.Pm = 0.5 * (Condenseur.Pfond + volumeA.P) 8/26 (1): staticCentrifugalPump.rho = ThermoSysPro.Properties.Fluid.Density_Ph(staticCentrifugalPump.Pm, staticCentrifugalPump.h, staticCentrifugalPump.fluid, staticCentrifugalPump.mode, 0.0, 1.0, 0.0, 0.0) 9/27 (1): staticCentrifugalPump.Q = staticCentrifugalPump.Qv * staticCentrifugalPump.rho 10/28 (1): staticCentrifugalPump.rh = max(if noEvent(abs(staticCentrifugalPump.R) > staticCentrifugalPump.eps) then staticCentrifugalPump.b1 * staticCentrifugalPump.Qv * abs(staticCentrifugalPump.Qv) / staticCentrifugalPump.R ^ 2.0 + staticCentrifugalPump.b2 * staticCentrifugalPump.Qv / staticCentrifugalPump.R + staticCentrifugalPump.b3 else staticCentrifugalPump.b3, staticCentrifugalPump.rhmin) 11/29 (1): staticCentrifugalPump.deltaH = 9.80665 * staticCentrifugalPump.hn / staticCentrifugalPump.rh 12/30 (1): staticCentrifugalPump.deltaH = staticCentrifugalPump.C2.h - Condenseur.Cl.h 13/31 (1): 0.0 = staticCentrifugalPump.Q * (-2.501569e6 + staticCentrifugalPump.C2.h) + heatSource.W0[1] - staticCentrifugalPump.Q * volumeA.Cs2.h 14/32 (1): staticCentrifugalPump.h = 0.5 * (Condenseur.Cl.h + staticCentrifugalPump.C2.h) 15/33 (1): staticCentrifugalPump.hn = (staticCentrifugalPump.a1 * abs(staticCentrifugalPump.Qv) + staticCentrifugalPump.a2 * staticCentrifugalPump.R) * staticCentrifugalPump.Qv + staticCentrifugalPump.a3 * staticCentrifugalPump.R ^ 2.0 16/34 (1): staticCentrifugalPump.deltaP = 9.80665 * staticCentrifugalPump.rho * staticCentrifugalPump.hn 17/35 (10): Condenseur.prod = ThermoSysPro.Properties.Fluid.Ph(Condenseur.Pfond, Condenseur.Cl.h, 0, Condenseur.fluid_c) 18/45 (1): Condenseur.Pfond = if Condenseur.gravity_pressure then Condenseur.P + Condenseur.prod.d * 9.80665 * Condenseur.Vl / Condenseur.A else Condenseur.P Variables: 1: Condenseur.prod.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real 2: Condenseur.prod.ddph:VARIABLE(unit = "s2/m2" ) "Derivative of density wrt. pressure at constant specific enthalpy" type: Real 3: staticCentrifugalPump.deltaP:VARIABLE(unit = "Pa" ) "Pressure variation between the outlet and the inlet" type: Real 4: staticCentrifugalPump.hn:VARIABLE(min = 0.0 start = 71.08245675235786 unit = "m" fixed = false ) "Pump head" type: Real 5: staticCentrifugalPump.h:VARIABLE(start = 193554.9971298399 unit = "J/kg" ) "Fluid average specific enthalpy" type: Real 6: staticCentrifugalPump.Q:VARIABLE(start = 500.0 unit = "kg/s" fixed = false ) "Mass flow rate" type: Real 7: staticCentrifugalPump.C2.h:VARIABLE(flow=false start = 195297.69906611618 unit = "J/kg" ) "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real 8: staticCentrifugalPump.deltaH:VARIABLE(unit = "J/kg" ) "Specific enthalpy variation between the outlet and the inlet" type: Real 9: staticCentrifugalPump.rh:VARIABLE() "Hydraulic efficiency" type: Real 10: staticCentrifugalPump.Qv:VARIABLE(start = 0.009081311621074862 unit = "m3/s" ) "Volume flow rate" type: Real 11: staticCentrifugalPump.rho:VARIABLE(min = 0.0 start = 998.0 unit = "kg/m3" ) "Fluid density" type: Real 12: staticCentrifugalPump.Pm:VARIABLE(min = 0.0 start = 355000.00000015664 unit = "Pa" nominal = 1e5 ) "Fluid average pressure" type: Real 13: stodolaTurbine.Te:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 300.0 ) "Temperature at the inlet" type: Real 14: $cse1.duph:VARIABLE(protected = true ) type: Real unreplaceable 15: stodolaTurbine.proe.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific inner energy" type: Real 16: stodolaTurbine.proe.ddph:VARIABLE(unit = "s2/m2" ) "Derivative of density wrt. pressure at constant specific enthalpy" type: Real 17: stodolaTurbine.proe.duhp:VARIABLE(unit = "1" ) "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real 18: stodolaTurbine.proe.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific heat capacity at constant presure" type: Real 19: stodolaTurbine.proe.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real 20: stodolaTurbine.proe.duph:VARIABLE(unit = "m3/kg" ) "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real 21: stodolaTurbine.proe.x:VARIABLE(min = 0.0 max = 1.0 start = 1.0 unit = "1" fixed = true ) "Vapor mass fraction" type: Real 22: stodolaTurbine.proe.ddhp:VARIABLE(unit = "kg.s2/m5" ) "Derivative of density wrt. specific enthalpy at constant pressure" type: Real 23: stodolaTurbine.proe.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real 24: $cse1.cp:VARIABLE(protected = true ) type: Real unreplaceable 25: $cse1.ddph:VARIABLE(protected = true ) type: Real unreplaceable 26: $cse1.u:VARIABLE(protected = true ) type: Real unreplaceable 27: $cse1.duhp:VARIABLE(protected = true ) type: Real unreplaceable 28: $cse1.s:VARIABLE(protected = true ) type: Real unreplaceable 29: $cse1.d:VARIABLE(protected = true ) type: Real unreplaceable 30: $cse1.x:VARIABLE(protected = true ) type: Real unreplaceable 31: $cse1.ddhp:VARIABLE(protected = true ) type: Real unreplaceable 32: volumeA.P:VARIABLE(min = 0.0 start = 7e5 unit = "Pa" fixed = true nominal = 1e5 ) "Fluid pressure" type: Real 33: $cse1.T:VARIABLE(protected = true ) type: Real unreplaceable 34: volumeA.Cs2.h:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real 35: volumeA.h:VARIABLE(start = 2e6 unit = "J/kg" ) "Fluid specific enthalpy" type: Real 36: Condenseur.Cl.h:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real 37: Condenseur.prod.T:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 320.0 ) "Temperature" type: Real 38: Condenseur.prod.duph:VARIABLE(unit = "m3/kg" ) "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real 39: Condenseur.prod.ddhp:VARIABLE(unit = "kg.s2/m5" ) "Derivative of density wrt. specific enthalpy at constant pressure" type: Real 40: Condenseur.prod.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific heat capacity at constant presure" type: Real 41: Condenseur.prod.x:VARIABLE(min = 0.0 max = 1.0 unit = "1" ) "Vapor mass fraction" type: Real 42: Condenseur.prod.duhp:VARIABLE(unit = "1" ) "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real 43: Condenseur.prod.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific inner energy" type: Real 44: Condenseur.prod.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real 45: Condenseur.Pfond:VARIABLE(min = 0.0 start = 1e4 unit = "Pa" nominal = 1e5 ) "Fluid pressure at the bottom of the cavity" 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 postOpt createDAEmodeBDAE (simulation): time 0.002364/3.413, allocations: 1.541 MB / 1.243 GB, free: 214.8 MB / 0.8262 GB Error: post-optimization module createDAEmodeBDAE (simulation) failed. Error: Internal error SimCode DAEmode: The model ThermoSysPro.Fluid.Examples.SimpleExamples.TestSimpleDynamicCondenser1 could not be translated