Running: ./testmodel.py --libraries=/home/hudson/saved_omc/libraries/.openmodelica/libraries --ompython_omhome=/usr ClaRa_dev_ClaRa.Examples.VapourCycle_01.conf.json loadFile("/home/hudson/saved_omc/libraries/.openmodelica/libraries/SMArtInt main/package.mo", uses=false) [Timeout 180] "Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/SMArtInt main/package.mo): time 0.01209/0.01209, allocations: 1.773 MB / 18.82 MB, free: 4.246 MB / 14.72 MB " [Timeout remaining time 180] loadFile("/home/hudson/saved_omc/libraries/.openmodelica/libraries/ModelicaServices 4.1.0+maint.om/package.mo", uses=false) [Timeout 180] "Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/ModelicaServices 4.1.0+maint.om/package.mo): time 0.001321/0.001321, allocations: 111.6 kB / 22.07 MB, free: 0.9922 MB / 14.72 MB " [Timeout remaining time 180] loadFile("/home/hudson/saved_omc/libraries/.openmodelica/libraries/Complex 4.1.0+maint.om/package.mo", uses=false) [Timeout 180] "Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/Complex 4.1.0+maint.om/package.mo): time 0.001855/0.001855, allocations: 209.2 kB / 25.45 MB, free: 3.25 MB / 14.72 MB " [Timeout remaining time 180] loadFile("/home/hudson/saved_omc/libraries/.openmodelica/libraries/Modelica 4.1.0+maint.om/package.mo", uses=false) [Timeout 180] "Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/Modelica 4.1.0+maint.om/package.mo): time 1.456/1.456, allocations: 230.6 MB / 259.3 MB, free: 13.15 MB / 206.1 MB " [Timeout remaining time 178] loadFile("/home/hudson/saved_omc/libraries/.openmodelica/libraries/ClaRa main/package.mo", uses=false) [Timeout 180] "Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/ClaRa main/package.mo): time 1.097/1.097, allocations: 130.5 MB / 446.3 MB, free: 14.92 MB / 350.1 MB " [Timeout remaining time 179] Using package ClaRa with version 1.9.0 (/home/hudson/saved_omc/libraries/.openmodelica/libraries/ClaRa main/package.mo) Using package Modelica with version 4.1.0 (/home/hudson/saved_omc/libraries/.openmodelica/libraries/Modelica 4.1.0+maint.om/package.mo) Using package Complex with version 4.1.0 (/home/hudson/saved_omc/libraries/.openmodelica/libraries/Complex 4.1.0+maint.om/package.mo) Using package ModelicaServices with version 4.1.0 (/home/hudson/saved_omc/libraries/.openmodelica/libraries/ModelicaServices 4.1.0+maint.om/package.mo) Using package SMArtInt with version 0.3.1 (/home/hudson/saved_omc/libraries/.openmodelica/libraries/SMArtInt main/package.mo) Running command: translateModel(ClaRa.Examples.VapourCycle_01,tolerance=1e-05,outputFormat="mat",numberOfIntervals=2500,variableFilter="Time|condenser.finWall.U.1.|condenser.finWall.U.2.|condenser.finWall.U.3.|condenser.finWall.U.4.|condenser.finWall.U.5.|condenser.finWall.U.6.|condenser.finWall.U.7.|condenser.finWall.U.8.|condenser.finWall.U.9.|condenser.flow_a.h.1.|condenser.flow_a.h.2.|condenser.flow_a.h.3.|condenser.flow_a.h.4.|condenser.flow_a.h.5.|condenser.flow_a.h.6.|condenser.flow_a.h.7.|condenser.flow_a.h.8.|condenser.flow_a.h.9.|condenser.flow_a.p.1.|condenser.flow_a.p.2.|condenser.flow_a.p.3.|condenser.flow_a.p.4.|condenser.flow_a.p.5.|condenser.flow_a.p.6.|condenser.flow_a.p.7.|condenser.flow_a.p.8.|condenser.flow_a.p.9.|condenser.flow_b.h.1.|condenser.flow_b.h.2.|condenser.flow_b.h.3.|condenser.flow_b.h.4.|condenser.flow_b.h.5.|condenser.flow_b.h.6.|condenser.flow_b.h.7.|condenser.flow_b.h.8.|condenser.flow_b.h.9.|condenser.flow_b.p.1.|condenser.flow_b.p.2.|condenser.flow_b.p.3.|condenser.flow_b.p.4.|condenser.flow_b.p.5.|condenser.flow_b.p.6.|condenser.flow_b.p.7.|condenser.flow_b.p.8.|condenser.flow_b.p.9.|condenser.flow_b.xi.1,1.|condenser.flow_b.xi.1,2.|condenser.flow_b.xi.1,3.|condenser.flow_b.xi.1,4.|condenser.flow_b.xi.1,5.|condenser.flow_b.xi.1,6.|condenser.flow_b.xi.1,7.|condenser.flow_b.xi.1,8.|condenser.flow_b.xi.1,9.|condenser.flow_b.xi.2,1.|condenser.flow_b.xi.2,2.|condenser.flow_b.xi.2,3.|condenser.flow_b.xi.2,4.|condenser.flow_b.xi.2,5.|condenser.flow_b.xi.2,6.|condenser.flow_b.xi.2,7.|condenser.flow_b.xi.2,8.|condenser.flow_b.xi.2,9.|condenser.flow_b.xi.3,1.|condenser.flow_b.xi.3,2.|condenser.flow_b.xi.3,3.|condenser.flow_b.xi.3,4.|condenser.flow_b.xi.3,5.|condenser.flow_b.xi.3,6.|condenser.flow_b.xi.3,7.|condenser.flow_b.xi.3,8.|condenser.flow_b.xi.3,9.|condenser.flow_b.xi.4,1.|condenser.flow_b.xi.4,2.|condenser.flow_b.xi.4,3.|condenser.flow_b.xi.4,4.|condenser.flow_b.xi.4,5.|condenser.flow_b.xi.4,6.|condenser.flow_b.xi.4,7.|condenser.flow_b.xi.4,8.|condenser.flow_b.xi.4,9.|condenser.flow_b.xi.5,1.|condenser.flow_b.xi.5,2.|condenser.flow_b.xi.5,3.|condenser.flow_b.xi.5,4.|condenser.flow_b.xi.5,5.|condenser.flow_b.xi.5,6.|condenser.flow_b.xi.5,7.|condenser.flow_b.xi.5,8.|condenser.flow_b.xi.5,9.|condenser.flow_b.xi.6,1.|condenser.flow_b.xi.6,2.|condenser.flow_b.xi.6,3.|condenser.flow_b.xi.6,4.|condenser.flow_b.xi.6,5.|condenser.flow_b.xi.6,6.|condenser.flow_b.xi.6,7.|condenser.flow_b.xi.6,8.|condenser.flow_b.xi.6,9.|condenser.flow_b.xi.7,1.|condenser.flow_b.xi.7,2.|condenser.flow_b.xi.7,3.|condenser.flow_b.xi.7,4.|condenser.flow_b.xi.7,5.|condenser.flow_b.xi.7,6.|condenser.flow_b.xi.7,7.|condenser.flow_b.xi.7,8.|condenser.flow_b.xi.7,9.|condenser.flow_b.xi.8,1.|condenser.flow_b.xi.8,2.|condenser.flow_b.xi.8,3.|condenser.flow_b.xi.8,4.|condenser.flow_b.xi.8,5.|condenser.flow_b.xi.8,6.|condenser.flow_b.xi.8,7.|condenser.flow_b.xi.8,8.|condenser.flow_b.xi.8,9.|condenser.flow_b.xi.9,1.|condenser.flow_b.xi.9,2.|condenser.flow_b.xi.9,3.|condenser.flow_b.xi.9,4.|condenser.flow_b.xi.9,5.|condenser.flow_b.xi.9,6.|condenser.flow_b.xi.9,7.|condenser.flow_b.xi.9,8.|condenser.flow_b.xi.9,9.|condenser.tubeWall.U.1.|condenser.tubeWall.U.2.|condenser.tubeWall.U.3.|condenser.tubeWall.U.4.|condenser.tubeWall.U.5.|condenser.tubeWall.U.6.|condenser.tubeWall.U.7.|condenser.tubeWall.U.8.|condenser.tubeWall.U.9.|plateHEX.flow_a.h.1.|plateHEX.flow_a.h.2.|plateHEX.flow_a.h.3.|plateHEX.flow_a.h.4.|plateHEX.flow_a.h.5.|plateHEX.flow_a.p.1.|plateHEX.flow_a.p.2.|plateHEX.flow_a.p.3.|plateHEX.flow_a.p.4.|plateHEX.flow_a.p.5.|plateHEX.flow_b.h.1.|plateHEX.flow_b.h.2.|plateHEX.flow_b.h.3.|plateHEX.flow_b.h.4.|plateHEX.flow_b.h.5.|plateHEX.flow_b.p.1.|plateHEX.flow_b.p.2.|plateHEX.flow_b.p.3.|plateHEX.flow_b.p.4.|plateHEX.flow_b.p.5.|plateHEX.thinWall.U.1.|plateHEX.thinWall.U.2.|plateHEX.thinWall.U.3.|plateHEX.thinWall.U.4.|plateHEX.thinWall.U.5.|steamSeparator.volume.h_liq|steamSeparator.volume.h_vap|steamSeparator.volume.p_vap|steamSeparator.volume.volume_vap|tube.h.1.|tube.h.2.|tube.h.3.|tube.p.1.|tube.p.2.|tube.p.3.",fileNamePrefix="ClaRa_dev_ClaRa.Examples.VapourCycle_01") translateModel(ClaRa.Examples.VapourCycle_01,tolerance=1e-05,outputFormat="mat",numberOfIntervals=2500,variableFilter="Time|condenser.finWall.U.1.|condenser.finWall.U.2.|condenser.finWall.U.3.|condenser.finWall.U.4.|condenser.finWall.U.5.|condenser.finWall.U.6.|condenser.finWall.U.7.|condenser.finWall.U.8.|condenser.finWall.U.9.|condenser.flow_a.h.1.|condenser.flow_a.h.2.|condenser.flow_a.h.3.|condenser.flow_a.h.4.|condenser.flow_a.h.5.|condenser.flow_a.h.6.|condenser.flow_a.h.7.|condenser.flow_a.h.8.|condenser.flow_a.h.9.|condenser.flow_a.p.1.|condenser.flow_a.p.2.|condenser.flow_a.p.3.|condenser.flow_a.p.4.|condenser.flow_a.p.5.|condenser.flow_a.p.6.|condenser.flow_a.p.7.|condenser.flow_a.p.8.|condenser.flow_a.p.9.|condenser.flow_b.h.1.|condenser.flow_b.h.2.|condenser.flow_b.h.3.|condenser.flow_b.h.4.|condenser.flow_b.h.5.|condenser.flow_b.h.6.|condenser.flow_b.h.7.|condenser.flow_b.h.8.|condenser.flow_b.h.9.|condenser.flow_b.p.1.|condenser.flow_b.p.2.|condenser.flow_b.p.3.|condenser.flow_b.p.4.|condenser.flow_b.p.5.|condenser.flow_b.p.6.|condenser.flow_b.p.7.|condenser.flow_b.p.8.|condenser.flow_b.p.9.|condenser.flow_b.xi.1,1.|condenser.flow_b.xi.1,2.|condenser.flow_b.xi.1,3.|condenser.flow_b.xi.1,4.|condenser.flow_b.xi.1,5.|condenser.flow_b.xi.1,6.|condenser.flow_b.xi.1,7.|condenser.flow_b.xi.1,8.|condenser.flow_b.xi.1,9.|condenser.flow_b.xi.2,1.|condenser.flow_b.xi.2,2.|condenser.flow_b.xi.2,3.|condenser.flow_b.xi.2,4.|condenser.flow_b.xi.2,5.|condenser.flow_b.xi.2,6.|condenser.flow_b.xi.2,7.|condenser.flow_b.xi.2,8.|condenser.flow_b.xi.2,9.|condenser.flow_b.xi.3,1.|condenser.flow_b.xi.3,2.|condenser.flow_b.xi.3,3.|condenser.flow_b.xi.3,4.|condenser.flow_b.xi.3,5.|condenser.flow_b.xi.3,6.|condenser.flow_b.xi.3,7.|condenser.flow_b.xi.3,8.|condenser.flow_b.xi.3,9.|condenser.flow_b.xi.4,1.|condenser.flow_b.xi.4,2.|condenser.flow_b.xi.4,3.|condenser.flow_b.xi.4,4.|condenser.flow_b.xi.4,5.|condenser.flow_b.xi.4,6.|condenser.flow_b.xi.4,7.|condenser.flow_b.xi.4,8.|condenser.flow_b.xi.4,9.|condenser.flow_b.xi.5,1.|condenser.flow_b.xi.5,2.|condenser.flow_b.xi.5,3.|condenser.flow_b.xi.5,4.|condenser.flow_b.xi.5,5.|condenser.flow_b.xi.5,6.|condenser.flow_b.xi.5,7.|condenser.flow_b.xi.5,8.|condenser.flow_b.xi.5,9.|condenser.flow_b.xi.6,1.|condenser.flow_b.xi.6,2.|condenser.flow_b.xi.6,3.|condenser.flow_b.xi.6,4.|condenser.flow_b.xi.6,5.|condenser.flow_b.xi.6,6.|condenser.flow_b.xi.6,7.|condenser.flow_b.xi.6,8.|condenser.flow_b.xi.6,9.|condenser.flow_b.xi.7,1.|condenser.flow_b.xi.7,2.|condenser.flow_b.xi.7,3.|condenser.flow_b.xi.7,4.|condenser.flow_b.xi.7,5.|condenser.flow_b.xi.7,6.|condenser.flow_b.xi.7,7.|condenser.flow_b.xi.7,8.|condenser.flow_b.xi.7,9.|condenser.flow_b.xi.8,1.|condenser.flow_b.xi.8,2.|condenser.flow_b.xi.8,3.|condenser.flow_b.xi.8,4.|condenser.flow_b.xi.8,5.|condenser.flow_b.xi.8,6.|condenser.flow_b.xi.8,7.|condenser.flow_b.xi.8,8.|condenser.flow_b.xi.8,9.|condenser.flow_b.xi.9,1.|condenser.flow_b.xi.9,2.|condenser.flow_b.xi.9,3.|condenser.flow_b.xi.9,4.|condenser.flow_b.xi.9,5.|condenser.flow_b.xi.9,6.|condenser.flow_b.xi.9,7.|condenser.flow_b.xi.9,8.|condenser.flow_b.xi.9,9.|condenser.tubeWall.U.1.|condenser.tubeWall.U.2.|condenser.tubeWall.U.3.|condenser.tubeWall.U.4.|condenser.tubeWall.U.5.|condenser.tubeWall.U.6.|condenser.tubeWall.U.7.|condenser.tubeWall.U.8.|condenser.tubeWall.U.9.|plateHEX.flow_a.h.1.|plateHEX.flow_a.h.2.|plateHEX.flow_a.h.3.|plateHEX.flow_a.h.4.|plateHEX.flow_a.h.5.|plateHEX.flow_a.p.1.|plateHEX.flow_a.p.2.|plateHEX.flow_a.p.3.|plateHEX.flow_a.p.4.|plateHEX.flow_a.p.5.|plateHEX.flow_b.h.1.|plateHEX.flow_b.h.2.|plateHEX.flow_b.h.3.|plateHEX.flow_b.h.4.|plateHEX.flow_b.h.5.|plateHEX.flow_b.p.1.|plateHEX.flow_b.p.2.|plateHEX.flow_b.p.3.|plateHEX.flow_b.p.4.|plateHEX.flow_b.p.5.|plateHEX.thinWall.U.1.|plateHEX.thinWall.U.2.|plateHEX.thinWall.U.3.|plateHEX.thinWall.U.4.|plateHEX.thinWall.U.5.|steamSeparator.volume.h_liq|steamSeparator.volume.h_vap|steamSeparator.volume.p_vap|steamSeparator.volume.volume_vap|tube.h.1.|tube.h.2.|tube.h.3.|tube.p.1.|tube.p.2.|tube.p.3.",fileNamePrefix="ClaRa_dev_ClaRa.Examples.VapourCycle_01") [Timeout 800] "Notification: SMArtInt requested package Modelica of version 4.0.0. Modelica 4.1.0 is used instead which states that it is fully compatible without conversion script needed. Notification: ClaRa requested package Modelica of version 4.0.0. Modelica 4.1.0 is used instead which states that it is fully compatible without conversion script needed. Notification: Automatically loaded package TILMedia 1.9.0 ClaRa due to uses annotation from ClaRa. Notification: TILMedia requested package Modelica of version 4.0.0. Modelica 4.1.0 is used instead which states that it is fully compatible without conversion script needed. Warning: Requested package SMArtInt of version 0.5.1, but this package was already loaded with version 0.3.1. There are no conversion annotations for this version but 0.5.1 is newer than 0.3.1. There is a possibility that 0.3.1 remains backwards compatible, but it is not loaded so OpenModelica cannot verify this. Notification: Performance of FrontEnd - loaded program: time 0.3894/0.3894, allocations: 46.15 MB / 0.6556 GB, free: 30.64 MB / 0.4982 GB Notification: Performance of FrontEnd - Absyn->SCode: time 0.1804/0.5698, allocations: 89.05 MB / 0.7426 GB, free: 2.48 MB / 0.545 GB Notification: Performance of NFInst.instantiate(ClaRa.Examples.VapourCycle_01): time 0.0498/0.6196, allocations: 43.58 MB / 0.7851 GB, free: 6.73 MB / 0.5919 GB Notification: Performance of NFInst.instExpressions: time 0.08227/0.7019, allocations: 45.88 MB / 0.8299 GB, free: 8.715 MB / 0.6388 GB Notification: Performance of NFInst.updateImplicitVariability: time 0.01213/0.714, allocations: 246.3 kB / 0.8302 GB, free: 8.473 MB / 0.6388 GB [/home/hudson/saved_omc/libraries/.openmodelica/libraries/ClaRa main/SimCenter.mo:71:5-72:35:writable] Warning: Connector cycleSumPort is not balanced: The number of potential variables (0) is not equal to the number of flow variables (4). Notification: Performance of NFTyping.typeComponents: time 0.0151/0.7291, allocations: 5.516 MB / 0.8356 GB, free: 2.93 MB / 0.6388 GB Notification: Performance of NFTyping.typeBindings: time 0.02739/0.7565, allocations: 9.443 MB / 0.8448 GB, free: 9.445 MB / 0.6544 GB Notification: Performance of NFTyping.typeClassSections: time 0.03111/0.7876, allocations: 9.778 MB / 0.8543 GB, free: 15.65 MB / 0.67 GB Notification: Performance of NFFlatten.flatten: time 0.8659/1.654, allocations: 41.85 MB / 0.8952 GB, free: 19.21 MB / 0.6702 GB Notification: Performance of NFFlatten.resolveConnections: time 0.02765/1.681, allocations: 14.78 MB / 0.9096 GB, free: 18.58 MB / 0.6702 GB Notification: Performance of NFEvalConstants.evaluate: time 0.03664/1.718, allocations: 16.31 MB / 0.9256 GB, free: 16.93 MB / 0.6702 GB Notification: Performance of NFSimplifyModel.simplify: time 0.03765/1.755, allocations: 22.25 MB / 0.9473 GB, free: 7.832 MB / 0.6702 GB Notification: Performance of NFPackage.collectConstants: time 0.01863/1.774, allocations: 4.539 MB / 0.9517 GB, free: 7.832 MB / 0.6702 GB Notification: Performance of NFFlatten.collectFunctions: time 0.03306/1.807, allocations: 11.14 MB / 0.9626 GB, free: 3.746 MB / 0.6702 GB Notification: Performance of NFScalarize.scalarize: time 0.03509/1.842, allocations: 16.89 MB / 0.9791 GB, free: 3.164 MB / 0.6858 GB Notification: Performance of NFVerifyModel.verify: time 0.05196/1.894, allocations: 20.25 MB / 0.9989 GB, free: 15.04 MB / 0.717 GB Notification: Performance of NFConvertDAE.convert: time 0.1064/2.001, allocations: 66.53 MB / 1.064 GB, free: 14.59 MB / 0.7795 GB Notification: Performance of FrontEnd - DAE generated: time 7.013e-06/2.001, allocations: 3.562 kB / 1.064 GB, free: 14.59 MB / 0.7795 GB Notification: Performance of FrontEnd: time 1.994e-06/2.001, allocations: 0 / 1.064 GB, free: 14.59 MB / 0.7795 GB Notification: Performance of Transformations before backend: time 0.002096/2.003, allocations: 0 / 1.064 GB, free: 14.59 MB / 0.7795 GB Notification: Model statistics after passing the front-end and creating the data structures used by the back-end: * Number of equations: 5822 * Number of variables: 5822 Notification: Performance of Generate backend data structure: time 0.1593/2.162, allocations: 42.78 MB / 1.106 GB, free: 4.367 MB / 0.8108 GB Notification: Performance of prepare preOptimizeDAE: time 5.139e-05/2.162, allocations: 11.97 kB / 1.106 GB, free: 4.355 MB / 0.8108 GB Notification: Performance of preOpt normalInlineFunction (simulation): time 0.02379/2.186, allocations: 3.563 MB / 1.109 GB, free: 0.7734 MB / 0.8108 GB Notification: Performance of preOpt evaluateParameters (simulation): time 0.08786/2.274, allocations: 37.43 MB / 1.146 GB, free: 12.31 MB / 0.8577 GB Notification: Performance of preOpt simplifyIfEquations (simulation): time 0.001588/2.275, allocations: 1.06 MB / 1.147 GB, free: 11.29 MB / 0.8577 GB Notification: Performance of preOpt expandDerOperator (simulation): time 0.01174/2.287, allocations: 1.434 MB / 1.148 GB, free: 9.891 MB / 0.8577 GB Notification: Performance of preOpt clockPartitioning (simulation): time 0.6477/2.935, allocations: 64.18 MB / 1.211 GB, free: 253 MB / 0.9045 GB Notification: Performance of preOpt findStateOrder (simulation): time 0.0007671/2.935, allocations: 108.4 kB / 1.211 GB, free: 253 MB / 0.9045 GB Notification: Performance of preOpt replaceEdgeChange (simulation): time 0.00993/2.945, allocations: 0.686 MB / 1.212 GB, free: 253 MB / 0.9045 GB Notification: Performance of preOpt inlineArrayEqn (simulation): time 0.003474/2.949, allocations: 2.741 MB / 1.214 GB, free: 252.9 MB / 0.9045 GB Notification: Performance of preOpt removeEqualRHS (simulation): time 0.1602/3.109, allocations: 95.19 MB / 1.307 GB, free: 215.4 MB / 0.9045 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 0.3091/3.418, allocations: 215.8 MB / 1.518 GB, free: 296 kB / 0.9045 GB Notification: Performance of preOpt comSubExp (simulation): time 0.6026/4.021, allocations: 51.93 MB / 1.569 GB, free: 285.2 MB / 0.9514 GB Notification: Performance of preOpt resolveLoops (simulation): time 0.04851/4.069, allocations: 30.72 MB / 1.599 GB, free: 276 MB / 0.9514 GB Notification: Performance of preOpt evalFunc (simulation): time 0.006291/4.076, allocations: 1.301 MB / 1.6 GB, free: 275.7 MB / 0.9514 GB Notification: Performance of preOpt encapsulateWhenConditions (simulation): time 0.00036/4.076, allocations: 298.2 kB / 1.6 GB, free: 275.5 MB / 0.9514 GB Notification: Performance of pre-optimization done (n=3004): time 2.624e-05/4.076, allocations: 2.953 kB / 1.6 GB, free: 275.5 MB / 0.9514 GB Notification: Performance of matching and sorting (n=3005): time 1.238/5.314, allocations: 328.6 MB / 1.921 GB, free: 278.6 MB / 0.9514 GB Notification: Performance of inlineWhenForInitialization (initialization): time 0.0005631/5.314, allocations: 2.382 MB / 1.923 GB, free: 275.9 MB / 0.9514 GB Notification: Performance of selectInitializationVariablesDAE (initialization): time 0.05543/5.37, allocations: 24.48 MB / 1.947 GB, free: 268.5 MB / 0.9514 GB Notification: Performance of collectPreVariables (initialization): time 0.009097/5.379, allocations: 370.3 kB / 1.948 GB, free: 268.2 MB / 0.9514 GB Notification: Performance of collectInitialEqns (initialization): time 0.01285/5.392, allocations: 10.63 MB / 1.958 GB, free: 263.1 MB / 0.9514 GB Notification: Performance of collectInitialBindings (initialization): time 0.01777/5.41, allocations: 10.63 MB / 1.969 GB, free: 256.7 MB / 0.9514 GB Notification: Performance of simplifyInitialFunctions (initialization): time 0.03588/5.446, allocations: 6.986 MB / 1.975 GB, free: 254.4 MB / 0.9514 GB Notification: Performance of setup shared object (initialization): time 5.74e-05/5.446, allocations: 309.2 kB / 1.976 GB, free: 254.1 MB / 0.9514 GB Notification: Performance of preBalanceInitialSystem (initialization): time 0.04724/5.493, allocations: 33.37 MB / 2.008 GB, free: 241.1 MB / 0.9514 GB Notification: Performance of partitionIndependentBlocks (initialization): time 0.05585/5.549, allocations: 39.91 MB / 2.047 GB, free: 218.3 MB / 0.9514 GB Notification: Performance of analyzeInitialSystem (initialization): time 1.216/6.764, allocations: 248.7 MB / 2.29 GB, free: 258.9 MB / 0.9514 GB Notification: Performance of solveInitialSystemEqSystem (initialization): time 0.0002399/6.765, allocations: 49.48 kB / 2.29 GB, free: 258.9 MB / 0.9514 GB Notification: Performance of matching and sorting (n=4066) (initialization): time 0.1704/6.935, allocations: 82.3 MB / 2.371 GB, free: 228.2 MB / 0.9514 GB Notification: Performance of prepare postOptimizeDAE: time 0.0001234/6.935, allocations: 80.59 kB / 2.371 GB, free: 228.2 MB / 0.9514 GB Notification: Performance of postOpt simplifyComplexFunction (initialization): time 0.1255/7.061, allocations: 74.14 MB / 2.443 GB, free: 173.1 MB / 0.9514 GB Notification: Performance of postOpt tearingSystem (initialization): time 0.0144/7.075, allocations: 5.262 MB / 2.448 GB, free: 167.8 MB / 0.9514 GB Notification: Performance of postOpt solveSimpleEquations (initialization): time 0.04755/7.123, allocations: 8.536 MB / 2.456 GB, free: 159.3 MB / 0.9514 GB Notification: Performance of postOpt calculateStrongComponentJacobians (initialization): time 0.06417/7.187, allocations: 112.1 MB / 2.566 GB, free: 38.84 MB / 0.9514 GB Notification: Performance of postOpt simplifyAllExpressions (initialization): time 0.03142/7.218, allocations: 1.338 MB / 2.567 GB, free: 37.61 MB / 0.9514 GB Notification: Performance of postOpt collapseArrayExpressions (initialization): time 0.0111/7.229, allocations: 2.171 MB / 2.569 GB, free: 35.43 MB / 0.9514 GB Warning: Assuming fixed start value for the following 65 variables: tube.h[1]:VARIABLE(start = tube.mechanicalEquilibrium.h_start[1] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [3] tube.h[2]:VARIABLE(start = tube.mechanicalEquilibrium.h_start[2] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [3] tube.h[3]:VARIABLE(start = tube.mechanicalEquilibrium.h_start[3] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [3] tube.p[1]:VARIABLE(min = 0.0 start = tube.p_start_internal[1] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [3] tube.p[2]:VARIABLE(min = 0.0 start = tube.p_start_internal[2] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [3] tube.p[3]:VARIABLE(min = 0.0 start = tube.p_start_internal[3] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [3] plateHEX.flow_a.h[1]:VARIABLE(start = plateHEX.flow_a.mechanicalEquilibrium.h_start[1] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [5] plateHEX.flow_a.h[2]:VARIABLE(start = plateHEX.flow_a.mechanicalEquilibrium.h_start[2] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [5] plateHEX.flow_a.h[3]:VARIABLE(start = plateHEX.flow_a.mechanicalEquilibrium.h_start[3] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [5] plateHEX.flow_a.h[4]:VARIABLE(start = plateHEX.flow_a.mechanicalEquilibrium.h_start[4] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [5] plateHEX.flow_a.h[5]:VARIABLE(start = plateHEX.flow_a.mechanicalEquilibrium.h_start[5] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [5] plateHEX.flow_a.p[1]:VARIABLE(min = 0.0 start = plateHEX.flow_a.p_start_internal[1] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [5] plateHEX.flow_a.p[2]:VARIABLE(min = 0.0 start = plateHEX.flow_a.p_start_internal[2] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [5] plateHEX.flow_a.p[3]:VARIABLE(min = 0.0 start = plateHEX.flow_a.p_start_internal[3] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [5] plateHEX.flow_a.p[4]:VARIABLE(min = 0.0 start = plateHEX.flow_a.p_start_internal[4] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [5] plateHEX.flow_a.p[5]:VARIABLE(min = 0.0 start = plateHEX.flow_a.p_start_internal[5] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [5] plateHEX.flow_b.h[1]:VARIABLE(start = plateHEX.flow_b.mechanicalEquilibrium.h_start[1] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [5] plateHEX.flow_b.h[2]:VARIABLE(start = plateHEX.flow_b.mechanicalEquilibrium.h_start[2] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [5] plateHEX.flow_b.h[3]:VARIABLE(start = plateHEX.flow_b.mechanicalEquilibrium.h_start[3] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [5] plateHEX.flow_b.h[4]:VARIABLE(start = plateHEX.flow_b.mechanicalEquilibrium.h_start[4] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [5] plateHEX.flow_b.h[5]:VARIABLE(start = plateHEX.flow_b.mechanicalEquilibrium.h_start[5] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [5] plateHEX.flow_b.p[1]:VARIABLE(min = 0.0 start = plateHEX.flow_b.p_start_internal[1] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [5] plateHEX.flow_b.p[2]:VARIABLE(min = 0.0 start = plateHEX.flow_b.p_start_internal[2] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [5] plateHEX.flow_b.p[3]:VARIABLE(min = 0.0 start = plateHEX.flow_b.p_start_internal[3] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [5] plateHEX.flow_b.p[4]:VARIABLE(min = 0.0 start = plateHEX.flow_b.p_start_internal[4] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [5] plateHEX.flow_b.p[5]:VARIABLE(min = 0.0 start = plateHEX.flow_b.p_start_internal[5] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [5] condenser.flow_a.h[1]:VARIABLE(start = condenser.flow_a.mechanicalEquilibrium.h_start[1] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [9] condenser.flow_a.h[2]:VARIABLE(start = condenser.flow_a.mechanicalEquilibrium.h_start[2] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [9] condenser.flow_a.h[3]:VARIABLE(start = condenser.flow_a.mechanicalEquilibrium.h_start[3] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [9] condenser.flow_a.h[4]:VARIABLE(start = condenser.flow_a.mechanicalEquilibrium.h_start[4] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [9] condenser.flow_a.h[5]:VARIABLE(start = condenser.flow_a.mechanicalEquilibrium.h_start[5] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [9] condenser.flow_a.h[6]:VARIABLE(start = condenser.flow_a.mechanicalEquilibrium.h_start[6] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [9] condenser.flow_a.h[7]:VARIABLE(start = condenser.flow_a.mechanicalEquilibrium.h_start[7] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [9] condenser.flow_a.h[8]:VARIABLE(start = condenser.flow_a.mechanicalEquilibrium.h_start[8] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [9] condenser.flow_a.h[9]:VARIABLE(start = condenser.flow_a.mechanicalEquilibrium.h_start[9] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [9] condenser.flow_a.p[1]:VARIABLE(min = 0.0 start = condenser.flow_a.p_start_internal[1] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [9] condenser.flow_a.p[2]:VARIABLE(min = 0.0 start = condenser.flow_a.p_start_internal[2] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [9] condenser.flow_a.p[3]:VARIABLE(min = 0.0 start = condenser.flow_a.p_start_internal[3] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [9] condenser.flow_a.p[4]:VARIABLE(min = 0.0 start = condenser.flow_a.p_start_internal[4] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [9] condenser.flow_a.p[5]:VARIABLE(min = 0.0 start = condenser.flow_a.p_start_internal[5] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [9] condenser.flow_a.p[6]:VARIABLE(min = 0.0 start = condenser.flow_a.p_start_internal[6] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [9] condenser.flow_a.p[7]:VARIABLE(min = 0.0 start = condenser.flow_a.p_start_internal[7] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [9] condenser.flow_a.p[8]:VARIABLE(min = 0.0 start = condenser.flow_a.p_start_internal[8] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [9] condenser.flow_a.p[9]:VARIABLE(min = 0.0 start = condenser.flow_a.p_start_internal[9] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [9] condenser.flow_b.h[1]:VARIABLE(start = condenser.flow_b.h_start[1] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer ) \"Cell enthalpy\" type: Real [9] condenser.flow_b.h[2]:VARIABLE(start = condenser.flow_b.h_start[2] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer ) \"Cell enthalpy\" type: Real [9] condenser.flow_b.h[3]:VARIABLE(start = condenser.flow_b.h_start[3] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer ) \"Cell enthalpy\" type: Real [9] condenser.flow_b.h[4]:VARIABLE(start = condenser.flow_b.h_start[4] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer ) \"Cell enthalpy\" type: Real [9] condenser.flow_b.h[5]:VARIABLE(start = condenser.flow_b.h_start[5] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer ) \"Cell enthalpy\" type: Real [9] condenser.flow_b.h[6]:VARIABLE(start = condenser.flow_b.h_start[6] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer ) \"Cell enthalpy\" type: Real [9] condenser.flow_b.h[7]:VARIABLE(start = condenser.flow_b.h_start[7] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer ) \"Cell enthalpy\" type: Real [9] condenser.flow_b.h[8]:VARIABLE(start = condenser.flow_b.h_start[8] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer ) \"Cell enthalpy\" type: Real [9] condenser.flow_b.h[9]:VARIABLE(start = condenser.flow_b.h_start[9] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer ) \"Cell enthalpy\" type: Real [9] condenser.flow_b.p[1]:VARIABLE(min = 0.0 start = condenser.flow_b.p_start[1] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [9] condenser.flow_b.p[2]:VARIABLE(min = 0.0 start = condenser.flow_b.p_start[2] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [9] condenser.flow_b.p[3]:VARIABLE(min = 0.0 start = condenser.flow_b.p_start[3] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [9] condenser.flow_b.p[4]:VARIABLE(min = 0.0 start = condenser.flow_b.p_start[4] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [9] condenser.flow_b.p[5]:VARIABLE(min = 0.0 start = condenser.flow_b.p_start[5] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [9] condenser.flow_b.p[6]:VARIABLE(min = 0.0 start = condenser.flow_b.p_start[6] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [9] condenser.flow_b.p[7]:VARIABLE(min = 0.0 start = condenser.flow_b.p_start[7] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [9] condenser.flow_b.p[8]:VARIABLE(min = 0.0 start = condenser.flow_b.p_start[8] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [9] condenser.flow_b.p[9]:VARIABLE(min = 0.0 start = condenser.flow_b.p_start[9] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [9] steamSeparator.volume.h_liq:VARIABLE(start = steamSeparator.volume.h_liq_start unit = \"J/kg\" fixed = true nominal = 1000.0 ) \"Specific enthalpy of liquid phase\" type: Real steamSeparator.volume.h_vap:VARIABLE(start = steamSeparator.volume.h_vap_start unit = \"J/kg\" fixed = true nominal = 1000.0 ) \"Specific enthalpy of vapour phase\" type: Real steamSeparator.volume.p_vap:VARIABLE(min = 0.0 start = steamSeparator.volume.p_start unit = \"Pa\" fixed = true nominal = 1e5 stateSelect=StateSelect.prefer ) \"Vapour pressure\" type: Real Notification: Performance of preBalanceInitialSystem (initialization_lambda0): time 0.0722/7.301, allocations: 41.93 MB / 2.61 GB, free: 9.594 MB / 0.967 GB Notification: Performance of partitionIndependentBlocks (initialization_lambda0): time 0.5742/7.876, allocations: 39.24 MB / 2.649 GB, free: 271.5 MB / 0.9827 GB Notification: Performance of analyzeInitialSystem (initialization_lambda0): time 0.7116/8.587, allocations: 246 MB / 2.889 GB, free: 111.6 MB / 0.9827 GB Notification: Performance of solveInitialSystemEqSystem (initialization_lambda0): time 0.0002769/8.587, allocations: 52 kB / 2.889 GB, free: 111.5 MB / 0.9827 GB Notification: Performance of matching and sorting (n=4066) (initialization_lambda0): time 0.1548/8.742, allocations: 80.82 MB / 2.968 GB, free: 32.54 MB / 0.9827 GB Notification: Performance of prepare postOptimizeDAE: time 0.0001435/8.742, allocations: 81.25 kB / 2.968 GB, free: 32.46 MB / 0.9827 GB Notification: Performance of postOpt simplifyComplexFunction (initialization): time 0.6318/9.374, allocations: 72.65 MB / 3.039 GB, free: 275.5 MB / 0.9983 GB Notification: Performance of postOpt tearingSystem (initialization): time 0.01476/9.389, allocations: 5.2 MB / 3.044 GB, free: 273.9 MB / 0.9983 GB Notification: Performance of postOpt solveSimpleEquations (initialization): time 0.04815/9.437, allocations: 8.469 MB / 3.052 GB, free: 273.6 MB / 0.9983 GB Notification: Performance of postOpt calculateStrongComponentJacobians (initialization): time 0.06764/9.505, allocations: 111.5 MB / 3.161 GB, free: 174.6 MB / 0.9983 GB Notification: Performance of postOpt simplifyAllExpressions (initialization): time 0.03324/9.538, allocations: 1.291 MB / 3.162 GB, free: 174.1 MB / 0.9983 GB Notification: Performance of postOpt collapseArrayExpressions (initialization): time 0.01155/9.55, allocations: 2.134 MB / 3.164 GB, free: 173.8 MB / 0.9983 GB Warning: Assuming fixed start value for the following 65 variables: tube.h[1]:VARIABLE(start = tube.mechanicalEquilibrium.h_start[1] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [3] tube.h[2]:VARIABLE(start = tube.mechanicalEquilibrium.h_start[2] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [3] tube.h[3]:VARIABLE(start = tube.mechanicalEquilibrium.h_start[3] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [3] tube.p[1]:VARIABLE(min = 0.0 start = tube.p_start_internal[1] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [3] tube.p[2]:VARIABLE(min = 0.0 start = tube.p_start_internal[2] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [3] tube.p[3]:VARIABLE(min = 0.0 start = tube.p_start_internal[3] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [3] plateHEX.flow_a.h[1]:VARIABLE(start = plateHEX.flow_a.mechanicalEquilibrium.h_start[1] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [5] plateHEX.flow_a.h[2]:VARIABLE(start = plateHEX.flow_a.mechanicalEquilibrium.h_start[2] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [5] plateHEX.flow_a.h[3]:VARIABLE(start = plateHEX.flow_a.mechanicalEquilibrium.h_start[3] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [5] plateHEX.flow_a.h[4]:VARIABLE(start = plateHEX.flow_a.mechanicalEquilibrium.h_start[4] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [5] plateHEX.flow_a.h[5]:VARIABLE(start = plateHEX.flow_a.mechanicalEquilibrium.h_start[5] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [5] plateHEX.flow_a.p[1]:VARIABLE(min = 0.0 start = plateHEX.flow_a.p_start_internal[1] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [5] plateHEX.flow_a.p[2]:VARIABLE(min = 0.0 start = plateHEX.flow_a.p_start_internal[2] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [5] plateHEX.flow_a.p[3]:VARIABLE(min = 0.0 start = plateHEX.flow_a.p_start_internal[3] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [5] plateHEX.flow_a.p[4]:VARIABLE(min = 0.0 start = plateHEX.flow_a.p_start_internal[4] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [5] plateHEX.flow_a.p[5]:VARIABLE(min = 0.0 start = plateHEX.flow_a.p_start_internal[5] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [5] plateHEX.flow_b.h[1]:VARIABLE(start = plateHEX.flow_b.mechanicalEquilibrium.h_start[1] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [5] plateHEX.flow_b.h[2]:VARIABLE(start = plateHEX.flow_b.mechanicalEquilibrium.h_start[2] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [5] plateHEX.flow_b.h[3]:VARIABLE(start = plateHEX.flow_b.mechanicalEquilibrium.h_start[3] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [5] plateHEX.flow_b.h[4]:VARIABLE(start = plateHEX.flow_b.mechanicalEquilibrium.h_start[4] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [5] plateHEX.flow_b.h[5]:VARIABLE(start = plateHEX.flow_b.mechanicalEquilibrium.h_start[5] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [5] plateHEX.flow_b.p[1]:VARIABLE(min = 0.0 start = plateHEX.flow_b.p_start_internal[1] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [5] plateHEX.flow_b.p[2]:VARIABLE(min = 0.0 start = plateHEX.flow_b.p_start_internal[2] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [5] plateHEX.flow_b.p[3]:VARIABLE(min = 0.0 start = plateHEX.flow_b.p_start_internal[3] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [5] plateHEX.flow_b.p[4]:VARIABLE(min = 0.0 start = plateHEX.flow_b.p_start_internal[4] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [5] plateHEX.flow_b.p[5]:VARIABLE(min = 0.0 start = plateHEX.flow_b.p_start_internal[5] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [5] condenser.flow_a.h[1]:VARIABLE(start = condenser.flow_a.mechanicalEquilibrium.h_start[1] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [9] condenser.flow_a.h[2]:VARIABLE(start = condenser.flow_a.mechanicalEquilibrium.h_start[2] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [9] condenser.flow_a.h[3]:VARIABLE(start = condenser.flow_a.mechanicalEquilibrium.h_start[3] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [9] condenser.flow_a.h[4]:VARIABLE(start = condenser.flow_a.mechanicalEquilibrium.h_start[4] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [9] condenser.flow_a.h[5]:VARIABLE(start = condenser.flow_a.mechanicalEquilibrium.h_start[5] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [9] condenser.flow_a.h[6]:VARIABLE(start = condenser.flow_a.mechanicalEquilibrium.h_start[6] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [9] condenser.flow_a.h[7]:VARIABLE(start = condenser.flow_a.mechanicalEquilibrium.h_start[7] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [9] condenser.flow_a.h[8]:VARIABLE(start = condenser.flow_a.mechanicalEquilibrium.h_start[8] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [9] condenser.flow_a.h[9]:VARIABLE(start = condenser.flow_a.mechanicalEquilibrium.h_start[9] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true ) \"Cell enthalpy\" type: Real [9] condenser.flow_a.p[1]:VARIABLE(min = 0.0 start = condenser.flow_a.p_start_internal[1] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [9] condenser.flow_a.p[2]:VARIABLE(min = 0.0 start = condenser.flow_a.p_start_internal[2] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [9] condenser.flow_a.p[3]:VARIABLE(min = 0.0 start = condenser.flow_a.p_start_internal[3] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [9] condenser.flow_a.p[4]:VARIABLE(min = 0.0 start = condenser.flow_a.p_start_internal[4] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [9] condenser.flow_a.p[5]:VARIABLE(min = 0.0 start = condenser.flow_a.p_start_internal[5] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [9] condenser.flow_a.p[6]:VARIABLE(min = 0.0 start = condenser.flow_a.p_start_internal[6] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [9] condenser.flow_a.p[7]:VARIABLE(min = 0.0 start = condenser.flow_a.p_start_internal[7] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [9] condenser.flow_a.p[8]:VARIABLE(min = 0.0 start = condenser.flow_a.p_start_internal[8] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [9] condenser.flow_a.p[9]:VARIABLE(min = 0.0 start = condenser.flow_a.p_start_internal[9] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [9] condenser.flow_b.h[1]:VARIABLE(start = condenser.flow_b.h_start[1] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer ) \"Cell enthalpy\" type: Real [9] condenser.flow_b.h[2]:VARIABLE(start = condenser.flow_b.h_start[2] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer ) \"Cell enthalpy\" type: Real [9] condenser.flow_b.h[3]:VARIABLE(start = condenser.flow_b.h_start[3] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer ) \"Cell enthalpy\" type: Real [9] condenser.flow_b.h[4]:VARIABLE(start = condenser.flow_b.h_start[4] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer ) \"Cell enthalpy\" type: Real [9] condenser.flow_b.h[5]:VARIABLE(start = condenser.flow_b.h_start[5] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer ) \"Cell enthalpy\" type: Real [9] condenser.flow_b.h[6]:VARIABLE(start = condenser.flow_b.h_start[6] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer ) \"Cell enthalpy\" type: Real [9] condenser.flow_b.h[7]:VARIABLE(start = condenser.flow_b.h_start[7] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer ) \"Cell enthalpy\" type: Real [9] condenser.flow_b.h[8]:VARIABLE(start = condenser.flow_b.h_start[8] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer ) \"Cell enthalpy\" type: Real [9] condenser.flow_b.h[9]:VARIABLE(start = condenser.flow_b.h_start[9] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer ) \"Cell enthalpy\" type: Real [9] condenser.flow_b.p[1]:VARIABLE(min = 0.0 start = condenser.flow_b.p_start[1] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [9] condenser.flow_b.p[2]:VARIABLE(min = 0.0 start = condenser.flow_b.p_start[2] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [9] condenser.flow_b.p[3]:VARIABLE(min = 0.0 start = condenser.flow_b.p_start[3] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [9] condenser.flow_b.p[4]:VARIABLE(min = 0.0 start = condenser.flow_b.p_start[4] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [9] condenser.flow_b.p[5]:VARIABLE(min = 0.0 start = condenser.flow_b.p_start[5] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [9] condenser.flow_b.p[6]:VARIABLE(min = 0.0 start = condenser.flow_b.p_start[6] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [9] condenser.flow_b.p[7]:VARIABLE(min = 0.0 start = condenser.flow_b.p_start[7] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [9] condenser.flow_b.p[8]:VARIABLE(min = 0.0 start = condenser.flow_b.p_start[8] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [9] condenser.flow_b.p[9]:VARIABLE(min = 0.0 start = condenser.flow_b.p_start[9] unit = \"Pa\" fixed = true nominal = 1e5 protected = true ) \"Cell pressure\" type: Real [9] steamSeparator.volume.h_liq:VARIABLE(start = steamSeparator.volume.h_liq_start unit = \"J/kg\" fixed = true nominal = 1000.0 ) \"Specific enthalpy of liquid phase\" type: Real steamSeparator.volume.h_vap:VARIABLE(start = steamSeparator.volume.h_vap_start unit = \"J/kg\" fixed = true nominal = 1000.0 ) \"Specific enthalpy of vapour phase\" type: Real steamSeparator.volume.p_vap:VARIABLE(min = 0.0 start = steamSeparator.volume.p_start unit = \"Pa\" fixed = true nominal = 1e5 stateSelect=StateSelect.prefer ) \"Vapour pressure\" type: Real Notification: Model statistics after passing the back-end for initialization: * Number of independent subsystems: 785 * Number of states: 0 () * Number of discrete variables: 0 () * Number of discrete states: 0 () * Number of clocked states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for initialization (3979): * Single equations (assignments): 3913 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 0 * When equations: 0 * If-equations: 0 * Equation systems (not torn): 1 * Torn equation systems: 65 * Mixed (continuous/discrete) equation systems: 0 Notification: Equation system details (not torn): * Constant Jacobian (size): 0 systems * Linear Jacobian (size,density): 0 systems * Non-linear Jacobian (size): 1 system {1} * Without analytic Jacobian (size): 0 systems Notification: Torn system details for strict tearing set: * Linear torn systems (#iteration vars, #inner vars, density): 64 systems {(1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,6,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,6,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,6,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (4,3,87.5%), (1,1,100.0%), (1,2,100.0%), (1,1,100.0%), (1,1,100.0%)} * Non-linear torn systems (#iteration vars, #inner vars): 1 system {(1,2)} Notification: Performance of prepare postOptimizeDAE: time 0.01913/9.569, allocations: 2.33 MB / 3.167 GB, free: 172.8 MB / 0.9983 GB Notification: Performance of postOpt lateInlineFunction (simulation): time 0.01665/9.585, allocations: 2.623 MB / 3.169 GB, free: 172.8 MB / 0.9983 GB Warning: After manipulating the system with postOptModule wrapFunctionCalls the system is unbalanced. This indicates that the original system is singular. You can use -d=dumpCSE and -d=dumpCSE_verbose for more information. Error: Too many equations, over-determined system. The model has 3887 equation(s) and 3767 variable(s). [/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia main/VLEFluid/MixtureCompatible/VLEFluid_ph.mo:55:3-60:21:writable] Error: (tube.steamQuality[1], tube.fluid[1].cp, tube.fluid[1].cv, tube.fluid[1].beta, tube.fluid[1].kappa, tube.fluid[1].drhodp_hxi, tube.fluid[1].drhodh_pxi, _, tube.fluid[1].w, tube.fluid[1].gamma) = ($cse342, $cse343, $cse344, $cse345, $cse346, $cse347, $cse348, $cse349, $cse350, $cse351) has size 9 but 3 variables (pumpVLE_L1_simple.outlet.h_outflow, quadruple1.m_flow, steamSeparator.volume.outlet[2].h_outflow) Error: Internal error Transformation Module PFPlusExt index Reduction Method Pantelides failed! Notification: Performance of postOpt wrapFunctionCalls (simulation): time 0.11/9.695, allocations: 53.72 MB / 3.222 GB, free: 148.2 MB / 0.9983 GB Error: post-optimization module wrapFunctionCalls (simulation) failed. " [Timeout remaining time 790] [Calling sys.exit(0), Time elapsed: 13.322391380032059] Failed to read output from testmodel.py, exit status != 0: 9.705577825021464 9.714588526 7.709533763 Calling exit ...