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 0.01745/0.01745, allocations: 1.765 MB / 18.12 MB, free: 4.945 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 0.001761/0.001761, allocations: 103.7 kB / 21.36 MB, free: 1.715 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 0.001612/0.001612, allocations: 215.4 kB / 24.75 MB, free: 3.742 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 1.385/1.385, allocations: 230.6 MB / 258.5 MB, free: 13.09 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 1.024/1.024, allocations: 130.5 MB / 445.6 MB, free: 14.57 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 0.3736/0.3736, allocations: 46.14 MB / 0.6549 GB, free: 31.15 MB / 0.4982 GB Notification: Performance of FrontEnd - Absyn->SCode: time 0.1695/0.5431, allocations: 89.04 MB / 0.7419 GB, free: 2.312 MB / 0.545 GB Notification: Performance of NFInst.instantiate(ClaRa.Examples.VapourCycle_01): time 0.04588/0.589, allocations: 43.59 MB / 0.7844 GB, free: 6.559 MB / 0.5919 GB Notification: Performance of NFInst.instExpressions: time 0.07465/0.6636, allocations: 45.89 MB / 0.8293 GB, free: 8.539 MB / 0.6388 GB Notification: Performance of NFInst.updateImplicitVariability: time 0.01008/0.6737, allocations: 250.2 kB / 0.8295 GB, free: 8.293 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 0.01442/0.6881, allocations: 5.52 MB / 0.8349 GB, free: 2.746 MB / 0.6388 GB Notification: Performance of NFTyping.typeBindings: time 0.02522/0.7133, allocations: 9.427 MB / 0.8441 GB, free: 9.273 MB / 0.6544 GB Notification: Performance of NFTyping.typeClassSections: time 0.02437/0.7377, allocations: 9.786 MB / 0.8536 GB, free: 15.47 MB / 0.67 GB Notification: Performance of NFFlatten.flatten: time 0.4201/1.158, allocations: 41.85 MB / 0.8945 GB, free: 18.98 MB / 0.67 GB Notification: Performance of NFFlatten.resolveConnections: time 0.02335/1.181, allocations: 14.78 MB / 0.909 GB, free: 18.36 MB / 0.67 GB Notification: Performance of NFEvalConstants.evaluate: time 0.03169/1.213, allocations: 16.32 MB / 0.9249 GB, free: 16.7 MB / 0.67 GB Notification: Performance of NFSimplifyModel.simplify: time 0.03349/1.246, allocations: 22.25 MB / 0.9466 GB, free: 7.465 MB / 0.67 GB Notification: Performance of NFPackage.collectConstants: time 0.01433/1.261, allocations: 4.542 MB / 0.9511 GB, free: 7.465 MB / 0.67 GB Notification: Performance of NFFlatten.collectFunctions: time 0.02744/1.288, allocations: 11.14 MB / 0.9619 GB, free: 3.5 MB / 0.67 GB Notification: Performance of NFScalarize.scalarize: time 0.02741/1.316, allocations: 16.88 MB / 0.9784 GB, free: 2.922 MB / 0.6857 GB Notification: Performance of NFVerifyModel.verify: time 0.04412/1.36, allocations: 20.25 MB / 0.9982 GB, free: 14.8 MB / 0.7169 GB Notification: Performance of NFConvertDAE.convert: time 0.09458/1.454, allocations: 66.53 MB / 1.063 GB, free: 14.35 MB / 0.7794 GB Notification: Performance of FrontEnd - DAE generated: time 6.873e-06/1.454, allocations: 0 / 1.063 GB, free: 14.35 MB / 0.7794 GB Notification: Performance of FrontEnd: time 2.124e-06/1.454, allocations: 0 / 1.063 GB, free: 14.35 MB / 0.7794 GB Notification: Performance of Transformations before backend: time 0.001524/1.456, allocations: 1.688 kB / 1.063 GB, free: 14.35 MB / 0.7794 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 0.1332/1.589, allocations: 42.79 MB / 1.105 GB, free: 4.125 MB / 0.8107 GB Notification: Performance of prepare preOptimizeDAE: time 4.898e-05/1.589, allocations: 12.03 kB / 1.105 GB, free: 4.113 MB / 0.8107 GB Notification: Performance of preOpt normalInlineFunction (simulation): time 0.02092/1.61, allocations: 3.557 MB / 1.108 GB, free: 0.5391 MB / 0.8107 GB Notification: Performance of preOpt evaluateParameters (simulation): time 0.08597/1.696, allocations: 37.43 MB / 1.145 GB, free: 12.07 MB / 0.8575 GB Notification: Performance of preOpt simplifyIfEquations (simulation): time 0.001517/1.697, allocations: 1.059 MB / 1.146 GB, free: 11.05 MB / 0.8575 GB Notification: Performance of preOpt expandDerOperator (simulation): time 0.009887/1.707, allocations: 1.44 MB / 1.147 GB, free: 9.648 MB / 0.8575 GB Notification: Performance of preOpt clockPartitioning (simulation): time 0.8826/2.59, allocations: 64.18 MB / 1.21 GB, free: 252.8 MB / 0.9045 GB Notification: Performance of preOpt findStateOrder (simulation): time 0.000747/2.591, allocations: 107.3 kB / 1.21 GB, free: 252.8 MB / 0.9045 GB Notification: Performance of preOpt replaceEdgeChange (simulation): time 0.008801/2.599, allocations: 0.6855 MB / 1.211 GB, free: 252.8 MB / 0.9045 GB Notification: Performance of preOpt inlineArrayEqn (simulation): time 0.003351/2.603, allocations: 2.742 MB / 1.214 GB, free: 252.7 MB / 0.9045 GB Notification: Performance of preOpt removeEqualRHS (simulation): time 0.1603/2.763, allocations: 95.19 MB / 1.307 GB, free: 215.5 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 0.3077/3.071, allocations: 215.8 MB / 1.517 GB, free: 320 kB / 0.9045 GB Notification: Performance of preOpt comSubExp (simulation): time 0.5461/3.617, allocations: 51.92 MB / 1.568 GB, free: 285.8 MB / 0.9514 GB Notification: Performance of preOpt resolveLoops (simulation): time 0.04483/3.662, allocations: 30.72 MB / 1.598 GB, free: 275.9 MB / 0.9514 GB Notification: Performance of preOpt evalFunc (simulation): time 0.006011/3.668, allocations: 1.303 MB / 1.599 GB, free: 275.7 MB / 0.9514 GB Notification: Performance of preOpt encapsulateWhenConditions (simulation): time 0.0002939/3.668, allocations: 298.5 kB / 1.6 GB, free: 275.5 MB / 0.9514 GB Notification: Performance of pre-optimization done (n=3004): time 2.702e-05/3.668, allocations: 2.656 kB / 1.6 GB, free: 275.5 MB / 0.9514 GB Notification: Performance of matching and sorting (n=3005): time 1.091/4.759, allocations: 328.6 MB / 1.92 GB, free: 278.4 MB / 0.9514 GB Notification: Performance of inlineWhenForInitialization (initialization): time 0.0005399/4.759, allocations: 2.381 MB / 1.923 GB, free: 275.7 MB / 0.9514 GB Notification: Performance of selectInitializationVariablesDAE (initialization): time 0.05241/4.812, allocations: 24.49 MB / 1.947 GB, free: 268.3 MB / 0.9514 GB Notification: Performance of collectPreVariables (initialization): time 0.007768/4.82, allocations: 369.1 kB / 1.947 GB, free: 268 MB / 0.9514 GB Notification: Performance of collectInitialEqns (initialization): time 0.01233/4.832, allocations: 10.62 MB / 1.957 GB, free: 262.9 MB / 0.9514 GB Notification: Performance of collectInitialBindings (initialization): time 0.02019/4.852, allocations: 10.63 MB / 1.968 GB, free: 256.5 MB / 0.9514 GB Notification: Performance of simplifyInitialFunctions (initialization): time 0.03509/4.887, allocations: 6.98 MB / 1.975 GB, free: 254.2 MB / 0.9514 GB Notification: Performance of setup shared object (initialization): time 5.108e-05/4.887, allocations: 308.8 kB / 1.975 GB, free: 253.9 MB / 0.9514 GB Notification: Performance of preBalanceInitialSystem (initialization): time 0.04933/4.936, allocations: 33.37 MB / 2.008 GB, free: 240.9 MB / 0.9514 GB Notification: Performance of partitionIndependentBlocks (initialization): time 0.05634/4.993, allocations: 39.91 MB / 2.046 GB, free: 218.1 MB / 0.9514 GB Notification: Performance of analyzeInitialSystem (initialization): time 1.153/6.145, allocations: 248.7 MB / 2.289 GB, free: 258.9 MB / 0.9514 GB Notification: Performance of solveInitialSystemEqSystem (initialization): time 0.0002003/6.146, allocations: 53.62 kB / 2.289 GB, free: 258.9 MB / 0.9514 GB Notification: Performance of matching and sorting (n=4066) (initialization): time 0.1611/6.307, allocations: 82.3 MB / 2.37 GB, free: 228.2 MB / 0.9514 GB Notification: Performance of prepare postOptimizeDAE: time 0.0002923/6.307, allocations: 80.03 kB / 2.37 GB, free: 228.2 MB / 0.9514 GB Notification: Performance of postOpt simplifyComplexFunction (initialization): time 0.1325/6.439, allocations: 74.16 MB / 2.442 GB, free: 173 MB / 0.9514 GB Notification: Performance of postOpt tearingSystem (initialization): time 0.01532/6.455, allocations: 5.261 MB / 2.447 GB, free: 167.7 MB / 0.9514 GB Notification: Performance of postOpt solveSimpleEquations (initialization): time 0.04686/6.502, allocations: 8.532 MB / 2.456 GB, free: 159.2 MB / 0.9514 GB Notification: Performance of postOpt calculateStrongComponentJacobians (initialization): time 0.06785/6.57, allocations: 112.1 MB / 2.565 GB, free: 38.76 MB / 0.9514 GB Notification: Performance of postOpt simplifyAllExpressions (initialization): time 0.03054/6.6, allocations: 1.339 MB / 2.567 GB, free: 37.52 MB / 0.9514 GB Notification: Performance of postOpt collapseArrayExpressions (initialization): time 0.01072/6.611, allocations: 2.167 MB / 2.569 GB, free: 35.35 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 0.0698/6.681, allocations: 41.93 MB / 2.61 GB, free: 9.516 MB / 0.967 GB Notification: Performance of partitionIndependentBlocks (initialization_lambda0): time 0.5129/7.193, allocations: 39.24 MB / 2.648 GB, free: 271.7 MB / 0.9827 GB Notification: Performance of analyzeInitialSystem (initialization_lambda0): time 0.7339/7.927, allocations: 246 MB / 2.888 GB, free: 111.4 MB / 0.9827 GB Notification: Performance of solveInitialSystemEqSystem (initialization_lambda0): time 0.0004381/7.928, allocations: 48 kB / 2.888 GB, free: 111.4 MB / 0.9827 GB Notification: Performance of matching and sorting (n=4066) (initialization_lambda0): time 0.1519/8.08, allocations: 80.82 MB / 2.967 GB, free: 32.34 MB / 0.9827 GB Notification: Performance of prepare postOptimizeDAE: time 0.0003344/8.08, allocations: 80 kB / 2.967 GB, free: 32.27 MB / 0.9827 GB Notification: Performance of postOpt simplifyComplexFunction (initialization): time 0.6034/8.683, allocations: 72.64 MB / 3.038 GB, free: 275.7 MB / 0.9983 GB Notification: Performance of postOpt tearingSystem (initialization): time 0.0146/8.698, allocations: 5.209 MB / 3.043 GB, free: 274 MB / 0.9983 GB Notification: Performance of postOpt solveSimpleEquations (initialization): time 0.04586/8.744, allocations: 8.463 MB / 3.051 GB, free: 273.8 MB / 0.9983 GB Notification: Performance of postOpt calculateStrongComponentJacobians (initialization): time 0.06594/8.81, allocations: 111.5 MB / 3.16 GB, free: 174.7 MB / 0.9983 GB Notification: Performance of postOpt simplifyAllExpressions (initialization): time 0.02915/8.839, allocations: 1.3 MB / 3.162 GB, free: 174.2 MB / 0.9983 GB Notification: Performance of postOpt collapseArrayExpressions (initialization): time 0.01071/8.85, allocations: 2.128 MB / 3.164 GB, free: 173.9 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 0.01777/8.867, allocations: 2.327 MB / 3.166 GB, free: 172.9 MB / 0.9983 GB Notification: Performance of postOpt lateInlineFunction (simulation): time 0.0155/8.883, allocations: 2.622 MB / 3.169 GB, free: 172.9 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 0.09884/8.982, allocations: 53.73 MB / 3.221 GB, free: 148.3 MB / 0.9983 GB Error: post-optimization module wrapFunctionCalls (simulation) failed. " [Timeout remaining time 791] [Calling sys.exit(0), Time elapsed: 12.388020962011069] Failed to read output from testmodel.py, exit status != 0: 8.991047415009234 9.00039767 7.542207209 Calling exit ...