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 0.00598/0.00598, allocations: 1.446 MB / 20.54 MB, free: 4.008 MB / 18.57 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 0.0006589/0.0006589, allocations: 91.45 kB / 24.16 MB, free: 396 kB / 18.57 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 0.0008207/0.0008207, allocations: 163.6 kB / 27.85 MB, free: 5.5 MB / 18.57 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 0.8621/0.8621, allocations: 177.2 MB / 208.6 MB, free: 2.949 MB / 186.7 MB
"
[Timeout remaining time 179]
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 0.6901/0.6901, allocations: 102.4 MB / 367.9 MB, free: 1.457 MB / 330.8 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 0.5.2 (/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: Performance of FrontEnd - loaded program: time 1.313e-06/1.313e-06, allocations: 0 / 0.5366 GB, free: 39.8 MB / 490.8 MB
Notification: Performance of FrontEnd - Absyn->SCode: time 1.399e-05/1.53e-05, allocations: 5.641 kB / 0.5366 GB, free: 39.8 MB / 490.8 MB
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.
Notification: Automatically loaded package TILMedia 1.9.0 ClaRa due to usage.
Notification: Performance of NFInst.instantiate(ClaRa.Examples.VapourCycle_01): time 0.1214/0.1214, allocations: 84.3 MB / 0.6189 GB, free: 7.629 MB / 0.5105 GB
Notification: Performance of NFInst.instExpressions: time 0.04772/0.1691, allocations: 43.59 MB / 0.6615 GB, free: 11.91 MB / 0.5574 GB
Notification: Performance of NFInst.updateImplicitVariability: time 0.007894/0.177, allocations: 250.2 kB / 0.6618 GB, free: 11.66 MB / 0.5574 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 0.008522/0.1856, allocations: 5.42 MB / 0.6671 GB, free: 6.215 MB / 0.5574 GB
Notification: Performance of NFTyping.typeBindings: time 0.01794/0.2035, allocations: 9.924 MB / 0.6767 GB, free: 12.23 MB / 0.573 GB
Notification: Performance of NFTyping.typeClassSections: time 0.01677/0.2203, allocations: 10.32 MB / 0.6868 GB, free: 1.891 MB / 0.573 GB
Notification: Performance of NFFlatten.flatten: time 0.03558/0.2558, allocations: 42.8 MB / 0.7286 GB, free: 6.984 MB / 0.6199 GB
Notification: Performance of NFFlatten.resolveConnections: time 0.01854/0.2744, allocations: 13.97 MB / 0.7422 GB, free: 8.902 MB / 0.6355 GB
Notification: Performance of NFEvalConstants.evaluate: time 0.03595/0.3103, allocations: 22.36 MB / 0.7641 GB, free: 2.496 MB / 0.6512 GB
Notification: Performance of NFSimplifyModel.simplify: time 0.2819/0.5922, allocations: 20.81 MB / 0.7844 GB, free: 51.61 MB / 0.6512 GB
Notification: Performance of NFPackage.collectConstants: time 0.01358/0.6058, allocations: 4.541 MB / 0.7888 GB, free: 51.61 MB / 0.6512 GB
Notification: Performance of NFFlatten.collectFunctions: time 0.02322/0.629, allocations: 9.338 MB / 0.798 GB, free: 51.61 MB / 0.6512 GB
Notification: Performance of NFScalarize.scalarize: time 0.01842/0.6475, allocations: 17.43 MB / 0.815 GB, free: 51.61 MB / 0.6512 GB
Notification: Performance of NFVerifyModel.verify: time 0.02716/0.6746, allocations: 14.33 MB / 0.829 GB, free: 51.61 MB / 0.6512 GB
Notification: Performance of NFConvertDAE.convert: time 0.06025/0.7349, allocations: 68.68 MB / 0.896 GB, free: 12.92 MB / 0.6512 GB
Notification: Performance of FrontEnd - DAE generated: time 5.35e-06/0.7349, allocations: 0 / 0.896 GB, free: 12.92 MB / 0.6512 GB
Notification: Performance of FrontEnd: time 1.683e-06/0.7349, allocations: 0 / 0.896 GB, free: 12.92 MB / 0.6512 GB
Notification: Performance of Transformations before backend: time 0.001639/0.7365, allocations: 0 / 0.896 GB, free: 12.92 MB / 0.6512 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 0.09947/0.836, allocations: 42.45 MB / 0.9375 GB, free: 6.672 MB / 0.6824 GB
Notification: Performance of prepare preOptimizeDAE: time 4.312e-05/0.836, allocations: 8.031 kB / 0.9375 GB, free: 6.664 MB / 0.6824 GB
Notification: Performance of preOpt normalInlineFunction (simulation): time 0.01565/0.8517, allocations: 3.563 MB / 0.941 GB, free: 3.082 MB / 0.6824 GB
Notification: Performance of preOpt evaluateParameters (simulation): time 0.0634/0.9151, allocations: 37.73 MB / 0.9778 GB, free: 14.29 MB / 0.7293 GB
Notification: Performance of preOpt simplifyIfEquations (simulation): time 0.0009199/0.916, allocations: 1.092 MB / 0.9789 GB, free: 13.23 MB / 0.7293 GB
Notification: Performance of preOpt expandDerOperator (simulation): time 0.009067/0.9251, allocations: 1.435 MB / 0.9803 GB, free: 11.83 MB / 0.7293 GB
Notification: Performance of preOpt clockPartitioning (simulation): time 0.108/1.033, allocations: 75.4 MB / 1.054 GB, free: 10.7 MB / 0.8074 GB
Notification: Performance of preOpt findStateOrder (simulation): time 0.0005977/1.034, allocations: 108.5 kB / 1.054 GB, free: 10.66 MB / 0.8074 GB
Notification: Performance of preOpt replaceEdgeChange (simulation): time 0.008578/1.042, allocations: 0.6842 MB / 1.055 GB, free: 10.02 MB / 0.8074 GB
Notification: Performance of preOpt inlineArrayEqn (simulation): time 0.002335/1.045, allocations: 2.735 MB / 1.057 GB, free: 7.281 MB / 0.8074 GB
Notification: Performance of preOpt removeEqualRHS (simulation): time 0.3968/1.441, allocations: 94.5 MB / 1.15 GB, free: 223.6 MB / 0.8074 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 0.2322/1.674, allocations: 196.2 MB / 1.341 GB, free: 29.28 MB / 0.8074 GB
Notification: Performance of preOpt comSubExp (simulation): time 0.3522/2.026, allocations: 51.83 MB / 1.392 GB, free: 233.3 MB / 0.8074 GB
Notification: Performance of preOpt resolveLoops (simulation): time 0.03808/2.064, allocations: 30.72 MB / 1.422 GB, free: 220.1 MB / 0.8074 GB
Notification: Performance of preOpt evalFunc (simulation): time 0.004243/2.068, allocations: 1.058 MB / 1.423 GB, free: 219.9 MB / 0.8074 GB
Notification: Performance of preOpt encapsulateWhenConditions (simulation): time 0.0002275/2.068, allocations: 308 kB / 1.423 GB, free: 219.7 MB / 0.8074 GB
Notification: Performance of pre-optimization done (n=3004): time 2.268e-05/2.068, allocations: 0 / 1.423 GB, free: 219.7 MB / 0.8074 GB
Notification: Performance of matching and sorting (n=3005): time 0.7871/2.855, allocations: 323.5 MB / 1.739 GB, free: 190 MB / 0.8074 GB
Notification: Performance of inlineWhenForInitialization (initialization): time 0.0005025/2.856, allocations: 2.378 MB / 1.741 GB, free: 187.3 MB / 0.8074 GB
Notification: Performance of selectInitializationVariablesDAE (initialization): time 0.04136/2.897, allocations: 23.83 MB / 1.765 GB, free: 178.9 MB / 0.8074 GB
Notification: Performance of collectPreVariables (initialization): time 0.007306/2.905, allocations: 365.4 kB / 1.765 GB, free: 178.6 MB / 0.8074 GB
Notification: Performance of collectInitialEqns (initialization): time 0.009289/2.914, allocations: 10.67 MB / 1.776 GB, free: 170.3 MB / 0.8074 GB
Notification: Performance of collectInitialBindings (initialization): time 0.01601/2.93, allocations: 10.49 MB / 1.786 GB, free: 162 MB / 0.8074 GB
Notification: Performance of simplifyInitialFunctions (initialization): time 0.02471/2.955, allocations: 6.842 MB / 1.792 GB, free: 159.7 MB / 0.8074 GB
Notification: Performance of setup shared object (initialization): time 3.203e-05/2.955, allocations: 305.1 kB / 1.793 GB, free: 159.4 MB / 0.8074 GB
Notification: Performance of preBalanceInitialSystem (initialization): time 0.03618/2.991, allocations: 33.24 MB / 1.825 GB, free: 145.8 MB / 0.8074 GB
Notification: Performance of partitionIndependentBlocks (initialization): time 0.04164/3.033, allocations: 40.79 MB / 1.865 GB, free: 103.1 MB / 0.8074 GB
Notification: Performance of analyzeInitialSystem (initialization): time 0.7511/3.784, allocations: 250.5 MB / 2.11 GB, free: 146 MB / 0.8074 GB
Notification: Performance of solveInitialSystemEqSystem (initialization): time 0.0001383/3.784, allocations: 52 kB / 2.11 GB, free: 145.9 MB / 0.8074 GB
Notification: Performance of matching and sorting (n=4020) (initialization): time 0.1168/3.901, allocations: 81.91 MB / 2.19 GB, free: 65.18 MB / 0.8074 GB
Notification: Performance of prepare postOptimizeDAE: time 0.000101/3.901, allocations: 80.78 kB / 2.19 GB, free: 65.1 MB / 0.8074 GB
Notification: Performance of postOpt simplifyComplexFunction (initialization): time 0.1016/4.002, allocations: 73.8 MB / 2.262 GB, free: 7.094 MB / 0.823 GB
Notification: Performance of postOpt tearingSystem (initialization): time 0.01026/4.013, allocations: 5.305 MB / 2.267 GB, free: 1.59 MB / 0.823 GB
Notification: Performance of postOpt solveSimpleEquations (initialization): time 0.3664/4.379, allocations: 8.463 MB / 2.275 GB, free: 245.6 MB / 0.8387 GB
Notification: Performance of postOpt calculateStrongComponentJacobians (initialization): time 0.0462/4.425, allocations: 103.5 MB / 2.376 GB, free: 162.9 MB / 0.8387 GB
Notification: Performance of postOpt simplifyAllExpressions (initialization): time 0.02214/4.447, allocations: 1.329 MB / 2.378 GB, free: 162.4 MB / 0.8387 GB
Notification: Performance of postOpt collapseArrayExpressions (initialization): time 0.008613/4.456, allocations: 2.161 MB / 2.38 GB, free: 162.2 MB / 0.8387 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 0.0562/4.512, allocations: 41.8 MB / 2.421 GB, free: 145.8 MB / 0.8387 GB
Notification: Performance of partitionIndependentBlocks (initialization_lambda0): time 0.04164/4.554, allocations: 40.11 MB / 2.46 GB, free: 123.3 MB / 0.8387 GB
Notification: Performance of analyzeInitialSystem (initialization_lambda0): time 0.7482/5.302, allocations: 247.7 MB / 2.702 GB, free: 182 MB / 0.8387 GB
Notification: Performance of solveInitialSystemEqSystem (initialization_lambda0): time 0.0001486/5.302, allocations: 47.56 kB / 2.702 GB, free: 182 MB / 0.8387 GB
Notification: Performance of matching and sorting (n=4020) (initialization_lambda0): time 0.1156/5.418, allocations: 80.42 MB / 2.78 GB, free: 103.2 MB / 0.8387 GB
Notification: Performance of prepare postOptimizeDAE: time 9.465e-05/5.418, allocations: 80 kB / 2.78 GB, free: 103.1 MB / 0.8387 GB
Notification: Performance of postOpt simplifyComplexFunction (initialization): time 0.09628/5.514, allocations: 72.31 MB / 2.851 GB, free: 30.64 MB / 0.8387 GB
Notification: Performance of postOpt tearingSystem (initialization): time 0.008444/5.522, allocations: 5.25 MB / 2.856 GB, free: 25.2 MB / 0.8387 GB
Notification: Performance of postOpt solveSimpleEquations (initialization): time 0.02826/5.551, allocations: 8.397 MB / 2.864 GB, free: 16.79 MB / 0.8387 GB
Notification: Performance of postOpt calculateStrongComponentJacobians (initialization): time 0.381/5.932, allocations: 102.9 MB / 2.965 GB, free: 191.2 MB / 0.8699 GB
Notification: Performance of postOpt simplifyAllExpressions (initialization): time 0.02412/5.956, allocations: 1.294 MB / 2.966 GB, free: 191.2 MB / 0.8699 GB
Notification: Performance of postOpt collapseArrayExpressions (initialization): time 0.009468/5.965, allocations: 2.119 MB / 2.968 GB, free: 191.2 MB / 0.8699 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 (3933):
 * Single equations (assignments): 3867
 * 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 0.01653/5.982, allocations: 2.318 MB / 2.97 GB, free: 190.9 MB / 0.8699 GB
Notification: Performance of postOpt lateInlineFunction (simulation): time 0.01407/5.996, allocations: 2.561 MB / 2.973 GB, free: 190.9 MB / 0.8699 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 <failed> postOpt wrapFunctionCalls (simulation): time 0.08047/6.076, allocations: 53.76 MB / 3.025 GB, free: 172 MB / 0.8699 GB
Error: post-optimization module wrapFunctionCalls (simulation) failed.
"
[Timeout remaining time 794]
[Calling sys.exit(0), Time elapsed: 8.71854792535305]
Failed to read output from testmodel.py, exit status != 0:
6.216947348788381 6.229632684 5.492294318
Calling exit ...
<OMPython.OMCSessionZMQ object at 0x761337fc9340>