Running: ./testmodel.py --libraries=/home/hudson/saved_omc/libraries/.openmodelica/libraries --ompython_omhome=/usr ClaRa_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 0.01243/0.01243, allocations: 1.348 MB / 20.45 MB, free: 1.25 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 0.001608/0.001608, allocations: 75.17 kB / 24.02 MB, free: 2.59 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 0.001893/0.001893, allocations: 154.5 kB / 27.71 MB, free: 3.844 MB / 19.63 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 1.463/1.463, allocations: 177.1 MB / 208.4 MB, free: 7.672 MB / 190.1 MB
"
[Timeout remaining time 178]
loadFile("/home/hudson/saved_omc/libraries/.openmodelica/libraries/ClaRa 1.9.0/package.mo", uses=false) [Timeout 180]
"Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/ClaRa 1.9.0/package.mo): time 1.052/1.052, allocations: 102.5 MB / 367.8 MB, free: 4.598 MB / 334.1 MB
"
[Timeout remaining time 179]
Using package ClaRa with version 1.9.0 (/home/hudson/saved_omc/libraries/.openmodelica/libraries/ClaRa 1.9.0/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_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_ClaRa.Examples.VapourCycle_01") [Timeout 800]
"Notification: Performance of FrontEnd - loaded program: time 1.653e-06/1.653e-06, allocations: 0 / 0.5364 GB, free: 7.113 MB / 446.1 MB
Notification: Performance of FrontEnd - Absyn->SCode: time 2.776e-05/2.942e-05, allocations: 2.281 kB / 0.5364 GB, free: 7.109 MB / 446.1 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 0.1997/0.1997, allocations: 84.33 MB / 0.6188 GB, free: 5.223 MB / 0.5138 GB
Notification: Performance of NFInst.instExpressions: time 0.07666/0.2764, allocations: 43.58 MB / 0.6613 GB, free: 9.512 MB / 0.5607 GB
Notification: Performance of NFInst.updateImplicitVariability: time 0.01519/0.2915, allocations: 250.2 kB / 0.6616 GB, free: 9.266 MB / 0.5607 GB
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/ClaRa 1.9.0/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 0.01486/0.3064, allocations: 5.422 MB / 0.6669 GB, free: 3.816 MB / 0.5607 GB
Notification: Performance of NFTyping.typeBindings: time 0.02636/0.3328, allocations: 9.931 MB / 0.6766 GB, free: 9.832 MB / 0.5763 GB
Notification: Performance of NFTyping.typeClassSections: time 0.36/0.6927, allocations: 10.31 MB / 0.6866 GB, free: 30.28 MB / 0.5763 GB
Notification: Performance of NFFlatten.flatten: time 0.04935/0.7421, allocations: 42.8 MB / 0.7284 GB, free: 24.82 MB / 0.5763 GB
Notification: Performance of NFFlatten.resolveConnections: time 0.02556/0.7676, allocations: 13.97 MB / 0.7421 GB, free: 19.77 MB / 0.5763 GB
Notification: Performance of NFEvalConstants.evaluate: time 0.05276/0.8204, allocations: 22.37 MB / 0.7639 GB, free: 3.777 MB / 0.5763 GB
Notification: Performance of NFSimplifyModel.simplify: time 0.03691/0.8573, allocations: 20.82 MB / 0.7843 GB, free: 424 kB / 0.5919 GB
Notification: Performance of NFPackage.collectConstants: time 0.01405/0.8714, allocations: 4.539 MB / 0.7887 GB, free: 11.87 MB / 0.6075 GB
Notification: Performance of NFFlatten.collectFunctions: time 0.03104/0.9024, allocations: 9.34 MB / 0.7978 GB, free: 3.215 MB / 0.6075 GB
Notification: Performance of NFScalarize.scalarize: time 0.02754/0.9299, allocations: 17.42 MB / 0.8148 GB, free: 2.262 MB / 0.6232 GB
Notification: Performance of NFVerifyModel.verify: time 0.04041/0.9703, allocations: 14.33 MB / 0.8288 GB, free: 4.297 MB / 0.6388 GB
Notification: Performance of NFConvertDAE.convert: time 0.1005/1.071, allocations: 68.68 MB / 0.8959 GB, free: 1.887 MB / 0.7013 GB
Notification: Performance of FrontEnd - DAE generated: time 7.594e-06/1.071, allocations: 0 / 0.8959 GB, free: 1.887 MB / 0.7013 GB
Notification: Performance of FrontEnd: time 1.613e-06/1.071, allocations: 0 / 0.8959 GB, free: 1.887 MB / 0.7013 GB
Notification: Performance of Transformations before backend: time 0.001647/1.072, allocations: 0 / 0.8959 GB, free: 1.887 MB / 0.7013 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 0.141/1.213, allocations: 42.45 MB / 0.9373 GB, free: 8.023 MB / 0.7482 GB
Notification: Performance of prepare preOptimizeDAE: time 4.4e-05/1.213, allocations: 8.031 kB / 0.9373 GB, free: 8.016 MB / 0.7482 GB
Notification: Performance of preOpt normalInlineFunction (simulation): time 0.02047/1.234, allocations: 3.563 MB / 0.9408 GB, free: 4.434 MB / 0.7482 GB
Notification: Performance of preOpt evaluateParameters (simulation): time 0.6768/1.911, allocations: 37.73 MB / 0.9777 GB, free: 237.1 MB / 0.7795 GB
Notification: Performance of preOpt simplifyIfEquations (simulation): time 0.001498/1.912, allocations: 1.081 MB / 0.9787 GB, free: 237 MB / 0.7795 GB
Notification: Performance of preOpt expandDerOperator (simulation): time 0.01086/1.923, allocations: 1.437 MB / 0.9801 GB, free: 237 MB / 0.7795 GB
Notification: Performance of preOpt clockPartitioning (simulation): time 0.1532/2.076, allocations: 75.4 MB / 1.054 GB, free: 192.4 MB / 0.7795 GB
Notification: Performance of preOpt findStateOrder (simulation): time 0.0009631/2.077, allocations: 110.9 kB / 1.054 GB, free: 192.3 MB / 0.7795 GB
Notification: Performance of preOpt replaceEdgeChange (simulation): time 0.01019/2.087, allocations: 0.6824 MB / 1.055 GB, free: 191.7 MB / 0.7795 GB
Notification: Performance of preOpt inlineArrayEqn (simulation): time 0.002965/2.09, allocations: 2.732 MB / 1.057 GB, free: 189 MB / 0.7795 GB
Notification: Performance of preOpt removeEqualRHS (simulation): time 0.155/2.245, allocations: 94.5 MB / 1.149 GB, free: 94.41 MB / 0.7795 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 0.7214/2.967, allocations: 196.2 MB / 1.341 GB, free: 174.6 MB / 0.8108 GB
Notification: Performance of preOpt comSubExp (simulation): time 0.1065/3.073, allocations: 51.84 MB / 1.392 GB, free: 155 MB / 0.8108 GB
Notification: Performance of preOpt resolveLoops (simulation): time 0.04708/3.12, allocations: 30.72 MB / 1.422 GB, free: 138.6 MB / 0.8108 GB
Notification: Performance of preOpt evalFunc (simulation): time 0.005786/3.126, allocations: 1.057 MB / 1.423 GB, free: 138.3 MB / 0.8108 GB
Notification: Performance of preOpt encapsulateWhenConditions (simulation): time 0.0004357/3.127, allocations: 300.9 kB / 1.423 GB, free: 138.1 MB / 0.8108 GB
Notification: Performance of pre-optimization done (n=3004): time 9.336e-05/3.127, allocations: 0 / 1.423 GB, free: 138.1 MB / 0.8108 GB
Notification: Performance of matching and sorting (n=3005): time 1.115/4.242, allocations: 323.5 MB / 1.739 GB, free: 165.1 MB / 0.842 GB
Notification: Performance of inlineWhenForInitialization (initialization): time 0.0007282/4.242, allocations: 2.383 MB / 1.741 GB, free: 162.4 MB / 0.842 GB
Notification: Performance of selectInitializationVariablesDAE (initialization): time 0.04745/4.29, allocations: 23.83 MB / 1.765 GB, free: 152.8 MB / 0.842 GB
Notification: Performance of collectPreVariables (initialization): time 0.008249/4.298, allocations: 361.7 kB / 1.765 GB, free: 152.4 MB / 0.842 GB
Notification: Performance of collectInitialEqns (initialization): time 0.009773/4.308, allocations: 10.67 MB / 1.775 GB, free: 143.6 MB / 0.842 GB
Notification: Performance of collectInitialBindings (initialization): time 0.01556/4.323, allocations: 10.48 MB / 1.786 GB, free: 135.4 MB / 0.842 GB
Notification: Performance of simplifyInitialFunctions (initialization): time 0.03022/4.354, allocations: 6.846 MB / 1.792 GB, free: 129.5 MB / 0.842 GB
Notification: Performance of setup shared object (initialization): time 4.106e-05/4.354, allocations: 301.1 kB / 1.793 GB, free: 129.2 MB / 0.842 GB
Notification: Performance of preBalanceInitialSystem (initialization): time 0.0443/4.398, allocations: 33.23 MB / 1.825 GB, free: 96.53 MB / 0.842 GB
Notification: Performance of partitionIndependentBlocks (initialization): time 0.05195/4.45, allocations: 40.79 MB / 1.865 GB, free: 52.99 MB / 0.842 GB
Notification: Performance of analyzeInitialSystem (initialization): time 1.146/5.595, allocations: 250.5 MB / 2.109 GB, free: 99.92 MB / 0.842 GB
Notification: Performance of solveInitialSystemEqSystem (initialization): time 0.000239/5.596, allocations: 52 kB / 2.11 GB, free: 99.87 MB / 0.842 GB
Notification: Performance of matching and sorting (n=4020) (initialization): time 0.157/5.753, allocations: 81.91 MB / 2.19 GB, free: 19.1 MB / 0.842 GB
Notification: Performance of prepare postOptimizeDAE: time 0.0001251/5.753, allocations: 76.19 kB / 2.19 GB, free: 19.02 MB / 0.842 GB
Notification: Performance of postOpt simplifyComplexFunction (initialization): time 0.5145/6.267, allocations: 73.82 MB / 2.262 GB, free: 236.4 MB / 0.842 GB
Notification: Performance of postOpt tearingSystem (initialization): time 0.01613/6.283, allocations: 5.306 MB / 2.267 GB, free: 234.7 MB / 0.842 GB
Notification: Performance of postOpt solveSimpleEquations (initialization): time 0.04947/6.333, allocations: 8.463 MB / 2.275 GB, free: 234.2 MB / 0.842 GB
Notification: Performance of postOpt calculateStrongComponentJacobians (initialization): time 0.06777/6.401, allocations: 103.5 MB / 2.376 GB, free: 138.4 MB / 0.842 GB
Notification: Performance of postOpt simplifyAllExpressions (initialization): time 0.02973/6.43, allocations: 1.33 MB / 2.377 GB, free: 137.2 MB / 0.842 GB
Notification: Performance of postOpt collapseArrayExpressions (initialization): time 0.009616/6.44, allocations: 2.159 MB / 2.38 GB, free: 135 MB / 0.842 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 0.06883/6.509, allocations: 41.79 MB / 2.42 GB, free: 93.4 MB / 0.842 GB
Notification: Performance of partitionIndependentBlocks (initialization_lambda0): time 0.05212/6.561, allocations: 40.11 MB / 2.46 GB, free: 50.52 MB / 0.842 GB
Notification: Performance of analyzeInitialSystem (initialization_lambda0): time 1.147/7.708, allocations: 247.7 MB / 2.701 GB, free: 130.8 MB / 0.8577 GB
Notification: Performance of solveInitialSystemEqSystem (initialization_lambda0): time 0.000203/7.709, allocations: 48 kB / 2.701 GB, free: 130.8 MB / 0.8577 GB
Notification: Performance of matching and sorting (n=4020) (initialization_lambda0): time 0.1479/7.857, allocations: 80.42 MB / 2.78 GB, free: 51.54 MB / 0.8577 GB
Notification: Performance of prepare postOptimizeDAE: time 0.0001201/7.857, allocations: 80.78 kB / 2.78 GB, free: 51.46 MB / 0.8577 GB
Notification: Performance of postOpt simplifyComplexFunction (initialization): time 0.5511/8.408, allocations: 72.3 MB / 2.851 GB, free: 254.4 MB / 0.8889 GB
Notification: Performance of postOpt tearingSystem (initialization): time 0.01741/8.425, allocations: 5.249 MB / 2.856 GB, free: 253.9 MB / 0.8889 GB
Notification: Performance of postOpt solveSimpleEquations (initialization): time 0.05231/8.477, allocations: 8.392 MB / 2.864 GB, free: 253.9 MB / 0.8889 GB
Notification: Performance of postOpt calculateStrongComponentJacobians (initialization): time 0.06807/8.545, allocations: 102.9 MB / 2.964 GB, free: 172.8 MB / 0.8889 GB
Notification: Performance of postOpt simplifyAllExpressions (initialization): time 0.03098/8.576, allocations: 1.296 MB / 2.966 GB, free: 172.3 MB / 0.8889 GB
Notification: Performance of postOpt collapseArrayExpressions (initialization): time 0.01015/8.587, allocations: 2.118 MB / 2.968 GB, free: 172 MB / 0.8889 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 0.01966/8.606, allocations: 2.325 MB / 2.97 GB, free: 170.6 MB / 0.8889 GB
Notification: Performance of postOpt lateInlineFunction (simulation): time 0.01691/8.623, allocations: 2.559 MB / 2.973 GB, free: 170.6 MB / 0.8889 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 0.1083/8.732, allocations: 53.75 MB / 3.025 GB, free: 146.1 MB / 0.8889 GB
Error: post-optimization module wrapFunctionCalls (simulation) failed.
"
[Timeout remaining time 791]
[Calling sys.exit(0), Time elapsed: 12.527740154415369]
Failed to read output from testmodel.py, exit status != 0:
8.924242608249187 8.934101985 7.860487538
Calling exit ...
<OMPython.OMCSessionZMQ object at 0x7fd33e29cfd0>