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 0.01403/0.01403, allocations: 1.758 MB / 20.59 MB, free: 1.277 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 0.001746/0.001746, allocations: 113.4 kB / 24.19 MB, free: 2.652 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 0.002528/0.002528, allocations: 209.7 kB / 27.92 MB, free: 4.004 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 1.571/1.571, allocations: 230.6 MB / 262.1 MB, free: 6.004 MB / 206.1 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 1.177/1.177, allocations: 130.8 MB / 449.7 MB, free: 6.52 MB / 350.1 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: SMArtInt requested package Modelica of version 4.0.0. Modelica 4.1.0 is used instead which states that it is fully compatible without conversion script needed.
Notification: ClaRa requested package Modelica of version 4.0.0. Modelica 4.1.0 is used instead which states that it is fully compatible without conversion script needed.
Notification: Skipped loading package TILMedia (1.9.0 ClaRa) using MODELICAPATH /home/hudson/saved_omc/libraries/.openmodelica/libraries (uses-annotation may be wrong).
Warning: Requested package SMArtInt of version 0.5.1, but this package was already loaded with version 0.3.1. There are no conversion annotations for this version but 0.5.1 is newer than 0.3.1. There is a possibility that 0.3.1 remains backwards compatible, but it is not loaded so OpenModelica cannot verify this.
Notification: Performance of FrontEnd - loaded program: time 0.03512/0.03512, allocations: 20.78 MB / 0.6362 GB, free: 4.633 MB / 462.1 MB
Notification: Performance of FrontEnd - Absyn->SCode: time 0.1949/0.23, allocations: 81.92 MB / 0.7162 GB, free: 2.621 MB / 0.5294 GB
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 0.6883/0.9183, allocations: 76.57 MB / 0.791 GB, free: 14.19 MB / 0.5763 GB
Notification: Performance of NFInst.instExpressions: time 0.09554/1.014, allocations: 46.36 MB / 0.8363 GB, free: 7.855 MB / 0.6075 GB
Notification: Performance of NFInst.updateImplicitVariability: time 0.01899/1.033, allocations: 246.3 kB / 0.8365 GB, free: 7.613 MB / 0.6075 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 0.02114/1.054, allocations: 5.657 MB / 0.842 GB, free: 1.941 MB / 0.6075 GB
Notification: Performance of NFTyping.typeBindings: time 0.03987/1.094, allocations: 9.69 MB / 0.8515 GB, free: 8.277 MB / 0.6232 GB
Notification: Performance of NFTyping.typeClassSections: time 0.03167/1.126, allocations: 10.23 MB / 0.8615 GB, free: 14.09 MB / 0.6388 GB
Notification: Performance of NFFlatten.flatten: time 0.0654/1.191, allocations: 42.07 MB / 0.9025 GB, free: 3.949 MB / 0.67 GB
Notification: Performance of NFFlatten.resolveConnections: time 0.02849/1.219, allocations: 13.38 MB / 0.9156 GB, free: 6.457 MB / 0.6857 GB
Notification: Performance of NFEvalConstants.evaluate: time 0.04098/1.26, allocations: 16.34 MB / 0.9316 GB, free: 6.07 MB / 0.7013 GB
Notification: Performance of NFSimplifyModel.simplify: time 0.04527/1.306, allocations: 22.38 MB / 0.9534 GB, free: 15.64 MB / 0.7325 GB
Notification: Performance of NFPackage.collectConstants: time 0.01902/1.325, allocations: 4.539 MB / 0.9579 GB, free: 11.1 MB / 0.7325 GB
Notification: Performance of NFFlatten.collectFunctions: time 0.03743/1.362, allocations: 11.69 MB / 0.9693 GB, free: 15.42 MB / 0.7482 GB
Notification: Performance of NFScalarize.scalarize: time 0.03254/1.395, allocations: 16.94 MB / 0.9858 GB, free: 14.45 MB / 0.7638 GB
Notification: Performance of NFVerifyModel.verify: time 0.05534/1.45, allocations: 20.27 MB / 1.006 GB, free: 10.09 MB / 0.7794 GB
Notification: Performance of NFConvertDAE.convert: time 1.1/2.55, allocations: 66.69 MB / 1.071 GB, free: 108.6 MB / 0.8264 GB
Notification: Performance of FrontEnd - DAE generated: time 8.085e-06/2.55, allocations: 8.906 kB / 1.071 GB, free: 108.6 MB / 0.8264 GB
Notification: Performance of FrontEnd: time 2.054e-06/2.55, allocations: 0 / 1.071 GB, free: 108.6 MB / 0.8264 GB
Notification: Performance of Transformations before backend: time 0.002025/2.552, allocations: 0 / 1.071 GB, free: 108.6 MB / 0.8264 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 0.1686/2.721, allocations: 42.71 MB / 1.112 GB, free: 95.74 MB / 0.8264 GB
Notification: Performance of prepare preOptimizeDAE: time 5.008e-05/2.721, allocations: 15.66 kB / 1.112 GB, free: 95.74 MB / 0.8264 GB
Notification: Performance of preOpt normalInlineFunction (simulation): time 0.02538/2.746, allocations: 3.56 MB / 1.116 GB, free: 93.92 MB / 0.8264 GB
Notification: Performance of preOpt evaluateParameters (simulation): time 0.09368/2.84, allocations: 37.7 MB / 1.153 GB, free: 89 MB / 0.8264 GB
Notification: Performance of preOpt simplifyIfEquations (simulation): time 0.001662/2.842, allocations: 1.082 MB / 1.154 GB, free: 88.91 MB / 0.8264 GB
Notification: Performance of preOpt expandDerOperator (simulation): time 0.01497/2.857, allocations: 1.441 MB / 1.155 GB, free: 88.88 MB / 0.8264 GB
Notification: Performance of preOpt clockPartitioning (simulation): time 0.1543/3.011, allocations: 64.18 MB / 1.218 GB, free: 28.86 MB / 0.8264 GB
Notification: Performance of preOpt findStateOrder (simulation): time 0.0008984/3.012, allocations: 113 kB / 1.218 GB, free: 28.81 MB / 0.8264 GB
Notification: Performance of preOpt replaceEdgeChange (simulation): time 0.01445/3.026, allocations: 0.6913 MB / 1.219 GB, free: 28.16 MB / 0.8264 GB
Notification: Performance of preOpt inlineArrayEqn (simulation): time 0.002999/3.029, allocations: 2.73 MB / 1.221 GB, free: 25.43 MB / 0.8264 GB
Notification: Performance of preOpt removeEqualRHS (simulation): time 0.1993/3.229, allocations: 95.2 MB / 1.314 GB, free: 10.75 MB / 0.9045 GB
Warning: The model contains alias variables with redundant start and/or conflicting nominal values. It is recommended to resolve the conflicts, because otherwise the system could be hard to solve. To print the conflicting alias sets and the chosen candidates please use -d=aliasConflicts.
Notification: Performance of preOpt removeSimpleEquations (simulation): time 1.023/4.251, allocations: 215.8 MB / 1.525 GB, free: 226.4 MB / 1.014 GB
Notification: Performance of preOpt comSubExp (simulation): time 0.105/4.356, allocations: 51.94 MB / 1.576 GB, free: 215.4 MB / 1.014 GB
Notification: Performance of preOpt resolveLoops (simulation): time 0.04464/4.401, allocations: 30.73 MB / 1.606 GB, free: 198.5 MB / 1.014 GB
Notification: Performance of preOpt evalFunc (simulation): time 0.006587/4.407, allocations: 1.219 MB / 1.607 GB, free: 198 MB / 1.014 GB
Notification: Performance of preOpt encapsulateWhenConditions (simulation): time 0.000401/4.408, allocations: 305.3 kB / 1.607 GB, free: 197.8 MB / 1.014 GB
Notification: Performance of pre-optimization done (n=3004): time 2.697e-05/4.408, allocations: 0 / 1.607 GB, free: 197.8 MB / 1.014 GB
Notification: Performance of matching and sorting (n=3005): time 1.387/5.795, allocations: 323.6 MB / 1.923 GB, free: 353.6 MB / 1.014 GB
Notification: Performance of inlineWhenForInitialization (initialization): time 0.0009416/5.796, allocations: 2.382 MB / 1.926 GB, free: 350.9 MB / 1.014 GB
Notification: Performance of selectInitializationVariablesDAE (initialization): time 0.06635/5.862, allocations: 24.48 MB / 1.949 GB, free: 342.4 MB / 1.014 GB
Notification: Performance of collectPreVariables (initialization): time 0.01136/5.873, allocations: 369.1 kB / 1.95 GB, free: 342.1 MB / 1.014 GB
Notification: Performance of collectInitialEqns (initialization): time 0.01416/5.888, allocations: 10.62 MB / 1.96 GB, free: 333.8 MB / 1.014 GB
Notification: Performance of collectInitialBindings (initialization): time 0.01979/5.907, allocations: 10.63 MB / 1.971 GB, free: 325.5 MB / 1.014 GB
Notification: Performance of simplifyInitialFunctions (initialization): time 0.04086/5.948, allocations: 6.985 MB / 1.977 GB, free: 323.2 MB / 1.014 GB
Notification: Performance of setup shared object (initialization): time 6.634e-05/5.948, allocations: 305.1 kB / 1.978 GB, free: 322.9 MB / 1.014 GB
Notification: Performance of preBalanceInitialSystem (initialization): time 0.05202/6, allocations: 33.36 MB / 2.01 GB, free: 300.8 MB / 1.014 GB
Notification: Performance of partitionIndependentBlocks (initialization): time 0.06221/6.062, allocations: 39.92 MB / 2.049 GB, free: 263.8 MB / 1.014 GB
Notification: Performance of analyzeInitialSystem (initialization): time 1.231/7.293, allocations: 248.7 MB / 2.292 GB, free: 400.8 MB / 1.014 GB
Notification: Performance of solveInitialSystemEqSystem (initialization): time 0.0002273/7.294, allocations: 52.28 kB / 2.292 GB, free: 400.8 MB / 1.014 GB
Notification: Performance of matching and sorting (n=4066) (initialization): time 0.1708/7.464, allocations: 82.3 MB / 2.373 GB, free: 369.5 MB / 1.014 GB
Notification: Performance of prepare postOptimizeDAE: time 0.0001457/7.464, allocations: 80.12 kB / 2.373 GB, free: 369.5 MB / 1.014 GB
Notification: Performance of postOpt simplifyComplexFunction (initialization): time 0.14/7.604, allocations: 74.15 MB / 2.445 GB, free: 316.7 MB / 1.014 GB
Notification: Performance of postOpt tearingSystem (initialization): time 0.01553/7.62, allocations: 5.261 MB / 2.45 GB, free: 311.3 MB / 1.014 GB
Notification: Performance of postOpt solveSimpleEquations (initialization): time 0.04924/7.669, allocations: 8.538 MB / 2.459 GB, free: 302.8 MB / 1.014 GB
Notification: Performance of postOpt calculateStrongComponentJacobians (initialization): time 0.07067/7.74, allocations: 105.4 MB / 2.562 GB, free: 190.6 MB / 1.014 GB
Notification: Performance of postOpt simplifyAllExpressions (initialization): time 0.03584/7.776, allocations: 1.335 MB / 2.563 GB, free: 189.3 MB / 1.014 GB
Notification: Performance of postOpt collapseArrayExpressions (initialization): time 0.01285/7.789, allocations: 2.167 MB / 2.565 GB, free: 187.2 MB / 1.014 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 0.08596/7.875, allocations: 41.93 MB / 2.606 GB, free: 145.3 MB / 1.014 GB
Notification: Performance of partitionIndependentBlocks (initialization_lambda0): time 0.05743/7.932, allocations: 39.25 MB / 2.644 GB, free: 103.6 MB / 1.014 GB
Notification: Performance of analyzeInitialSystem (initialization_lambda0): time 1.301/9.233, allocations: 245.9 MB / 2.884 GB, free: 337.4 MB / 1.014 GB
Notification: Performance of solveInitialSystemEqSystem (initialization_lambda0): time 0.0002243/9.233, allocations: 48 kB / 2.884 GB, free: 337.4 MB / 1.014 GB
Notification: Performance of matching and sorting (n=4066) (initialization_lambda0): time 0.1778/9.411, allocations: 80.82 MB / 2.963 GB, free: 257.7 MB / 1.014 GB
Notification: Performance of prepare postOptimizeDAE: time 0.0001367/9.411, allocations: 76.94 kB / 2.963 GB, free: 257.7 MB / 1.014 GB
Notification: Performance of postOpt simplifyComplexFunction (initialization): time 0.1451/9.556, allocations: 72.66 MB / 3.034 GB, free: 184.8 MB / 1.014 GB
Notification: Performance of postOpt tearingSystem (initialization): time 0.0158/9.572, allocations: 5.209 MB / 3.039 GB, free: 179.4 MB / 1.014 GB
Notification: Performance of postOpt solveSimpleEquations (initialization): time 0.04911/9.621, allocations: 8.464 MB / 3.048 GB, free: 170.9 MB / 1.014 GB
Notification: Performance of postOpt calculateStrongComponentJacobians (initialization): time 0.06798/9.689, allocations: 104.8 MB / 3.15 GB, free: 59.32 MB / 1.014 GB
Notification: Performance of postOpt simplifyAllExpressions (initialization): time 0.03381/9.723, allocations: 1.295 MB / 3.151 GB, free: 58.05 MB / 1.014 GB
Notification: Performance of postOpt collapseArrayExpressions (initialization): time 0.01205/9.735, allocations: 2.132 MB / 3.153 GB, free: 55.92 MB / 1.014 GB
Warning: Assuming fixed start value for the following 65 variables:
         tube.h[1]:VARIABLE(start = tube.mechanicalEquilibrium.h_start[1] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true )  \"Cell enthalpy\" type: Real [3]
         tube.h[2]:VARIABLE(start = tube.mechanicalEquilibrium.h_start[2] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true )  \"Cell enthalpy\" type: Real [3]
         tube.h[3]:VARIABLE(start = tube.mechanicalEquilibrium.h_start[3] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true )  \"Cell enthalpy\" type: Real [3]
         tube.p[1]:VARIABLE(min = 0.0 start = tube.p_start_internal[1] unit = \"Pa\" fixed = true nominal = 1e5 protected = true )  \"Cell pressure\" type: Real [3]
         tube.p[2]:VARIABLE(min = 0.0 start = tube.p_start_internal[2] unit = \"Pa\" fixed = true nominal = 1e5 protected = true )  \"Cell pressure\" type: Real [3]
         tube.p[3]:VARIABLE(min = 0.0 start = tube.p_start_internal[3] unit = \"Pa\" fixed = true nominal = 1e5 protected = true )  \"Cell pressure\" type: Real [3]
         plateHEX.flow_a.h[1]:VARIABLE(start = plateHEX.flow_a.mechanicalEquilibrium.h_start[1] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true )  \"Cell enthalpy\" type: Real [5]
         plateHEX.flow_a.h[2]:VARIABLE(start = plateHEX.flow_a.mechanicalEquilibrium.h_start[2] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true )  \"Cell enthalpy\" type: Real [5]
         plateHEX.flow_a.h[3]:VARIABLE(start = plateHEX.flow_a.mechanicalEquilibrium.h_start[3] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true )  \"Cell enthalpy\" type: Real [5]
         plateHEX.flow_a.h[4]:VARIABLE(start = plateHEX.flow_a.mechanicalEquilibrium.h_start[4] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true )  \"Cell enthalpy\" type: Real [5]
         plateHEX.flow_a.h[5]:VARIABLE(start = plateHEX.flow_a.mechanicalEquilibrium.h_start[5] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true )  \"Cell enthalpy\" type: Real [5]
         plateHEX.flow_a.p[1]:VARIABLE(min = 0.0 start = plateHEX.flow_a.p_start_internal[1] unit = \"Pa\" fixed = true nominal = 1e5 protected = true )  \"Cell pressure\" type: Real [5]
         plateHEX.flow_a.p[2]:VARIABLE(min = 0.0 start = plateHEX.flow_a.p_start_internal[2] unit = \"Pa\" fixed = true nominal = 1e5 protected = true )  \"Cell pressure\" type: Real [5]
         plateHEX.flow_a.p[3]:VARIABLE(min = 0.0 start = plateHEX.flow_a.p_start_internal[3] unit = \"Pa\" fixed = true nominal = 1e5 protected = true )  \"Cell pressure\" type: Real [5]
         plateHEX.flow_a.p[4]:VARIABLE(min = 0.0 start = plateHEX.flow_a.p_start_internal[4] unit = \"Pa\" fixed = true nominal = 1e5 protected = true )  \"Cell pressure\" type: Real [5]
         plateHEX.flow_a.p[5]:VARIABLE(min = 0.0 start = plateHEX.flow_a.p_start_internal[5] unit = \"Pa\" fixed = true nominal = 1e5 protected = true )  \"Cell pressure\" type: Real [5]
         plateHEX.flow_b.h[1]:VARIABLE(start = plateHEX.flow_b.mechanicalEquilibrium.h_start[1] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true )  \"Cell enthalpy\" type: Real [5]
         plateHEX.flow_b.h[2]:VARIABLE(start = plateHEX.flow_b.mechanicalEquilibrium.h_start[2] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true )  \"Cell enthalpy\" type: Real [5]
         plateHEX.flow_b.h[3]:VARIABLE(start = plateHEX.flow_b.mechanicalEquilibrium.h_start[3] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true )  \"Cell enthalpy\" type: Real [5]
         plateHEX.flow_b.h[4]:VARIABLE(start = plateHEX.flow_b.mechanicalEquilibrium.h_start[4] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true )  \"Cell enthalpy\" type: Real [5]
         plateHEX.flow_b.h[5]:VARIABLE(start = plateHEX.flow_b.mechanicalEquilibrium.h_start[5] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true )  \"Cell enthalpy\" type: Real [5]
         plateHEX.flow_b.p[1]:VARIABLE(min = 0.0 start = plateHEX.flow_b.p_start_internal[1] unit = \"Pa\" fixed = true nominal = 1e5 protected = true )  \"Cell pressure\" type: Real [5]
         plateHEX.flow_b.p[2]:VARIABLE(min = 0.0 start = plateHEX.flow_b.p_start_internal[2] unit = \"Pa\" fixed = true nominal = 1e5 protected = true )  \"Cell pressure\" type: Real [5]
         plateHEX.flow_b.p[3]:VARIABLE(min = 0.0 start = plateHEX.flow_b.p_start_internal[3] unit = \"Pa\" fixed = true nominal = 1e5 protected = true )  \"Cell pressure\" type: Real [5]
         plateHEX.flow_b.p[4]:VARIABLE(min = 0.0 start = plateHEX.flow_b.p_start_internal[4] unit = \"Pa\" fixed = true nominal = 1e5 protected = true )  \"Cell pressure\" type: Real [5]
         plateHEX.flow_b.p[5]:VARIABLE(min = 0.0 start = plateHEX.flow_b.p_start_internal[5] unit = \"Pa\" fixed = true nominal = 1e5 protected = true )  \"Cell pressure\" type: Real [5]
         condenser.flow_a.h[1]:VARIABLE(start = condenser.flow_a.mechanicalEquilibrium.h_start[1] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true )  \"Cell enthalpy\" type: Real [9]
         condenser.flow_a.h[2]:VARIABLE(start = condenser.flow_a.mechanicalEquilibrium.h_start[2] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true )  \"Cell enthalpy\" type: Real [9]
         condenser.flow_a.h[3]:VARIABLE(start = condenser.flow_a.mechanicalEquilibrium.h_start[3] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true )  \"Cell enthalpy\" type: Real [9]
         condenser.flow_a.h[4]:VARIABLE(start = condenser.flow_a.mechanicalEquilibrium.h_start[4] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true )  \"Cell enthalpy\" type: Real [9]
         condenser.flow_a.h[5]:VARIABLE(start = condenser.flow_a.mechanicalEquilibrium.h_start[5] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true )  \"Cell enthalpy\" type: Real [9]
         condenser.flow_a.h[6]:VARIABLE(start = condenser.flow_a.mechanicalEquilibrium.h_start[6] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true )  \"Cell enthalpy\" type: Real [9]
         condenser.flow_a.h[7]:VARIABLE(start = condenser.flow_a.mechanicalEquilibrium.h_start[7] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true )  \"Cell enthalpy\" type: Real [9]
         condenser.flow_a.h[8]:VARIABLE(start = condenser.flow_a.mechanicalEquilibrium.h_start[8] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true )  \"Cell enthalpy\" type: Real [9]
         condenser.flow_a.h[9]:VARIABLE(start = condenser.flow_a.mechanicalEquilibrium.h_start[9] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true )  \"Cell enthalpy\" type: Real [9]
         condenser.flow_a.p[1]:VARIABLE(min = 0.0 start = condenser.flow_a.p_start_internal[1] unit = \"Pa\" fixed = true nominal = 1e5 protected = true )  \"Cell pressure\" type: Real [9]
         condenser.flow_a.p[2]:VARIABLE(min = 0.0 start = condenser.flow_a.p_start_internal[2] unit = \"Pa\" fixed = true nominal = 1e5 protected = true )  \"Cell pressure\" type: Real [9]
         condenser.flow_a.p[3]:VARIABLE(min = 0.0 start = condenser.flow_a.p_start_internal[3] unit = \"Pa\" fixed = true nominal = 1e5 protected = true )  \"Cell pressure\" type: Real [9]
         condenser.flow_a.p[4]:VARIABLE(min = 0.0 start = condenser.flow_a.p_start_internal[4] unit = \"Pa\" fixed = true nominal = 1e5 protected = true )  \"Cell pressure\" type: Real [9]
         condenser.flow_a.p[5]:VARIABLE(min = 0.0 start = condenser.flow_a.p_start_internal[5] unit = \"Pa\" fixed = true nominal = 1e5 protected = true )  \"Cell pressure\" type: Real [9]
         condenser.flow_a.p[6]:VARIABLE(min = 0.0 start = condenser.flow_a.p_start_internal[6] unit = \"Pa\" fixed = true nominal = 1e5 protected = true )  \"Cell pressure\" type: Real [9]
         condenser.flow_a.p[7]:VARIABLE(min = 0.0 start = condenser.flow_a.p_start_internal[7] unit = \"Pa\" fixed = true nominal = 1e5 protected = true )  \"Cell pressure\" type: Real [9]
         condenser.flow_a.p[8]:VARIABLE(min = 0.0 start = condenser.flow_a.p_start_internal[8] unit = \"Pa\" fixed = true nominal = 1e5 protected = true )  \"Cell pressure\" type: Real [9]
         condenser.flow_a.p[9]:VARIABLE(min = 0.0 start = condenser.flow_a.p_start_internal[9] unit = \"Pa\" fixed = true nominal = 1e5 protected = true )  \"Cell pressure\" type: Real [9]
         condenser.flow_b.h[1]:VARIABLE(start = condenser.flow_b.h_start[1] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer )  \"Cell enthalpy\" type: Real [9]
         condenser.flow_b.h[2]:VARIABLE(start = condenser.flow_b.h_start[2] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer )  \"Cell enthalpy\" type: Real [9]
         condenser.flow_b.h[3]:VARIABLE(start = condenser.flow_b.h_start[3] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer )  \"Cell enthalpy\" type: Real [9]
         condenser.flow_b.h[4]:VARIABLE(start = condenser.flow_b.h_start[4] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer )  \"Cell enthalpy\" type: Real [9]
         condenser.flow_b.h[5]:VARIABLE(start = condenser.flow_b.h_start[5] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer )  \"Cell enthalpy\" type: Real [9]
         condenser.flow_b.h[6]:VARIABLE(start = condenser.flow_b.h_start[6] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer )  \"Cell enthalpy\" type: Real [9]
         condenser.flow_b.h[7]:VARIABLE(start = condenser.flow_b.h_start[7] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer )  \"Cell enthalpy\" type: Real [9]
         condenser.flow_b.h[8]:VARIABLE(start = condenser.flow_b.h_start[8] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer )  \"Cell enthalpy\" type: Real [9]
         condenser.flow_b.h[9]:VARIABLE(start = condenser.flow_b.h_start[9] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer )  \"Cell enthalpy\" type: Real [9]
         condenser.flow_b.p[1]:VARIABLE(min = 0.0 start = condenser.flow_b.p_start[1] unit = \"Pa\" fixed = true nominal = 1e5 protected = true )  \"Cell pressure\" type: Real [9]
         condenser.flow_b.p[2]:VARIABLE(min = 0.0 start = condenser.flow_b.p_start[2] unit = \"Pa\" fixed = true nominal = 1e5 protected = true )  \"Cell pressure\" type: Real [9]
         condenser.flow_b.p[3]:VARIABLE(min = 0.0 start = condenser.flow_b.p_start[3] unit = \"Pa\" fixed = true nominal = 1e5 protected = true )  \"Cell pressure\" type: Real [9]
         condenser.flow_b.p[4]:VARIABLE(min = 0.0 start = condenser.flow_b.p_start[4] unit = \"Pa\" fixed = true nominal = 1e5 protected = true )  \"Cell pressure\" type: Real [9]
         condenser.flow_b.p[5]:VARIABLE(min = 0.0 start = condenser.flow_b.p_start[5] unit = \"Pa\" fixed = true nominal = 1e5 protected = true )  \"Cell pressure\" type: Real [9]
         condenser.flow_b.p[6]:VARIABLE(min = 0.0 start = condenser.flow_b.p_start[6] unit = \"Pa\" fixed = true nominal = 1e5 protected = true )  \"Cell pressure\" type: Real [9]
         condenser.flow_b.p[7]:VARIABLE(min = 0.0 start = condenser.flow_b.p_start[7] unit = \"Pa\" fixed = true nominal = 1e5 protected = true )  \"Cell pressure\" type: Real [9]
         condenser.flow_b.p[8]:VARIABLE(min = 0.0 start = condenser.flow_b.p_start[8] unit = \"Pa\" fixed = true nominal = 1e5 protected = true )  \"Cell pressure\" type: Real [9]
         condenser.flow_b.p[9]:VARIABLE(min = 0.0 start = condenser.flow_b.p_start[9] unit = \"Pa\" fixed = true nominal = 1e5 protected = true )  \"Cell pressure\" type: Real [9]
         steamSeparator.volume.h_liq:VARIABLE(start = steamSeparator.volume.h_liq_start unit = \"J/kg\" fixed = true nominal = 1000.0 )  \"Specific enthalpy of liquid phase\" type: Real
         steamSeparator.volume.h_vap:VARIABLE(start = steamSeparator.volume.h_vap_start unit = \"J/kg\" fixed = true nominal = 1000.0 )  \"Specific enthalpy of vapour phase\" type: Real
         steamSeparator.volume.p_vap:VARIABLE(min = 0.0 start = steamSeparator.volume.p_start unit = \"Pa\" fixed = true nominal = 1e5 stateSelect=StateSelect.prefer )  \"Vapour pressure\" type: Real
Notification: Model statistics after passing the back-end for initialization:
 * Number of independent subsystems: 785
 * Number of states: 0 ()
 * Number of discrete variables: 0 ()
 * Number of discrete states: 0 ()
 * Number of clocked states: 0 ()
 * Top-level inputs: 0
Notification: Strong component statistics for initialization (3979):
 * Single equations (assignments): 3913
 * Array equations: 0
 * Algorithm blocks: 0
 * Record equations: 0
 * When equations: 0
 * If-equations: 0
 * Equation systems (not torn): 1
 * Torn equation systems: 65
 * Mixed (continuous/discrete) equation systems: 0
Notification: Equation system details (not torn):
 * Constant Jacobian (size): 0 systems
 * Linear Jacobian (size,density): 0 systems
 * Non-linear Jacobian (size): 1 system
   {1}
 * Without analytic Jacobian (size): 0 systems
Notification: Torn system details for strict tearing set:
 * Linear torn systems (#iteration vars, #inner vars, density): 64 systems
   {(1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,6,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,6,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,6,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (4,3,87.5%), (1,1,100.0%), (1,2,100.0%), (1,1,100.0%), (1,1,100.0%)}
 * Non-linear torn systems (#iteration vars, #inner vars): 1 system
   {(1,2)}
Notification: Performance of prepare postOptimizeDAE: time 0.02199/9.757, allocations: 2.334 MB / 3.156 GB, free: 53.67 MB / 1.014 GB
Notification: Performance of postOpt lateInlineFunction (simulation): time 0.01835/9.775, allocations: 2.621 MB / 3.158 GB, free: 52.55 MB / 1.014 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 0.6617/10.44, allocations: 53.71 MB / 3.211 GB, free: 354.7 MB / 1.014 GB
Error: post-optimization module wrapFunctionCalls (simulation) failed.
"
[Timeout remaining time 789]
[Calling sys.exit(0), Time elapsed: 14.747669365955517]
Failed to read output from testmodel.py, exit status != 0:
10.62240314297378 10.634457986 8.080971296
Calling exit ...
<OMPython.OMCSessionZMQ object at 0x7f3df0082ad0>