Running: ./testmodel.py --libraries=/home/hudson/saved_omc/libraries/.openmodelica/libraries --ompython_omhome=/usr ClaRa_ClaRa.Components.HeatExchangers.Check.Test_FlatTubeFinnedHEXvle2gas_L4.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 0.01326/0.01326, allocations: 1.348 MB / 20.45 MB, free: 1.262 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 0.001685/0.001685, allocations: 78.88 kB / 24.02 MB, free: 2.609 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 0.002445/0.002445, allocations: 151.7 kB / 27.7 MB, free: 3.863 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 1.442/1.442, allocations: 177.1 MB / 208.4 MB, free: 7.676 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 1.12/1.12, allocations: 102.5 MB / 367.8 MB, free: 4.602 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.Components.HeatExchangers.Check.Test_FlatTubeFinnedHEXvle2gas_L4,tolerance=1e-06,outputFormat="mat",numberOfIntervals=2500,variableFilter="Time|flatTubeFinnedHX.finWall.U.1.|flatTubeFinnedHX.finWall.U.2.|flatTubeFinnedHX.finWall.U.3.|flatTubeFinnedHX.finWall.U.4.|flatTubeFinnedHX.finWall.U.5.|flatTubeFinnedHX.finWall.U.6.|flatTubeFinnedHX.finWall.U.7.|flatTubeFinnedHX.finWall.U.8.|flatTubeFinnedHX.finWall.U.9.|flatTubeFinnedHX.flow_a.h.1.|flatTubeFinnedHX.flow_a.h.2.|flatTubeFinnedHX.flow_a.h.3.|flatTubeFinnedHX.flow_a.h.4.|flatTubeFinnedHX.flow_a.h.5.|flatTubeFinnedHX.flow_a.h.6.|flatTubeFinnedHX.flow_a.h.7.|flatTubeFinnedHX.flow_a.h.8.|flatTubeFinnedHX.flow_a.h.9.|flatTubeFinnedHX.flow_a.p.1.|flatTubeFinnedHX.flow_a.p.2.|flatTubeFinnedHX.flow_a.p.3.|flatTubeFinnedHX.flow_a.p.4.|flatTubeFinnedHX.flow_a.p.5.|flatTubeFinnedHX.flow_a.p.6.|flatTubeFinnedHX.flow_a.p.7.|flatTubeFinnedHX.flow_a.p.8.|flatTubeFinnedHX.flow_a.p.9.|flatTubeFinnedHX.flow_b.h.1.|flatTubeFinnedHX.flow_b.h.2.|flatTubeFinnedHX.flow_b.h.3.|flatTubeFinnedHX.flow_b.h.4.|flatTubeFinnedHX.flow_b.h.5.|flatTubeFinnedHX.flow_b.h.6.|flatTubeFinnedHX.flow_b.h.7.|flatTubeFinnedHX.flow_b.h.8.|flatTubeFinnedHX.flow_b.h.9.|flatTubeFinnedHX.flow_b.p.1.|flatTubeFinnedHX.flow_b.p.2.|flatTubeFinnedHX.flow_b.p.3.|flatTubeFinnedHX.flow_b.p.4.|flatTubeFinnedHX.flow_b.p.5.|flatTubeFinnedHX.flow_b.p.6.|flatTubeFinnedHX.flow_b.p.7.|flatTubeFinnedHX.flow_b.p.8.|flatTubeFinnedHX.flow_b.p.9.|flatTubeFinnedHX.flow_b.xi.1,1.|flatTubeFinnedHX.flow_b.xi.1,2.|flatTubeFinnedHX.flow_b.xi.1,3.|flatTubeFinnedHX.flow_b.xi.1,4.|flatTubeFinnedHX.flow_b.xi.1,5.|flatTubeFinnedHX.flow_b.xi.1,6.|flatTubeFinnedHX.flow_b.xi.1,7.|flatTubeFinnedHX.flow_b.xi.1,8.|flatTubeFinnedHX.flow_b.xi.1,9.|flatTubeFinnedHX.flow_b.xi.2,1.|flatTubeFinnedHX.flow_b.xi.2,2.|flatTubeFinnedHX.flow_b.xi.2,3.|flatTubeFinnedHX.flow_b.xi.2,4.|flatTubeFinnedHX.flow_b.xi.2,5.|flatTubeFinnedHX.flow_b.xi.2,6.|flatTubeFinnedHX.flow_b.xi.2,7.|flatTubeFinnedHX.flow_b.xi.2,8.|flatTubeFinnedHX.flow_b.xi.2,9.|flatTubeFinnedHX.flow_b.xi.3,1.|flatTubeFinnedHX.flow_b.xi.3,2.|flatTubeFinnedHX.flow_b.xi.3,3.|flatTubeFinnedHX.flow_b.xi.3,4.|flatTubeFinnedHX.flow_b.xi.3,5.|flatTubeFinnedHX.flow_b.xi.3,6.|flatTubeFinnedHX.flow_b.xi.3,7.|flatTubeFinnedHX.flow_b.xi.3,8.|flatTubeFinnedHX.flow_b.xi.3,9.|flatTubeFinnedHX.flow_b.xi.4,1.|flatTubeFinnedHX.flow_b.xi.4,2.|flatTubeFinnedHX.flow_b.xi.4,3.|flatTubeFinnedHX.flow_b.xi.4,4.|flatTubeFinnedHX.flow_b.xi.4,5.|flatTubeFinnedHX.flow_b.xi.4,6.|flatTubeFinnedHX.flow_b.xi.4,7.|flatTubeFinnedHX.flow_b.xi.4,8.|flatTubeFinnedHX.flow_b.xi.4,9.|flatTubeFinnedHX.flow_b.xi.5,1.|flatTubeFinnedHX.flow_b.xi.5,2.|flatTubeFinnedHX.flow_b.xi.5,3.|flatTubeFinnedHX.flow_b.xi.5,4.|flatTubeFinnedHX.flow_b.xi.5,5.|flatTubeFinnedHX.flow_b.xi.5,6.|flatTubeFinnedHX.flow_b.xi.5,7.|flatTubeFinnedHX.flow_b.xi.5,8.|flatTubeFinnedHX.flow_b.xi.5,9.|flatTubeFinnedHX.flow_b.xi.6,1.|flatTubeFinnedHX.flow_b.xi.6,2.|flatTubeFinnedHX.flow_b.xi.6,3.|flatTubeFinnedHX.flow_b.xi.6,4.|flatTubeFinnedHX.flow_b.xi.6,5.|flatTubeFinnedHX.flow_b.xi.6,6.|flatTubeFinnedHX.flow_b.xi.6,7.|flatTubeFinnedHX.flow_b.xi.6,8.|flatTubeFinnedHX.flow_b.xi.6,9.|flatTubeFinnedHX.flow_b.xi.7,1.|flatTubeFinnedHX.flow_b.xi.7,2.|flatTubeFinnedHX.flow_b.xi.7,3.|flatTubeFinnedHX.flow_b.xi.7,4.|flatTubeFinnedHX.flow_b.xi.7,5.|flatTubeFinnedHX.flow_b.xi.7,6.|flatTubeFinnedHX.flow_b.xi.7,7.|flatTubeFinnedHX.flow_b.xi.7,8.|flatTubeFinnedHX.flow_b.xi.7,9.|flatTubeFinnedHX.flow_b.xi.8,1.|flatTubeFinnedHX.flow_b.xi.8,2.|flatTubeFinnedHX.flow_b.xi.8,3.|flatTubeFinnedHX.flow_b.xi.8,4.|flatTubeFinnedHX.flow_b.xi.8,5.|flatTubeFinnedHX.flow_b.xi.8,6.|flatTubeFinnedHX.flow_b.xi.8,7.|flatTubeFinnedHX.flow_b.xi.8,8.|flatTubeFinnedHX.flow_b.xi.8,9.|flatTubeFinnedHX.flow_b.xi.9,1.|flatTubeFinnedHX.flow_b.xi.9,2.|flatTubeFinnedHX.flow_b.xi.9,3.|flatTubeFinnedHX.flow_b.xi.9,4.|flatTubeFinnedHX.flow_b.xi.9,5.|flatTubeFinnedHX.flow_b.xi.9,6.|flatTubeFinnedHX.flow_b.xi.9,7.|flatTubeFinnedHX.flow_b.xi.9,8.|flatTubeFinnedHX.flow_b.xi.9,9.|flatTubeFinnedHX.tubeWall.U.1.|flatTubeFinnedHX.tubeWall.U.2.|flatTubeFinnedHX.tubeWall.U.3.|flatTubeFinnedHX.tubeWall.U.4.|flatTubeFinnedHX.tubeWall.U.5.|flatTubeFinnedHX.tubeWall.U.6.|flatTubeFinnedHX.tubeWall.U.7.|flatTubeFinnedHX.tubeWall.U.8.|flatTubeFinnedHX.tubeWall.U.9.",fileNamePrefix="ClaRa_ClaRa.Components.HeatExchangers.Check.Test_FlatTubeFinnedHEXvle2gas_L4")
translateModel(ClaRa.Components.HeatExchangers.Check.Test_FlatTubeFinnedHEXvle2gas_L4,tolerance=1e-06,outputFormat="mat",numberOfIntervals=2500,variableFilter="Time|flatTubeFinnedHX.finWall.U.1.|flatTubeFinnedHX.finWall.U.2.|flatTubeFinnedHX.finWall.U.3.|flatTubeFinnedHX.finWall.U.4.|flatTubeFinnedHX.finWall.U.5.|flatTubeFinnedHX.finWall.U.6.|flatTubeFinnedHX.finWall.U.7.|flatTubeFinnedHX.finWall.U.8.|flatTubeFinnedHX.finWall.U.9.|flatTubeFinnedHX.flow_a.h.1.|flatTubeFinnedHX.flow_a.h.2.|flatTubeFinnedHX.flow_a.h.3.|flatTubeFinnedHX.flow_a.h.4.|flatTubeFinnedHX.flow_a.h.5.|flatTubeFinnedHX.flow_a.h.6.|flatTubeFinnedHX.flow_a.h.7.|flatTubeFinnedHX.flow_a.h.8.|flatTubeFinnedHX.flow_a.h.9.|flatTubeFinnedHX.flow_a.p.1.|flatTubeFinnedHX.flow_a.p.2.|flatTubeFinnedHX.flow_a.p.3.|flatTubeFinnedHX.flow_a.p.4.|flatTubeFinnedHX.flow_a.p.5.|flatTubeFinnedHX.flow_a.p.6.|flatTubeFinnedHX.flow_a.p.7.|flatTubeFinnedHX.flow_a.p.8.|flatTubeFinnedHX.flow_a.p.9.|flatTubeFinnedHX.flow_b.h.1.|flatTubeFinnedHX.flow_b.h.2.|flatTubeFinnedHX.flow_b.h.3.|flatTubeFinnedHX.flow_b.h.4.|flatTubeFinnedHX.flow_b.h.5.|flatTubeFinnedHX.flow_b.h.6.|flatTubeFinnedHX.flow_b.h.7.|flatTubeFinnedHX.flow_b.h.8.|flatTubeFinnedHX.flow_b.h.9.|flatTubeFinnedHX.flow_b.p.1.|flatTubeFinnedHX.flow_b.p.2.|flatTubeFinnedHX.flow_b.p.3.|flatTubeFinnedHX.flow_b.p.4.|flatTubeFinnedHX.flow_b.p.5.|flatTubeFinnedHX.flow_b.p.6.|flatTubeFinnedHX.flow_b.p.7.|flatTubeFinnedHX.flow_b.p.8.|flatTubeFinnedHX.flow_b.p.9.|flatTubeFinnedHX.flow_b.xi.1,1.|flatTubeFinnedHX.flow_b.xi.1,2.|flatTubeFinnedHX.flow_b.xi.1,3.|flatTubeFinnedHX.flow_b.xi.1,4.|flatTubeFinnedHX.flow_b.xi.1,5.|flatTubeFinnedHX.flow_b.xi.1,6.|flatTubeFinnedHX.flow_b.xi.1,7.|flatTubeFinnedHX.flow_b.xi.1,8.|flatTubeFinnedHX.flow_b.xi.1,9.|flatTubeFinnedHX.flow_b.xi.2,1.|flatTubeFinnedHX.flow_b.xi.2,2.|flatTubeFinnedHX.flow_b.xi.2,3.|flatTubeFinnedHX.flow_b.xi.2,4.|flatTubeFinnedHX.flow_b.xi.2,5.|flatTubeFinnedHX.flow_b.xi.2,6.|flatTubeFinnedHX.flow_b.xi.2,7.|flatTubeFinnedHX.flow_b.xi.2,8.|flatTubeFinnedHX.flow_b.xi.2,9.|flatTubeFinnedHX.flow_b.xi.3,1.|flatTubeFinnedHX.flow_b.xi.3,2.|flatTubeFinnedHX.flow_b.xi.3,3.|flatTubeFinnedHX.flow_b.xi.3,4.|flatTubeFinnedHX.flow_b.xi.3,5.|flatTubeFinnedHX.flow_b.xi.3,6.|flatTubeFinnedHX.flow_b.xi.3,7.|flatTubeFinnedHX.flow_b.xi.3,8.|flatTubeFinnedHX.flow_b.xi.3,9.|flatTubeFinnedHX.flow_b.xi.4,1.|flatTubeFinnedHX.flow_b.xi.4,2.|flatTubeFinnedHX.flow_b.xi.4,3.|flatTubeFinnedHX.flow_b.xi.4,4.|flatTubeFinnedHX.flow_b.xi.4,5.|flatTubeFinnedHX.flow_b.xi.4,6.|flatTubeFinnedHX.flow_b.xi.4,7.|flatTubeFinnedHX.flow_b.xi.4,8.|flatTubeFinnedHX.flow_b.xi.4,9.|flatTubeFinnedHX.flow_b.xi.5,1.|flatTubeFinnedHX.flow_b.xi.5,2.|flatTubeFinnedHX.flow_b.xi.5,3.|flatTubeFinnedHX.flow_b.xi.5,4.|flatTubeFinnedHX.flow_b.xi.5,5.|flatTubeFinnedHX.flow_b.xi.5,6.|flatTubeFinnedHX.flow_b.xi.5,7.|flatTubeFinnedHX.flow_b.xi.5,8.|flatTubeFinnedHX.flow_b.xi.5,9.|flatTubeFinnedHX.flow_b.xi.6,1.|flatTubeFinnedHX.flow_b.xi.6,2.|flatTubeFinnedHX.flow_b.xi.6,3.|flatTubeFinnedHX.flow_b.xi.6,4.|flatTubeFinnedHX.flow_b.xi.6,5.|flatTubeFinnedHX.flow_b.xi.6,6.|flatTubeFinnedHX.flow_b.xi.6,7.|flatTubeFinnedHX.flow_b.xi.6,8.|flatTubeFinnedHX.flow_b.xi.6,9.|flatTubeFinnedHX.flow_b.xi.7,1.|flatTubeFinnedHX.flow_b.xi.7,2.|flatTubeFinnedHX.flow_b.xi.7,3.|flatTubeFinnedHX.flow_b.xi.7,4.|flatTubeFinnedHX.flow_b.xi.7,5.|flatTubeFinnedHX.flow_b.xi.7,6.|flatTubeFinnedHX.flow_b.xi.7,7.|flatTubeFinnedHX.flow_b.xi.7,8.|flatTubeFinnedHX.flow_b.xi.7,9.|flatTubeFinnedHX.flow_b.xi.8,1.|flatTubeFinnedHX.flow_b.xi.8,2.|flatTubeFinnedHX.flow_b.xi.8,3.|flatTubeFinnedHX.flow_b.xi.8,4.|flatTubeFinnedHX.flow_b.xi.8,5.|flatTubeFinnedHX.flow_b.xi.8,6.|flatTubeFinnedHX.flow_b.xi.8,7.|flatTubeFinnedHX.flow_b.xi.8,8.|flatTubeFinnedHX.flow_b.xi.8,9.|flatTubeFinnedHX.flow_b.xi.9,1.|flatTubeFinnedHX.flow_b.xi.9,2.|flatTubeFinnedHX.flow_b.xi.9,3.|flatTubeFinnedHX.flow_b.xi.9,4.|flatTubeFinnedHX.flow_b.xi.9,5.|flatTubeFinnedHX.flow_b.xi.9,6.|flatTubeFinnedHX.flow_b.xi.9,7.|flatTubeFinnedHX.flow_b.xi.9,8.|flatTubeFinnedHX.flow_b.xi.9,9.|flatTubeFinnedHX.tubeWall.U.1.|flatTubeFinnedHX.tubeWall.U.2.|flatTubeFinnedHX.tubeWall.U.3.|flatTubeFinnedHX.tubeWall.U.4.|flatTubeFinnedHX.tubeWall.U.5.|flatTubeFinnedHX.tubeWall.U.6.|flatTubeFinnedHX.tubeWall.U.7.|flatTubeFinnedHX.tubeWall.U.8.|flatTubeFinnedHX.tubeWall.U.9.",fileNamePrefix="ClaRa_ClaRa.Components.HeatExchangers.Check.Test_FlatTubeFinnedHEXvle2gas_L4") [Timeout 800]
"Notification: Performance of FrontEnd - loaded program: time 2.565e-06/2.565e-06, allocations: 0 / 0.5365 GB, free: 7.094 MB / 446.1 MB
Notification: Performance of FrontEnd - Absyn->SCode: time 4.679e-05/4.935e-05, allocations: 2.281 kB / 0.5365 GB, free: 7.09 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.Components.HeatExchangers.Check.Test_FlatTubeFinnedHEXvle2gas_L4): time 0.1857/0.1857, allocations: 63.05 MB / 0.5981 GB, free: 10.53 MB / 0.4982 GB
Notification: Performance of NFInst.instExpressions: time 0.05532/0.2411, allocations: 30.78 MB / 0.6281 GB, free: 11.65 MB / 0.5294 GB
Notification: Performance of NFInst.updateImplicitVariability: time 0.005191/0.2463, allocations: 91.38 kB / 0.6282 GB, free: 11.56 MB / 0.5294 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 0.008668/0.2549, allocations: 2.583 MB / 0.6307 GB, free: 8.969 MB / 0.5294 GB
Notification: Performance of NFTyping.typeBindings: time 0.01153/0.2665, allocations: 3.711 MB / 0.6343 GB, free: 5.238 MB / 0.5294 GB
Notification: Performance of NFTyping.typeClassSections: time 0.01496/0.2814, allocations: 5.636 MB / 0.6399 GB, free: 15.58 MB / 0.545 GB
Notification: Performance of NFFlatten.flatten: time 0.0287/0.3101, allocations: 21.66 MB / 0.661 GB, free: 9.879 MB / 0.5607 GB
Notification: Performance of NFFlatten.resolveConnections: time 0.01485/0.325, allocations: 8.087 MB / 0.6689 GB, free: 1.684 MB / 0.5607 GB
Notification: Performance of NFEvalConstants.evaluate: time 0.02774/0.3527, allocations: 11.45 MB / 0.6801 GB, free: 6.215 MB / 0.5763 GB
Notification: Performance of NFSimplifyModel.simplify: time 0.4315/0.7842, allocations: 12.9 MB / 0.6927 GB, free: 41.54 MB / 0.5763 GB
Notification: Performance of NFPackage.collectConstants: time 0.01571/0.7999, allocations: 3.188 MB / 0.6958 GB, free: 41.54 MB / 0.5763 GB
Notification: Performance of NFFlatten.collectFunctions: time 0.0242/0.8241, allocations: 7.065 MB / 0.7027 GB, free: 41.54 MB / 0.5763 GB
Notification: Performance of NFScalarize.scalarize: time 0.02056/0.8447, allocations: 11.81 MB / 0.7142 GB, free: 41.54 MB / 0.5763 GB
Notification: Performance of NFVerifyModel.verify: time 0.02936/0.874, allocations: 9.546 MB / 0.7235 GB, free: 40.49 MB / 0.5763 GB
Notification: Performance of NFConvertDAE.convert: time 0.06092/0.935, allocations: 47.9 MB / 0.7703 GB, free: 11.68 MB / 0.5763 GB
Notification: Performance of FrontEnd - DAE generated: time 6.762e-06/0.935, allocations: 0 / 0.7703 GB, free: 11.68 MB / 0.5763 GB
Notification: Performance of FrontEnd: time 1.924e-06/0.935, allocations: 0 / 0.7703 GB, free: 11.68 MB / 0.5763 GB
Notification: Performance of Transformations before backend: time 0.001241/0.9362, allocations: 0 / 0.7703 GB, free: 11.68 MB / 0.5763 GB
Notification: Model statistics after passing the front-end and creating the data structures used by the back-end:
 * Number of equations: 3282
 * Number of variables: 3282
Notification: Performance of Generate backend data structure: time 0.1137/1.05, allocations: 29.41 MB / 0.799 GB, free: 14.73 MB / 0.6075 GB
Notification: Performance of prepare preOptimizeDAE: time 4.973e-05/1.05, allocations: 8.031 kB / 0.7991 GB, free: 14.72 MB / 0.6075 GB
Notification: Performance of preOpt normalInlineFunction (simulation): time 0.01637/1.066, allocations: 2.072 MB / 0.8011 GB, free: 12.64 MB / 0.6075 GB
Notification: Performance of preOpt evaluateParameters (simulation): time 0.07501/1.141, allocations: 28.38 MB / 0.8288 GB, free: 0.8008 MB / 0.6232 GB
Notification: Performance of preOpt simplifyIfEquations (simulation): time 0.001005/1.142, allocations: 0.5696 MB / 0.8294 GB, free: 256 kB / 0.6232 GB
Notification: Performance of preOpt expandDerOperator (simulation): time 0.008793/1.151, allocations: 0.8282 MB / 0.8302 GB, free: 15.44 MB / 0.6388 GB
Notification: Performance of preOpt clockPartitioning (simulation): time 0.1324/1.284, allocations: 53.84 MB / 0.8827 GB, free: 5.957 MB / 0.6857 GB
Notification: Performance of preOpt findStateOrder (simulation): time 0.0005356/1.284, allocations: 33.97 kB / 0.8828 GB, free: 5.945 MB / 0.6857 GB
Notification: Performance of preOpt replaceEdgeChange (simulation): time 0.008027/1.292, allocations: 389.5 kB / 0.8831 GB, free: 5.59 MB / 0.6857 GB
Notification: Performance of preOpt inlineArrayEqn (simulation): time 0.00273/1.295, allocations: 1.913 MB / 0.885 GB, free: 3.676 MB / 0.6857 GB
Notification: Performance of preOpt removeEqualRHS (simulation): time 0.1808/1.476, allocations: 79.43 MB / 0.9626 GB, free: 4.398 MB / 0.7638 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 0.7619/2.237, allocations: 122.8 MB / 1.082 GB, free: 136.8 MB / 0.7638 GB
Notification: Performance of preOpt comSubExp (simulation): time 0.06901/2.306, allocations: 36.1 MB / 1.118 GB, free: 100.8 MB / 0.7638 GB
Notification: Performance of preOpt resolveLoops (simulation): time 0.03309/2.34, allocations: 25.58 MB / 1.143 GB, free: 75.12 MB / 0.7638 GB
Notification: Performance of preOpt evalFunc (simulation): time 0.004002/2.344, allocations: 0.7988 MB / 1.143 GB, free: 74.33 MB / 0.7638 GB
Notification: Performance of preOpt encapsulateWhenConditions (simulation): time 0.0001842/2.344, allocations: 197.5 kB / 1.144 GB, free: 74.13 MB / 0.7638 GB
Notification: Performance of pre-optimization done (n=1780): time 2.285e-05/2.344, allocations: 2.406 kB / 1.144 GB, free: 74.13 MB / 0.7638 GB
Notification: Performance of matching and sorting (n=1780): time 0.1993/2.543, allocations: 86.17 MB / 1.228 GB, free: 4.395 MB / 0.7794 GB
Notification: Performance of inlineWhenForInitialization (initialization): time 0.0007355/2.544, allocations: 0.9655 MB / 1.229 GB, free: 3.238 MB / 0.7794 GB
Notification: Performance of selectInitializationVariablesDAE (initialization): time 0.04296/2.587, allocations: 14.72 MB / 1.243 GB, free: 4.684 MB / 0.795 GB
Notification: Performance of collectPreVariables (initialization): time 0.0072/2.594, allocations: 268.1 kB / 1.243 GB, free: 4.418 MB / 0.795 GB
Notification: Performance of collectInitialEqns (initialization): time 0.011/2.605, allocations: 6.05 MB / 1.249 GB, free: 14.82 MB / 0.8107 GB
Notification: Performance of collectInitialBindings (initialization): time 0.01611/2.621, allocations: 6.267 MB / 1.255 GB, free: 8.762 MB / 0.8107 GB
Notification: Performance of simplifyInitialFunctions (initialization): time 0.03096/2.652, allocations: 4.255 MB / 1.26 GB, free: 4.496 MB / 0.8107 GB
Notification: Performance of setup shared object (initialization): time 0.0001389/2.652, allocations: 305.1 kB / 1.26 GB, free: 4.195 MB / 0.8107 GB
Notification: Performance of preBalanceInitialSystem (initialization): time 0.4574/3.11, allocations: 25.89 MB / 1.285 GB, free: 287.5 MB / 0.8263 GB
Notification: Performance of partitionIndependentBlocks (initialization): time 0.04782/3.157, allocations: 29.25 MB / 1.314 GB, free: 276.8 MB / 0.8263 GB
Notification: Performance of analyzeInitialSystem (initialization): time 0.5512/3.709, allocations: 197.5 MB / 1.507 GB, free: 116.1 MB / 0.8263 GB
Notification: Performance of solveInitialSystemEqSystem (initialization): time 0.0001046/3.709, allocations: 20 kB / 1.507 GB, free: 116.1 MB / 0.8263 GB
Notification: Performance of matching and sorting (n=2295) (initialization): time 0.1252/3.834, allocations: 60.77 MB / 1.566 GB, free: 55.96 MB / 0.8263 GB
Notification: Performance of prepare postOptimizeDAE: time 0.0001643/3.834, allocations: 35.94 kB / 1.566 GB, free: 55.93 MB / 0.8263 GB
Notification: Performance of postOpt simplifyComplexFunction (initialization): time 0.5845/4.419, allocations: 57.11 MB / 1.622 GB, free: 275.6 MB / 0.8263 GB
Notification: Performance of postOpt tearingSystem (initialization): time 0.0108/4.429, allocations: 3.49 MB / 1.625 GB, free: 274.6 MB / 0.8263 GB
Notification: Performance of postOpt solveSimpleEquations (initialization): time 0.0408/4.47, allocations: 5.196 MB / 1.63 GB, free: 274.2 MB / 0.8263 GB
Notification: Performance of postOpt calculateStrongComponentJacobians (initialization): time 0.04559/4.516, allocations: 63.67 MB / 1.692 GB, free: 220.3 MB / 0.8263 GB
Notification: Performance of postOpt simplifyAllExpressions (initialization): time 0.02718/4.543, allocations: 1.673 MB / 1.694 GB, free: 220 MB / 0.8263 GB
Notification: Performance of postOpt collapseArrayExpressions (initialization): time 0.01087/4.554, allocations: 1.377 MB / 1.695 GB, free: 219.8 MB / 0.8263 GB
Warning: Assuming fixed start value for the following 36 variables:
         flatTubeFinnedHX.flow_a.h[1]:VARIABLE(start = flatTubeFinnedHX.flow_a.mechanicalEquilibrium.h_start[1] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true )  \"Cell enthalpy\" type: Real [9]
         flatTubeFinnedHX.flow_a.h[2]:VARIABLE(start = flatTubeFinnedHX.flow_a.mechanicalEquilibrium.h_start[2] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true )  \"Cell enthalpy\" type: Real [9]
         flatTubeFinnedHX.flow_a.h[3]:VARIABLE(start = flatTubeFinnedHX.flow_a.mechanicalEquilibrium.h_start[3] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true )  \"Cell enthalpy\" type: Real [9]
         flatTubeFinnedHX.flow_a.h[4]:VARIABLE(start = flatTubeFinnedHX.flow_a.mechanicalEquilibrium.h_start[4] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true )  \"Cell enthalpy\" type: Real [9]
         flatTubeFinnedHX.flow_a.h[5]:VARIABLE(start = flatTubeFinnedHX.flow_a.mechanicalEquilibrium.h_start[5] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true )  \"Cell enthalpy\" type: Real [9]
         flatTubeFinnedHX.flow_a.h[6]:VARIABLE(start = flatTubeFinnedHX.flow_a.mechanicalEquilibrium.h_start[6] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true )  \"Cell enthalpy\" type: Real [9]
         flatTubeFinnedHX.flow_a.h[7]:VARIABLE(start = flatTubeFinnedHX.flow_a.mechanicalEquilibrium.h_start[7] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true )  \"Cell enthalpy\" type: Real [9]
         flatTubeFinnedHX.flow_a.h[8]:VARIABLE(start = flatTubeFinnedHX.flow_a.mechanicalEquilibrium.h_start[8] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true )  \"Cell enthalpy\" type: Real [9]
         flatTubeFinnedHX.flow_a.h[9]:VARIABLE(start = flatTubeFinnedHX.flow_a.mechanicalEquilibrium.h_start[9] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true )  \"Cell enthalpy\" type: Real [9]
         flatTubeFinnedHX.flow_a.p[1]:VARIABLE(min = 0.0 start = flatTubeFinnedHX.flow_a.p_start_internal[1] unit = \"Pa\" fixed = true nominal = 1e5 protected = true )  \"Cell pressure\" type: Real [9]
         flatTubeFinnedHX.flow_a.p[2]:VARIABLE(min = 0.0 start = flatTubeFinnedHX.flow_a.p_start_internal[2] unit = \"Pa\" fixed = true nominal = 1e5 protected = true )  \"Cell pressure\" type: Real [9]
         flatTubeFinnedHX.flow_a.p[3]:VARIABLE(min = 0.0 start = flatTubeFinnedHX.flow_a.p_start_internal[3] unit = \"Pa\" fixed = true nominal = 1e5 protected = true )  \"Cell pressure\" type: Real [9]
         flatTubeFinnedHX.flow_a.p[4]:VARIABLE(min = 0.0 start = flatTubeFinnedHX.flow_a.p_start_internal[4] unit = \"Pa\" fixed = true nominal = 1e5 protected = true )  \"Cell pressure\" type: Real [9]
         flatTubeFinnedHX.flow_a.p[5]:VARIABLE(min = 0.0 start = flatTubeFinnedHX.flow_a.p_start_internal[5] unit = \"Pa\" fixed = true nominal = 1e5 protected = true )  \"Cell pressure\" type: Real [9]
         flatTubeFinnedHX.flow_a.p[6]:VARIABLE(min = 0.0 start = flatTubeFinnedHX.flow_a.p_start_internal[6] unit = \"Pa\" fixed = true nominal = 1e5 protected = true )  \"Cell pressure\" type: Real [9]
         flatTubeFinnedHX.flow_a.p[7]:VARIABLE(min = 0.0 start = flatTubeFinnedHX.flow_a.p_start_internal[7] unit = \"Pa\" fixed = true nominal = 1e5 protected = true )  \"Cell pressure\" type: Real [9]
         flatTubeFinnedHX.flow_a.p[8]:VARIABLE(min = 0.0 start = flatTubeFinnedHX.flow_a.p_start_internal[8] unit = \"Pa\" fixed = true nominal = 1e5 protected = true )  \"Cell pressure\" type: Real [9]
         flatTubeFinnedHX.flow_a.p[9]:VARIABLE(min = 0.0 start = flatTubeFinnedHX.flow_a.p_start_internal[9] unit = \"Pa\" fixed = true nominal = 1e5 protected = true )  \"Cell pressure\" type: Real [9]
         flatTubeFinnedHX.flow_b.h[1]:VARIABLE(start = flatTubeFinnedHX.flow_b.h_start[1] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer )  \"Cell enthalpy\" type: Real [9]
         flatTubeFinnedHX.flow_b.h[2]:VARIABLE(start = flatTubeFinnedHX.flow_b.h_start[2] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer )  \"Cell enthalpy\" type: Real [9]
         flatTubeFinnedHX.flow_b.h[3]:VARIABLE(start = flatTubeFinnedHX.flow_b.h_start[3] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer )  \"Cell enthalpy\" type: Real [9]
         flatTubeFinnedHX.flow_b.h[4]:VARIABLE(start = flatTubeFinnedHX.flow_b.h_start[4] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer )  \"Cell enthalpy\" type: Real [9]
         flatTubeFinnedHX.flow_b.h[5]:VARIABLE(start = flatTubeFinnedHX.flow_b.h_start[5] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer )  \"Cell enthalpy\" type: Real [9]
         flatTubeFinnedHX.flow_b.h[6]:VARIABLE(start = flatTubeFinnedHX.flow_b.h_start[6] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer )  \"Cell enthalpy\" type: Real [9]
         flatTubeFinnedHX.flow_b.h[7]:VARIABLE(start = flatTubeFinnedHX.flow_b.h_start[7] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer )  \"Cell enthalpy\" type: Real [9]
         flatTubeFinnedHX.flow_b.h[8]:VARIABLE(start = flatTubeFinnedHX.flow_b.h_start[8] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer )  \"Cell enthalpy\" type: Real [9]
         flatTubeFinnedHX.flow_b.h[9]:VARIABLE(start = flatTubeFinnedHX.flow_b.h_start[9] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer )  \"Cell enthalpy\" type: Real [9]
         flatTubeFinnedHX.flow_b.p[1]:VARIABLE(min = 0.0 start = flatTubeFinnedHX.flow_b.p_start[1] unit = \"Pa\" fixed = true nominal = 1e5 protected = true )  \"Cell pressure\" type: Real [9]
         flatTubeFinnedHX.flow_b.p[2]:VARIABLE(min = 0.0 start = flatTubeFinnedHX.flow_b.p_start[2] unit = \"Pa\" fixed = true nominal = 1e5 protected = true )  \"Cell pressure\" type: Real [9]
         flatTubeFinnedHX.flow_b.p[3]:VARIABLE(min = 0.0 start = flatTubeFinnedHX.flow_b.p_start[3] unit = \"Pa\" fixed = true nominal = 1e5 protected = true )  \"Cell pressure\" type: Real [9]
         flatTubeFinnedHX.flow_b.p[4]:VARIABLE(min = 0.0 start = flatTubeFinnedHX.flow_b.p_start[4] unit = \"Pa\" fixed = true nominal = 1e5 protected = true )  \"Cell pressure\" type: Real [9]
         flatTubeFinnedHX.flow_b.p[5]:VARIABLE(min = 0.0 start = flatTubeFinnedHX.flow_b.p_start[5] unit = \"Pa\" fixed = true nominal = 1e5 protected = true )  \"Cell pressure\" type: Real [9]
         flatTubeFinnedHX.flow_b.p[6]:VARIABLE(min = 0.0 start = flatTubeFinnedHX.flow_b.p_start[6] unit = \"Pa\" fixed = true nominal = 1e5 protected = true )  \"Cell pressure\" type: Real [9]
         flatTubeFinnedHX.flow_b.p[7]:VARIABLE(min = 0.0 start = flatTubeFinnedHX.flow_b.p_start[7] unit = \"Pa\" fixed = true nominal = 1e5 protected = true )  \"Cell pressure\" type: Real [9]
         flatTubeFinnedHX.flow_b.p[8]:VARIABLE(min = 0.0 start = flatTubeFinnedHX.flow_b.p_start[8] unit = \"Pa\" fixed = true nominal = 1e5 protected = true )  \"Cell pressure\" type: Real [9]
         flatTubeFinnedHX.flow_b.p[9]:VARIABLE(min = 0.0 start = flatTubeFinnedHX.flow_b.p_start[9] unit = \"Pa\" fixed = true nominal = 1e5 protected = true )  \"Cell pressure\" type: Real [9]
Notification: Performance of preBalanceInitialSystem (initialization_lambda0): time 0.06111/4.615, allocations: 31.41 MB / 1.726 GB, free: 207.7 MB / 0.8263 GB
Notification: Performance of partitionIndependentBlocks (initialization_lambda0): time 0.04495/4.66, allocations: 28.7 MB / 1.754 GB, free: 187.7 MB / 0.8263 GB
Notification: Performance of analyzeInitialSystem (initialization_lambda0): time 0.9493/5.609, allocations: 195.3 MB / 1.945 GB, free: 263.2 MB / 0.8263 GB
Notification: Performance of solveInitialSystemEqSystem (initialization_lambda0): time 0.0001375/5.609, allocations: 20.28 kB / 1.945 GB, free: 263.2 MB / 0.8263 GB
Notification: Performance of matching and sorting (n=2295) (initialization_lambda0): time 0.1324/5.742, allocations: 59.57 MB / 2.003 GB, free: 245.7 MB / 0.8263 GB
Notification: Performance of prepare postOptimizeDAE: time 8.445e-05/5.742, allocations: 36.81 kB / 2.003 GB, free: 245.7 MB / 0.8263 GB
Notification: Performance of postOpt simplifyComplexFunction (initialization): time 0.1062/5.848, allocations: 55.9 MB / 2.058 GB, free: 211.5 MB / 0.8263 GB
Notification: Performance of postOpt tearingSystem (initialization): time 0.01087/5.859, allocations: 3.491 MB / 2.061 GB, free: 208 MB / 0.8263 GB
Notification: Performance of postOpt solveSimpleEquations (initialization): time 0.0406/5.9, allocations: 5.132 MB / 2.066 GB, free: 202.9 MB / 0.8263 GB
Notification: Performance of postOpt calculateStrongComponentJacobians (initialization): time 0.04438/5.944, allocations: 63.65 MB / 2.128 GB, free: 135.6 MB / 0.8263 GB
Notification: Performance of postOpt simplifyAllExpressions (initialization): time 0.02765/5.972, allocations: 1.546 MB / 2.13 GB, free: 134.4 MB / 0.8263 GB
Notification: Performance of postOpt collapseArrayExpressions (initialization): time 0.009321/5.981, allocations: 1.35 MB / 2.131 GB, free: 133 MB / 0.8263 GB
Warning: Assuming fixed start value for the following 36 variables:
         flatTubeFinnedHX.flow_a.h[1]:VARIABLE(start = flatTubeFinnedHX.flow_a.mechanicalEquilibrium.h_start[1] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true )  \"Cell enthalpy\" type: Real [9]
         flatTubeFinnedHX.flow_a.h[2]:VARIABLE(start = flatTubeFinnedHX.flow_a.mechanicalEquilibrium.h_start[2] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true )  \"Cell enthalpy\" type: Real [9]
         flatTubeFinnedHX.flow_a.h[3]:VARIABLE(start = flatTubeFinnedHX.flow_a.mechanicalEquilibrium.h_start[3] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true )  \"Cell enthalpy\" type: Real [9]
         flatTubeFinnedHX.flow_a.h[4]:VARIABLE(start = flatTubeFinnedHX.flow_a.mechanicalEquilibrium.h_start[4] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true )  \"Cell enthalpy\" type: Real [9]
         flatTubeFinnedHX.flow_a.h[5]:VARIABLE(start = flatTubeFinnedHX.flow_a.mechanicalEquilibrium.h_start[5] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true )  \"Cell enthalpy\" type: Real [9]
         flatTubeFinnedHX.flow_a.h[6]:VARIABLE(start = flatTubeFinnedHX.flow_a.mechanicalEquilibrium.h_start[6] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true )  \"Cell enthalpy\" type: Real [9]
         flatTubeFinnedHX.flow_a.h[7]:VARIABLE(start = flatTubeFinnedHX.flow_a.mechanicalEquilibrium.h_start[7] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true )  \"Cell enthalpy\" type: Real [9]
         flatTubeFinnedHX.flow_a.h[8]:VARIABLE(start = flatTubeFinnedHX.flow_a.mechanicalEquilibrium.h_start[8] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true )  \"Cell enthalpy\" type: Real [9]
         flatTubeFinnedHX.flow_a.h[9]:VARIABLE(start = flatTubeFinnedHX.flow_a.mechanicalEquilibrium.h_start[9] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true )  \"Cell enthalpy\" type: Real [9]
         flatTubeFinnedHX.flow_a.p[1]:VARIABLE(min = 0.0 start = flatTubeFinnedHX.flow_a.p_start_internal[1] unit = \"Pa\" fixed = true nominal = 1e5 protected = true )  \"Cell pressure\" type: Real [9]
         flatTubeFinnedHX.flow_a.p[2]:VARIABLE(min = 0.0 start = flatTubeFinnedHX.flow_a.p_start_internal[2] unit = \"Pa\" fixed = true nominal = 1e5 protected = true )  \"Cell pressure\" type: Real [9]
         flatTubeFinnedHX.flow_a.p[3]:VARIABLE(min = 0.0 start = flatTubeFinnedHX.flow_a.p_start_internal[3] unit = \"Pa\" fixed = true nominal = 1e5 protected = true )  \"Cell pressure\" type: Real [9]
         flatTubeFinnedHX.flow_a.p[4]:VARIABLE(min = 0.0 start = flatTubeFinnedHX.flow_a.p_start_internal[4] unit = \"Pa\" fixed = true nominal = 1e5 protected = true )  \"Cell pressure\" type: Real [9]
         flatTubeFinnedHX.flow_a.p[5]:VARIABLE(min = 0.0 start = flatTubeFinnedHX.flow_a.p_start_internal[5] unit = \"Pa\" fixed = true nominal = 1e5 protected = true )  \"Cell pressure\" type: Real [9]
         flatTubeFinnedHX.flow_a.p[6]:VARIABLE(min = 0.0 start = flatTubeFinnedHX.flow_a.p_start_internal[6] unit = \"Pa\" fixed = true nominal = 1e5 protected = true )  \"Cell pressure\" type: Real [9]
         flatTubeFinnedHX.flow_a.p[7]:VARIABLE(min = 0.0 start = flatTubeFinnedHX.flow_a.p_start_internal[7] unit = \"Pa\" fixed = true nominal = 1e5 protected = true )  \"Cell pressure\" type: Real [9]
         flatTubeFinnedHX.flow_a.p[8]:VARIABLE(min = 0.0 start = flatTubeFinnedHX.flow_a.p_start_internal[8] unit = \"Pa\" fixed = true nominal = 1e5 protected = true )  \"Cell pressure\" type: Real [9]
         flatTubeFinnedHX.flow_a.p[9]:VARIABLE(min = 0.0 start = flatTubeFinnedHX.flow_a.p_start_internal[9] unit = \"Pa\" fixed = true nominal = 1e5 protected = true )  \"Cell pressure\" type: Real [9]
         flatTubeFinnedHX.flow_b.h[1]:VARIABLE(start = flatTubeFinnedHX.flow_b.h_start[1] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer )  \"Cell enthalpy\" type: Real [9]
         flatTubeFinnedHX.flow_b.h[2]:VARIABLE(start = flatTubeFinnedHX.flow_b.h_start[2] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer )  \"Cell enthalpy\" type: Real [9]
         flatTubeFinnedHX.flow_b.h[3]:VARIABLE(start = flatTubeFinnedHX.flow_b.h_start[3] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer )  \"Cell enthalpy\" type: Real [9]
         flatTubeFinnedHX.flow_b.h[4]:VARIABLE(start = flatTubeFinnedHX.flow_b.h_start[4] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer )  \"Cell enthalpy\" type: Real [9]
         flatTubeFinnedHX.flow_b.h[5]:VARIABLE(start = flatTubeFinnedHX.flow_b.h_start[5] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer )  \"Cell enthalpy\" type: Real [9]
         flatTubeFinnedHX.flow_b.h[6]:VARIABLE(start = flatTubeFinnedHX.flow_b.h_start[6] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer )  \"Cell enthalpy\" type: Real [9]
         flatTubeFinnedHX.flow_b.h[7]:VARIABLE(start = flatTubeFinnedHX.flow_b.h_start[7] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer )  \"Cell enthalpy\" type: Real [9]
         flatTubeFinnedHX.flow_b.h[8]:VARIABLE(start = flatTubeFinnedHX.flow_b.h_start[8] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer )  \"Cell enthalpy\" type: Real [9]
         flatTubeFinnedHX.flow_b.h[9]:VARIABLE(start = flatTubeFinnedHX.flow_b.h_start[9] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer )  \"Cell enthalpy\" type: Real [9]
         flatTubeFinnedHX.flow_b.p[1]:VARIABLE(min = 0.0 start = flatTubeFinnedHX.flow_b.p_start[1] unit = \"Pa\" fixed = true nominal = 1e5 protected = true )  \"Cell pressure\" type: Real [9]
         flatTubeFinnedHX.flow_b.p[2]:VARIABLE(min = 0.0 start = flatTubeFinnedHX.flow_b.p_start[2] unit = \"Pa\" fixed = true nominal = 1e5 protected = true )  \"Cell pressure\" type: Real [9]
         flatTubeFinnedHX.flow_b.p[3]:VARIABLE(min = 0.0 start = flatTubeFinnedHX.flow_b.p_start[3] unit = \"Pa\" fixed = true nominal = 1e5 protected = true )  \"Cell pressure\" type: Real [9]
         flatTubeFinnedHX.flow_b.p[4]:VARIABLE(min = 0.0 start = flatTubeFinnedHX.flow_b.p_start[4] unit = \"Pa\" fixed = true nominal = 1e5 protected = true )  \"Cell pressure\" type: Real [9]
         flatTubeFinnedHX.flow_b.p[5]:VARIABLE(min = 0.0 start = flatTubeFinnedHX.flow_b.p_start[5] unit = \"Pa\" fixed = true nominal = 1e5 protected = true )  \"Cell pressure\" type: Real [9]
         flatTubeFinnedHX.flow_b.p[6]:VARIABLE(min = 0.0 start = flatTubeFinnedHX.flow_b.p_start[6] unit = \"Pa\" fixed = true nominal = 1e5 protected = true )  \"Cell pressure\" type: Real [9]
         flatTubeFinnedHX.flow_b.p[7]:VARIABLE(min = 0.0 start = flatTubeFinnedHX.flow_b.p_start[7] unit = \"Pa\" fixed = true nominal = 1e5 protected = true )  \"Cell pressure\" type: Real [9]
         flatTubeFinnedHX.flow_b.p[8]:VARIABLE(min = 0.0 start = flatTubeFinnedHX.flow_b.p_start[8] unit = \"Pa\" fixed = true nominal = 1e5 protected = true )  \"Cell pressure\" type: Real [9]
         flatTubeFinnedHX.flow_b.p[9]:VARIABLE(min = 0.0 start = flatTubeFinnedHX.flow_b.p_start[9] unit = \"Pa\" fixed = true nominal = 1e5 protected = true )  \"Cell pressure\" type: Real [9]
Notification: Model statistics after passing the back-end for initialization:
 * Number of independent subsystems: 311
 * 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 (2241):
 * Single equations (assignments): 2202
 * Array equations: 0
 * Algorithm blocks: 0
 * Record equations: 0
 * When equations: 0
 * If-equations: 0
 * Equation systems (not torn): 0
 * Torn equation systems: 39
 * Mixed (continuous/discrete) equation systems: 0
Notification: Torn system details for strict tearing set:
 * Linear torn systems (#iteration vars, #inner vars, density): 39 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%), (1,6,100.0%), (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%)}
 * Non-linear torn systems (#iteration vars, #inner vars): 0 systems
Notification: Performance of prepare postOptimizeDAE: time 0.0189/6, allocations: 1.381 MB / 2.132 GB, free: 131.7 MB / 0.8263 GB
Notification: Performance of postOpt lateInlineFunction (simulation): time 0.01411/6.014, allocations: 1.568 MB / 2.134 GB, free: 130.2 MB / 0.8263 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 2059 equation(s) and 2024 variable(s).
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia main/VLEFluid/MixtureCompatible/VLEFluid_ph.mo:65:5-70:23:writable] Error: (flatTubeFinnedHX.flow_a.fluid[7].VLE.d_l, flatTubeFinnedHX.flow_a.summary.fluid.h_bub[7], flatTubeFinnedHX.flow_a.fluid[7].VLE.p_l, flatTubeFinnedHX.flow_a.fluid[7].VLE.s_l, flatTubeFinnedHX.flow_a.summary.fluid.T_sat[7], _, flatTubeFinnedHX.flow_a.fluid[7].VLE.d_v, flatTubeFinnedHX.flow_a.summary.fluid.h_dew[7], flatTubeFinnedHX.flow_a.fluid[7].VLE.p_v, flatTubeFinnedHX.flow_a.fluid[7].VLE.s_v, flatTubeFinnedHX.flow_a.fluid[7].VLE.T_v, _) = ($cse232, $cse233, $cse234, $cse235, $cse236, $cse237, $cse238, $cse239, $cse240, $cse241, $cse242, $cse243) has size 10 but 8 variables ($cse88, $cse89, $cse90, $cse91, flatTubeFinnedHX.flow_a.fluid[1].transp.Pr, flatTubeFinnedHX.flow_a.fluid[1].transp.lambda, flatTubeFinnedHX.flow_a.fluid[1].transp.eta, flatTubeFinnedHX.flow_a.fluid[1].transp.sigma)
Error: Internal error Transformation Module PFPlusExt index Reduction Method Pantelides failed!
Notification: Performance of <failed> postOpt wrapFunctionCalls (simulation): time 0.07768/6.092, allocations: 36.99 MB / 2.17 GB, free: 93.47 MB / 0.8263 GB
Error: post-optimization module wrapFunctionCalls (simulation) failed.
"
[Timeout remaining time 794]
[Calling sys.exit(0), Time elapsed: 10.475943639874458]
Failed to read output from testmodel.py, exit status != 0:
6.273647852241993 6.629355543 5.690714398
Calling exit ...
<OMPython.OMCSessionZMQ object at 0x7ff188c84fd0>