Running: ./testmodel.py --libraries=/home/hudson/saved_omc/libraries/.openmodelica/libraries --ompython_omhome=/usr ClaRa_dev_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 0.006258/0.006258, allocations: 1.439 MB / 21.3 MB, free: 3.254 MB / 18.57 MB
"
[Timeout remaining time 180]
loadFile("/home/hudson/saved_omc/libraries/.openmodelica/libraries/ModelicaServices 4.1.0+maint.om/package.mo", uses=false) [Timeout 180]
"Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/ModelicaServices 4.1.0+maint.om/package.mo): time 0.00081/0.00081, allocations: 94.44 kB / 24.91 MB, free: 7.27 MB / 18.57 MB
"
[Timeout remaining time 180]
loadFile("/home/hudson/saved_omc/libraries/.openmodelica/libraries/Complex 4.1.0+maint.om/package.mo", uses=false) [Timeout 180]
"Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/Complex 4.1.0+maint.om/package.mo): time 0.0008022/0.0008022, allocations: 164.9 kB / 28.62 MB, free: 4.453 MB / 18.57 MB
"
[Timeout remaining time 180]
loadFile("/home/hudson/saved_omc/libraries/.openmodelica/libraries/Modelica 4.1.0+maint.om/package.mo", uses=false) [Timeout 180]
"Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/Modelica 4.1.0+maint.om/package.mo): time 0.8648/0.8648, allocations: 177.1 MB / 209.4 MB, free: 2.973 MB / 186.7 MB
"
[Timeout remaining time 179]
loadFile("/home/hudson/saved_omc/libraries/.openmodelica/libraries/ClaRa main/package.mo", uses=false) [Timeout 180]
"Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/ClaRa main/package.mo): time 0.7176/0.7176, allocations: 102.4 MB / 368.7 MB, free: 1.449 MB / 330.8 MB
"
[Timeout remaining time 179]
Using package ClaRa with version 1.9.0 (/home/hudson/saved_omc/libraries/.openmodelica/libraries/ClaRa main/package.mo)
Using package Modelica with version 4.1.0 (/home/hudson/saved_omc/libraries/.openmodelica/libraries/Modelica 4.1.0+maint.om/package.mo)
Using package Complex with version 4.1.0 (/home/hudson/saved_omc/libraries/.openmodelica/libraries/Complex 4.1.0+maint.om/package.mo)
Using package ModelicaServices with version 4.1.0 (/home/hudson/saved_omc/libraries/.openmodelica/libraries/ModelicaServices 4.1.0+maint.om/package.mo)
Using package SMArtInt with version 0.5.2 (/home/hudson/saved_omc/libraries/.openmodelica/libraries/SMArtInt main/package.mo)
Running command: translateModel(ClaRa.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_dev_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_dev_ClaRa.Components.HeatExchangers.Check.Test_FlatTubeFinnedHEXvle2gas_L4") [Timeout 800]
"Notification: Performance of FrontEnd - loaded program: time 1.403e-06/1.403e-06, allocations: 0 / 0.5374 GB, free: 39.73 MB / 490.8 MB
Notification: Performance of FrontEnd - Absyn->SCode: time 2.566e-05/2.706e-05, allocations: 5.234 kB / 0.5374 GB, free: 39.73 MB / 490.8 MB
Notification: TILMedia requested package Modelica of version 4.0.0. Modelica 4.1.0 is used instead which states that it is fully compatible without conversion script needed.
Notification: Automatically loaded package TILMedia 1.9.0 ClaRa due to usage.
Notification: Performance of NFInst.instantiate(ClaRa.Components.HeatExchangers.Check.Test_FlatTubeFinnedHEXvle2gas_L4): time 0.1196/0.1196, allocations: 63.02 MB / 0.599 GB, free: 12.94 MB / 0.4949 GB
Notification: Performance of NFInst.instExpressions: time 0.03634/0.156, allocations: 30.77 MB / 0.629 GB, free: 14.07 MB / 0.5262 GB
Notification: Performance of NFInst.updateImplicitVariability: time 0.003342/0.1593, allocations: 95.38 kB / 0.6291 GB, free: 13.98 MB / 0.5262 GB
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/ClaRa main/SimCenter.mo:71:5-72:35:writable] Warning: Connector cycleSumPort is not balanced: The number of potential variables (0) is not equal to the number of flow variables (4).
Notification: Performance of NFTyping.typeComponents: time 0.004652/0.164, allocations: 2.582 MB / 0.6316 GB, free: 11.39 MB / 0.5262 GB
Notification: Performance of NFTyping.typeBindings: time 0.006562/0.1705, allocations: 3.711 MB / 0.6352 GB, free: 7.656 MB / 0.5262 GB
Notification: Performance of NFTyping.typeClassSections: time 0.0117/0.1822, allocations: 5.64 MB / 0.6407 GB, free: 1.996 MB / 0.5262 GB
Notification: Performance of NFFlatten.flatten: time 0.01937/0.2016, allocations: 21.66 MB / 0.6619 GB, free: 12.29 MB / 0.5574 GB
Notification: Performance of NFFlatten.resolveConnections: time 0.01118/0.2128, allocations: 8.087 MB / 0.6698 GB, free: 4.098 MB / 0.5574 GB
Notification: Performance of NFEvalConstants.evaluate: time 0.02215/0.2349, allocations: 11.45 MB / 0.681 GB, free: 8.633 MB / 0.573 GB
Notification: Performance of NFSimplifyModel.simplify: time 0.01755/0.2525, allocations: 12.91 MB / 0.6936 GB, free: 11.7 MB / 0.5887 GB
Notification: Performance of NFPackage.collectConstants: time 0.008403/0.2609, allocations: 3.188 MB / 0.6967 GB, free: 8.516 MB / 0.5887 GB
Notification: Performance of NFFlatten.collectFunctions: time 0.01673/0.2776, allocations: 7.067 MB / 0.7036 GB, free: 1.438 MB / 0.5887 GB
Notification: Performance of NFScalarize.scalarize: time 0.01353/0.2911, allocations: 11.81 MB / 0.7151 GB, free: 5.602 MB / 0.6043 GB
Notification: Performance of NFVerifyModel.verify: time 0.0169/0.308, allocations: 9.546 MB / 0.7244 GB, free: 12.04 MB / 0.6199 GB
Notification: Performance of NFConvertDAE.convert: time 0.375/0.683, allocations: 47.9 MB / 0.7712 GB, free: 69.1 MB / 0.6512 GB
Notification: Performance of FrontEnd - DAE generated: time 8.727e-06/0.683, allocations: 0 / 0.7712 GB, free: 69.1 MB / 0.6512 GB
Notification: Performance of FrontEnd: time 4.468e-06/0.683, allocations: 1.125 kB / 0.7712 GB, free: 69.1 MB / 0.6512 GB
Notification: Performance of Transformations before backend: time 0.001491/0.6845, allocations: 0 / 0.7712 GB, free: 69.1 MB / 0.6512 GB
Notification: Model statistics after passing the front-end and creating the data structures used by the back-end:
 * Number of equations: 3282
 * Number of variables: 3282
Notification: Performance of Generate backend data structure: time 0.08235/0.7669, allocations: 29.4 MB / 0.7999 GB, free: 61.07 MB / 0.6512 GB
Notification: Performance of prepare preOptimizeDAE: time 4.633e-05/0.7669, allocations: 16.86 kB / 0.8 GB, free: 61.07 MB / 0.6512 GB
Notification: Performance of preOpt normalInlineFunction (simulation): time 0.01149/0.7784, allocations: 2.073 MB / 0.802 GB, free: 59.98 MB / 0.6512 GB
Notification: Performance of preOpt evaluateParameters (simulation): time 0.04328/0.8217, allocations: 28.37 MB / 0.8297 GB, free: 56.73 MB / 0.6512 GB
Notification: Performance of preOpt simplifyIfEquations (simulation): time 0.0005134/0.8222, allocations: 0.5709 MB / 0.8302 GB, free: 56.6 MB / 0.6512 GB
Notification: Performance of preOpt expandDerOperator (simulation): time 0.007457/0.8297, allocations: 0.8285 MB / 0.8311 GB, free: 56.32 MB / 0.6512 GB
Notification: Performance of preOpt clockPartitioning (simulation): time 0.06342/0.8931, allocations: 53.84 MB / 0.8836 GB, free: 14.14 MB / 0.6512 GB
Notification: Performance of preOpt findStateOrder (simulation): time 0.0001466/0.8932, allocations: 41.56 kB / 0.8837 GB, free: 14.12 MB / 0.6512 GB
Notification: Performance of preOpt replaceEdgeChange (simulation): time 0.001768/0.895, allocations: 393.5 kB / 0.884 GB, free: 13.76 MB / 0.6512 GB
Notification: Performance of preOpt inlineArrayEqn (simulation): time 0.001095/0.8961, allocations: 1.902 MB / 0.8859 GB, free: 11.86 MB / 0.6512 GB
Notification: Performance of preOpt removeEqualRHS (simulation): time 0.09669/0.9928, allocations: 79.42 MB / 0.9635 GB, free: 12.57 MB / 0.7293 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 0.5215/1.514, allocations: 122.8 MB / 1.083 GB, free: 274.8 MB / 0.823 GB
Notification: Performance of preOpt comSubExp (simulation): time 0.05196/1.566, allocations: 36.08 MB / 1.119 GB, free: 263.1 MB / 0.823 GB
Notification: Performance of preOpt resolveLoops (simulation): time 0.02725/1.594, allocations: 25.58 MB / 1.144 GB, free: 252.3 MB / 0.823 GB
Notification: Performance of preOpt evalFunc (simulation): time 0.003119/1.597, allocations: 0.8012 MB / 1.144 GB, free: 252.2 MB / 0.823 GB
Notification: Performance of preOpt encapsulateWhenConditions (simulation): time 0.0001335/1.597, allocations: 200.6 kB / 1.145 GB, free: 252 MB / 0.823 GB
Notification: Performance of pre-optimization done (n=1780): time 1.749e-05/1.597, allocations: 0 / 1.145 GB, free: 252 MB / 0.823 GB
Notification: Performance of matching and sorting (n=1780): time 0.1333/1.73, allocations: 86.17 MB / 1.229 GB, free: 170.9 MB / 0.823 GB
Notification: Performance of inlineWhenForInitialization (initialization): time 0.0001896/1.73, allocations: 0.962 MB / 1.23 GB, free: 169.8 MB / 0.823 GB
Notification: Performance of selectInitializationVariablesDAE (initialization): time 0.02397/1.754, allocations: 14.72 MB / 1.244 GB, free: 155.4 MB / 0.823 GB
Notification: Performance of collectPreVariables (initialization): time 0.005869/1.76, allocations: 273.7 kB / 1.244 GB, free: 155.1 MB / 0.823 GB
Notification: Performance of collectInitialEqns (initialization): time 0.005028/1.765, allocations: 6.047 MB / 1.25 GB, free: 150.1 MB / 0.823 GB
Notification: Performance of collectInitialBindings (initialization): time 0.01034/1.775, allocations: 6.267 MB / 1.256 GB, free: 144.2 MB / 0.823 GB
Notification: Performance of simplifyInitialFunctions (initialization): time 0.01871/1.794, allocations: 4.253 MB / 1.26 GB, free: 140 MB / 0.823 GB
Notification: Performance of setup shared object (initialization): time 4.073e-05/1.794, allocations: 310.2 kB / 1.261 GB, free: 139.7 MB / 0.823 GB
Notification: Performance of preBalanceInitialSystem (initialization): time 0.0285/1.823, allocations: 25.9 MB / 1.286 GB, free: 113.7 MB / 0.823 GB
Notification: Performance of partitionIndependentBlocks (initialization): time 0.03306/1.856, allocations: 29.24 MB / 1.315 GB, free: 83.42 MB / 0.823 GB
Notification: Performance of analyzeInitialSystem (initialization): time 0.6452/2.501, allocations: 197.5 MB / 1.507 GB, free: 224.3 MB / 0.823 GB
Notification: Performance of solveInitialSystemEqSystem (initialization): time 9.908e-05/2.501, allocations: 20 kB / 1.507 GB, free: 224.3 MB / 0.823 GB
Notification: Performance of matching and sorting (n=2295) (initialization): time 0.0922/2.593, allocations: 60.77 MB / 1.567 GB, free: 164.2 MB / 0.823 GB
Notification: Performance of prepare postOptimizeDAE: time 7.061e-05/2.593, allocations: 39.94 kB / 1.567 GB, free: 164.2 MB / 0.823 GB
Notification: Performance of postOpt simplifyComplexFunction (initialization): time 0.0777/2.671, allocations: 57.11 MB / 1.623 GB, free: 107 MB / 0.823 GB
Notification: Performance of postOpt tearingSystem (initialization): time 0.006165/2.677, allocations: 3.495 MB / 1.626 GB, free: 103.3 MB / 0.823 GB
Notification: Performance of postOpt solveSimpleEquations (initialization): time 0.0217/2.699, allocations: 5.203 MB / 1.631 GB, free: 98.12 MB / 0.823 GB
Notification: Performance of postOpt calculateStrongComponentJacobians (initialization): time 0.02603/2.725, allocations: 63.67 MB / 1.693 GB, free: 30.88 MB / 0.823 GB
Notification: Performance of postOpt simplifyAllExpressions (initialization): time 0.01763/2.743, allocations: 1.665 MB / 1.695 GB, free: 29.99 MB / 0.823 GB
Notification: Performance of postOpt collapseArrayExpressions (initialization): time 0.006082/2.749, allocations: 1.382 MB / 1.696 GB, free: 28.61 MB / 0.823 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 0.4051/3.154, allocations: 31.41 MB / 1.727 GB, free: 271 MB / 0.823 GB
Notification: Performance of partitionIndependentBlocks (initialization_lambda0): time 0.03736/3.191, allocations: 28.69 MB / 1.755 GB, free: 263.8 MB / 0.823 GB
Notification: Performance of analyzeInitialSystem (initialization_lambda0): time 0.2843/3.475, allocations: 195.3 MB / 1.946 GB, free: 108.7 MB / 0.823 GB
Notification: Performance of solveInitialSystemEqSystem (initialization_lambda0): time 9.053e-05/3.475, allocations: 20 kB / 1.946 GB, free: 108.7 MB / 0.823 GB
Notification: Performance of matching and sorting (n=2295) (initialization_lambda0): time 0.08468/3.56, allocations: 59.56 MB / 2.004 GB, free: 49.82 MB / 0.823 GB
Notification: Performance of prepare postOptimizeDAE: time 5.554e-05/3.56, allocations: 40.72 kB / 2.004 GB, free: 49.79 MB / 0.823 GB
Notification: Performance of postOpt simplifyComplexFunction (initialization): time 0.4179/3.978, allocations: 55.9 MB / 2.058 GB, free: 259.3 MB / 0.823 GB
Notification: Performance of postOpt tearingSystem (initialization): time 0.00613/3.984, allocations: 3.49 MB / 2.062 GB, free: 258.2 MB / 0.823 GB
Notification: Performance of postOpt solveSimpleEquations (initialization): time 0.0218/4.006, allocations: 5.131 MB / 2.067 GB, free: 258 MB / 0.823 GB
Notification: Performance of postOpt calculateStrongComponentJacobians (initialization): time 0.02718/4.033, allocations: 63.66 MB / 2.129 GB, free: 204.1 MB / 0.823 GB
Notification: Performance of postOpt simplifyAllExpressions (initialization): time 0.01707/4.05, allocations: 1.541 MB / 2.131 GB, free: 203.8 MB / 0.823 GB
Notification: Performance of postOpt collapseArrayExpressions (initialization): time 0.006631/4.057, allocations: 1.349 MB / 2.132 GB, free: 203.7 MB / 0.823 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 0.008509/4.065, allocations: 1.38 MB / 2.133 GB, free: 202.8 MB / 0.823 GB
Notification: Performance of postOpt lateInlineFunction (simulation): time 0.005303/4.071, allocations: 1.57 MB / 2.135 GB, free: 202.6 MB / 0.823 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 0.03434/4.105, allocations: 36.99 MB / 2.171 GB, free: 175.7 MB / 0.823 GB
Error: post-optimization module wrapFunctionCalls (simulation) failed.
"
[Timeout remaining time 796]
[Calling sys.exit(0), Time elapsed: 6.919202893972397]
Failed to read output from testmodel.py, exit status != 0:
4.2497094636783 4.255615126 3.570996222
Calling exit ...
<OMPython.OMCSessionZMQ object at 0x74431d7c2240>