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 0.01562/0.01562, allocations: 1.745 MB / 21.38 MB, free: 464 kB / 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 0.001598/0.001598, allocations: 103.6 kB / 24.97 MB, free: 2.035 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 0.002127/0.002127, allocations: 211.6 kB / 28.68 MB, free: 3.324 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 1.421/1.421, allocations: 230.6 MB / 262.9 MB, free: 5.797 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 1.051/1.051, allocations: 130.7 MB / 450.4 MB, free: 6.379 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: "" <> buildModelFMU(ClaRa.Examples.VapourCycle_01,fileNamePrefix="ClaRa_ClaRa_Examples_VapourCycle_01",fmuType="cs",version="2.0",platforms={"static"})
"" <> buildModelFMU(ClaRa.Examples.VapourCycle_01,fileNamePrefix="ClaRa_ClaRa_Examples_VapourCycle_01",fmuType="cs",version="2.0",platforms={"static"}) [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 0.06293/0.06293, allocations: 20.6 MB / 0.6362 GB, free: 5.09 MB / 462.1 MB
Notification: Performance of FrontEnd - Absyn->SCode: time 0.1646/0.2276, allocations: 81.91 MB / 0.7162 GB, free: 3.09 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 0.5133/0.7409, allocations: 70.65 MB / 0.7852 GB, free: 4.18 MB / 0.5607 GB
Notification: Performance of NFInst.instExpressions: time 0.08336/0.8243, allocations: 43.91 MB / 0.8281 GB, free: 324 kB / 0.5919 GB
Notification: Performance of NFInst.updateImplicitVariability: time 0.0139/0.8382, allocations: 250.2 kB / 0.8283 GB, free: 72 kB / 0.5919 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 0.01631/0.8545, allocations: 5.442 MB / 0.8336 GB, free: 10.62 MB / 0.6075 GB
Notification: Performance of NFTyping.typeBindings: time 0.02903/0.8835, allocations: 9.715 MB / 0.8431 GB, free: 0.9336 MB / 0.6075 GB
Notification: Performance of NFTyping.typeClassSections: time 0.02782/0.9113, allocations: 10.24 MB / 0.8531 GB, free: 6.742 MB / 0.6232 GB
Notification: Performance of NFFlatten.flatten: time 0.05518/0.9665, allocations: 42.03 MB / 0.8941 GB, free: 12.65 MB / 0.67 GB
Notification: Performance of NFFlatten.resolveConnections: time 0.02394/0.9904, allocations: 13.38 MB / 0.9072 GB, free: 15.16 MB / 0.6857 GB
Notification: Performance of NFEvalConstants.evaluate: time 0.03193/1.022, allocations: 16.4 MB / 0.9232 GB, free: 14.72 MB / 0.7013 GB
Notification: Performance of NFSimplifyModel.simplify: time 0.03595/1.058, allocations: 22.37 MB / 0.9451 GB, free: 8.293 MB / 0.7169 GB
Notification: Performance of NFPackage.collectConstants: time 0.01468/1.073, allocations: 4.535 MB / 0.9495 GB, free: 3.758 MB / 0.7169 GB
Notification: Performance of NFFlatten.collectFunctions: time 0.02773/1.101, allocations: 9.344 MB / 0.9586 GB, free: 10.41 MB / 0.7325 GB
Notification: Performance of NFScalarize.scalarize: time 0.02699/1.128, allocations: 16.95 MB / 0.9752 GB, free: 9.43 MB / 0.7482 GB
Notification: Performance of NFVerifyModel.verify: time 0.04189/1.17, allocations: 16.55 MB / 0.9913 GB, free: 8.816 MB / 0.7638 GB
Notification: Performance of NFConvertDAE.convert: time 0.09685/1.266, allocations: 66.51 MB / 1.056 GB, free: 6.105 MB / 0.8263 GB
Notification: Performance of FrontEnd - DAE generated: time 7.004e-06/1.266, allocations: 0 / 1.056 GB, free: 6.105 MB / 0.8263 GB
Notification: Performance of FrontEnd: time 1.954e-06/1.266, allocations: 2.656 kB / 1.056 GB, free: 6.105 MB / 0.8263 GB
Notification: Performance of Transformations before backend: time 0.001888/1.268, allocations: 0 / 1.056 GB, free: 6.105 MB / 0.8263 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 0.7045/1.973, allocations: 42.78 MB / 1.098 GB, free: 302.9 MB / 0.8264 GB
Notification: Performance of prepare preOptimizeDAE: time 4.845e-05/1.973, allocations: 8.031 kB / 1.098 GB, free: 302.9 MB / 0.8264 GB
Notification: Performance of preOpt introduceOutputRealDerivatives (simulation): time 0.000452/1.973, allocations: 431.5 kB / 1.098 GB, free: 302.5 MB / 0.8264 GB
Notification: Performance of preOpt introduceOutputAliases (simulation): time 0.01377/1.987, allocations: 2.743 MB / 1.101 GB, free: 299.8 MB / 0.8264 GB
Notification: Performance of preOpt normalInlineFunction (simulation): time 0.02249/2.01, allocations: 3.564 MB / 1.105 GB, free: 296.2 MB / 0.8264 GB
Notification: Performance of preOpt evaluateParameters (simulation): time 0.0746/2.084, allocations: 37.77 MB / 1.142 GB, free: 258.8 MB / 0.8264 GB
Notification: Performance of preOpt simplifyIfEquations (simulation): time 0.001359/2.086, allocations: 1.08 MB / 1.143 GB, free: 257.7 MB / 0.8264 GB
Notification: Performance of preOpt expandDerOperator (simulation): time 0.01458/2.1, allocations: 1.437 MB / 1.144 GB, free: 256.3 MB / 0.8264 GB
Notification: Performance of preOpt clockPartitioning (simulation): time 0.1399/2.24, allocations: 75.41 MB / 1.218 GB, free: 174.7 MB / 0.8264 GB
Notification: Performance of preOpt findStateOrder (simulation): time 0.0007636/2.241, allocations: 107 kB / 1.218 GB, free: 174.6 MB / 0.8264 GB
Notification: Performance of preOpt replaceEdgeChange (simulation): time 0.01257/2.253, allocations: 0.6823 MB / 1.218 GB, free: 174 MB / 0.8264 GB
Notification: Performance of preOpt inlineArrayEqn (simulation): time 0.002562/2.256, allocations: 2.736 MB / 1.221 GB, free: 171.3 MB / 0.8264 GB
Notification: Performance of preOpt removeEqualRHS (simulation): time 0.15/2.406, allocations: 95.2 MB / 1.314 GB, free: 76.02 MB / 0.8264 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 0.7746/3.181, allocations: 199.3 MB / 1.509 GB, free: 175.6 MB / 0.8264 GB
Notification: Performance of preOpt comSubExp (simulation): time 0.09854/3.279, allocations: 51.84 MB / 1.559 GB, free: 140.3 MB / 0.8264 GB
Notification: Performance of preOpt resolveLoops (simulation): time 0.03916/3.318, allocations: 30.72 MB / 1.589 GB, free: 109.4 MB / 0.8264 GB
Notification: Performance of preOpt evalFunc (simulation): time 0.005579/3.324, allocations: 1.063 MB / 1.59 GB, free: 108.4 MB / 0.8264 GB
Notification: Performance of preOpt encapsulateWhenConditions (simulation): time 0.0003357/3.324, allocations: 297.1 kB / 1.591 GB, free: 108.1 MB / 0.8264 GB
Notification: Performance of pre-optimization done (n=3004): time 3.247e-05/3.324, allocations: 0 / 1.591 GB, free: 108.1 MB / 0.8264 GB
Notification: Performance of matching and sorting (n=3005): time 1.133/4.458, allocations: 323.9 MB / 1.907 GB, free: 105.6 MB / 0.8264 GB
Notification: Performance of inlineWhenForInitialization (initialization): time 0.0007139/4.458, allocations: 2.381 MB / 1.909 GB, free: 102.7 MB / 0.8264 GB
Notification: Performance of selectInitializationVariablesDAE (initialization): time 0.05134/4.51, allocations: 24.48 MB / 1.933 GB, free: 80.01 MB / 0.8264 GB
Notification: Performance of collectPreVariables (initialization): time 0.007606/4.517, allocations: 365.7 kB / 1.934 GB, free: 79.65 MB / 0.8264 GB
Notification: Performance of collectInitialEqns (initialization): time 0.01061/4.528, allocations: 10.75 MB / 1.944 GB, free: 69.74 MB / 0.8264 GB
Notification: Performance of collectInitialBindings (initialization): time 0.0145/4.542, allocations: 10.57 MB / 1.954 GB, free: 59.34 MB / 0.8264 GB
Notification: Performance of simplifyInitialFunctions (initialization): time 0.02912/4.571, allocations: 6.698 MB / 1.961 GB, free: 52.62 MB / 0.8264 GB
Notification: Performance of setup shared object (initialization): time 5.381e-05/4.571, allocations: 309.1 kB / 1.961 GB, free: 52.32 MB / 0.8264 GB
Notification: Performance of preBalanceInitialSystem (initialization): time 0.0449/4.616, allocations: 32.91 MB / 1.993 GB, free: 19.39 MB / 0.8264 GB
Notification: Performance of partitionIndependentBlocks (initialization): time 0.4017/5.018, allocations: 40.39 MB / 2.033 GB, free: 247.8 MB / 0.8264 GB
Notification: Performance of analyzeInitialSystem (initialization): time 0.6882/5.706, allocations: 248.8 MB / 2.276 GB, free: 29.04 MB / 0.8264 GB
Notification: Performance of solveInitialSystemEqSystem (initialization): time 0.0002306/5.707, allocations: 48 kB / 2.276 GB, free: 29 MB / 0.8264 GB
Notification: Performance of matching and sorting (n=3948) (initialization): time 0.5045/6.211, allocations: 81.16 MB / 2.355 GB, free: 245.4 MB / 0.842 GB
Notification: Performance of prepare postOptimizeDAE: time 0.0001765/6.211, allocations: 79.94 kB / 2.355 GB, free: 245.4 MB / 0.842 GB
Notification: Performance of postOpt simplifyComplexFunction (initialization): time 0.1269/6.338, allocations: 73.06 MB / 2.426 GB, free: 199.8 MB / 0.842 GB
Notification: Performance of postOpt tearingSystem (initialization): time 0.01536/6.353, allocations: 5.28 MB / 2.432 GB, free: 194.5 MB / 0.842 GB
Notification: Performance of postOpt solveSimpleEquations (initialization): time 0.04487/6.398, allocations: 8.335 MB / 2.44 GB, free: 186.2 MB / 0.842 GB
Notification: Performance of postOpt calculateStrongComponentJacobians (initialization): time 0.06894/6.467, allocations: 105 MB / 2.542 GB, free: 74.59 MB / 0.842 GB
Notification: Performance of postOpt simplifyAllExpressions (initialization): time 0.03172/6.499, allocations: 1.303 MB / 2.544 GB, free: 73.39 MB / 0.842 GB
Notification: Performance of postOpt collapseArrayExpressions (initialization): time 0.01166/6.511, allocations: 2.124 MB / 2.546 GB, free: 71.26 MB / 0.842 GB
Warning: Assuming fixed start value for the following 65 variables:
         tube.h[1]:VARIABLE(start = tube.mechanicalEquilibrium.h_start[1] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true )  \"Cell enthalpy\" type: Real [3]
         tube.h[2]:VARIABLE(start = tube.mechanicalEquilibrium.h_start[2] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true )  \"Cell enthalpy\" type: Real [3]
         tube.h[3]:VARIABLE(start = tube.mechanicalEquilibrium.h_start[3] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true )  \"Cell enthalpy\" type: Real [3]
         tube.p[1]:VARIABLE(min = 0.0 start = tube.p_start_internal[1] unit = \"Pa\" fixed = true nominal = 1e5 protected = true )  \"Cell pressure\" type: Real [3]
         tube.p[2]:VARIABLE(min = 0.0 start = tube.p_start_internal[2] unit = \"Pa\" fixed = true nominal = 1e5 protected = true )  \"Cell pressure\" type: Real [3]
         tube.p[3]:VARIABLE(min = 0.0 start = tube.p_start_internal[3] unit = \"Pa\" fixed = true nominal = 1e5 protected = true )  \"Cell pressure\" type: Real [3]
         plateHEX.flow_a.h[1]:VARIABLE(start = plateHEX.flow_a.mechanicalEquilibrium.h_start[1] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true )  \"Cell enthalpy\" type: Real [5]
         plateHEX.flow_a.h[2]:VARIABLE(start = plateHEX.flow_a.mechanicalEquilibrium.h_start[2] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true )  \"Cell enthalpy\" type: Real [5]
         plateHEX.flow_a.h[3]:VARIABLE(start = plateHEX.flow_a.mechanicalEquilibrium.h_start[3] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true )  \"Cell enthalpy\" type: Real [5]
         plateHEX.flow_a.h[4]:VARIABLE(start = plateHEX.flow_a.mechanicalEquilibrium.h_start[4] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true )  \"Cell enthalpy\" type: Real [5]
         plateHEX.flow_a.h[5]:VARIABLE(start = plateHEX.flow_a.mechanicalEquilibrium.h_start[5] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true )  \"Cell enthalpy\" type: Real [5]
         plateHEX.flow_a.p[1]:VARIABLE(min = 0.0 start = plateHEX.flow_a.p_start_internal[1] unit = \"Pa\" fixed = true nominal = 1e5 protected = true )  \"Cell pressure\" type: Real [5]
         plateHEX.flow_a.p[2]:VARIABLE(min = 0.0 start = plateHEX.flow_a.p_start_internal[2] unit = \"Pa\" fixed = true nominal = 1e5 protected = true )  \"Cell pressure\" type: Real [5]
         plateHEX.flow_a.p[3]:VARIABLE(min = 0.0 start = plateHEX.flow_a.p_start_internal[3] unit = \"Pa\" fixed = true nominal = 1e5 protected = true )  \"Cell pressure\" type: Real [5]
         plateHEX.flow_a.p[4]:VARIABLE(min = 0.0 start = plateHEX.flow_a.p_start_internal[4] unit = \"Pa\" fixed = true nominal = 1e5 protected = true )  \"Cell pressure\" type: Real [5]
         plateHEX.flow_a.p[5]:VARIABLE(min = 0.0 start = plateHEX.flow_a.p_start_internal[5] unit = \"Pa\" fixed = true nominal = 1e5 protected = true )  \"Cell pressure\" type: Real [5]
         plateHEX.flow_b.h[1]:VARIABLE(start = plateHEX.flow_b.mechanicalEquilibrium.h_start[1] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true )  \"Cell enthalpy\" type: Real [5]
         plateHEX.flow_b.h[2]:VARIABLE(start = plateHEX.flow_b.mechanicalEquilibrium.h_start[2] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true )  \"Cell enthalpy\" type: Real [5]
         plateHEX.flow_b.h[3]:VARIABLE(start = plateHEX.flow_b.mechanicalEquilibrium.h_start[3] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true )  \"Cell enthalpy\" type: Real [5]
         plateHEX.flow_b.h[4]:VARIABLE(start = plateHEX.flow_b.mechanicalEquilibrium.h_start[4] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true )  \"Cell enthalpy\" type: Real [5]
         plateHEX.flow_b.h[5]:VARIABLE(start = plateHEX.flow_b.mechanicalEquilibrium.h_start[5] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true )  \"Cell enthalpy\" type: Real [5]
         plateHEX.flow_b.p[1]:VARIABLE(min = 0.0 start = plateHEX.flow_b.p_start_internal[1] unit = \"Pa\" fixed = true nominal = 1e5 protected = true )  \"Cell pressure\" type: Real [5]
         plateHEX.flow_b.p[2]:VARIABLE(min = 0.0 start = plateHEX.flow_b.p_start_internal[2] unit = \"Pa\" fixed = true nominal = 1e5 protected = true )  \"Cell pressure\" type: Real [5]
         plateHEX.flow_b.p[3]:VARIABLE(min = 0.0 start = plateHEX.flow_b.p_start_internal[3] unit = \"Pa\" fixed = true nominal = 1e5 protected = true )  \"Cell pressure\" type: Real [5]
         plateHEX.flow_b.p[4]:VARIABLE(min = 0.0 start = plateHEX.flow_b.p_start_internal[4] unit = \"Pa\" fixed = true nominal = 1e5 protected = true )  \"Cell pressure\" type: Real [5]
         plateHEX.flow_b.p[5]:VARIABLE(min = 0.0 start = plateHEX.flow_b.p_start_internal[5] unit = \"Pa\" fixed = true nominal = 1e5 protected = true )  \"Cell pressure\" type: Real [5]
         condenser.flow_a.h[1]:VARIABLE(start = condenser.flow_a.mechanicalEquilibrium.h_start[1] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true )  \"Cell enthalpy\" type: Real [9]
         condenser.flow_a.h[2]:VARIABLE(start = condenser.flow_a.mechanicalEquilibrium.h_start[2] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true )  \"Cell enthalpy\" type: Real [9]
         condenser.flow_a.h[3]:VARIABLE(start = condenser.flow_a.mechanicalEquilibrium.h_start[3] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true )  \"Cell enthalpy\" type: Real [9]
         condenser.flow_a.h[4]:VARIABLE(start = condenser.flow_a.mechanicalEquilibrium.h_start[4] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true )  \"Cell enthalpy\" type: Real [9]
         condenser.flow_a.h[5]:VARIABLE(start = condenser.flow_a.mechanicalEquilibrium.h_start[5] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true )  \"Cell enthalpy\" type: Real [9]
         condenser.flow_a.h[6]:VARIABLE(start = condenser.flow_a.mechanicalEquilibrium.h_start[6] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true )  \"Cell enthalpy\" type: Real [9]
         condenser.flow_a.h[7]:VARIABLE(start = condenser.flow_a.mechanicalEquilibrium.h_start[7] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true )  \"Cell enthalpy\" type: Real [9]
         condenser.flow_a.h[8]:VARIABLE(start = condenser.flow_a.mechanicalEquilibrium.h_start[8] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true )  \"Cell enthalpy\" type: Real [9]
         condenser.flow_a.h[9]:VARIABLE(start = condenser.flow_a.mechanicalEquilibrium.h_start[9] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true )  \"Cell enthalpy\" type: Real [9]
         condenser.flow_a.p[1]:VARIABLE(min = 0.0 start = condenser.flow_a.p_start_internal[1] unit = \"Pa\" fixed = true nominal = 1e5 protected = true )  \"Cell pressure\" type: Real [9]
         condenser.flow_a.p[2]:VARIABLE(min = 0.0 start = condenser.flow_a.p_start_internal[2] unit = \"Pa\" fixed = true nominal = 1e5 protected = true )  \"Cell pressure\" type: Real [9]
         condenser.flow_a.p[3]:VARIABLE(min = 0.0 start = condenser.flow_a.p_start_internal[3] unit = \"Pa\" fixed = true nominal = 1e5 protected = true )  \"Cell pressure\" type: Real [9]
         condenser.flow_a.p[4]:VARIABLE(min = 0.0 start = condenser.flow_a.p_start_internal[4] unit = \"Pa\" fixed = true nominal = 1e5 protected = true )  \"Cell pressure\" type: Real [9]
         condenser.flow_a.p[5]:VARIABLE(min = 0.0 start = condenser.flow_a.p_start_internal[5] unit = \"Pa\" fixed = true nominal = 1e5 protected = true )  \"Cell pressure\" type: Real [9]
         condenser.flow_a.p[6]:VARIABLE(min = 0.0 start = condenser.flow_a.p_start_internal[6] unit = \"Pa\" fixed = true nominal = 1e5 protected = true )  \"Cell pressure\" type: Real [9]
         condenser.flow_a.p[7]:VARIABLE(min = 0.0 start = condenser.flow_a.p_start_internal[7] unit = \"Pa\" fixed = true nominal = 1e5 protected = true )  \"Cell pressure\" type: Real [9]
         condenser.flow_a.p[8]:VARIABLE(min = 0.0 start = condenser.flow_a.p_start_internal[8] unit = \"Pa\" fixed = true nominal = 1e5 protected = true )  \"Cell pressure\" type: Real [9]
         condenser.flow_a.p[9]:VARIABLE(min = 0.0 start = condenser.flow_a.p_start_internal[9] unit = \"Pa\" fixed = true nominal = 1e5 protected = true )  \"Cell pressure\" type: Real [9]
         condenser.flow_b.h[1]:VARIABLE(start = condenser.flow_b.h_start[1] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer )  \"Cell enthalpy\" type: Real [9]
         condenser.flow_b.h[2]:VARIABLE(start = condenser.flow_b.h_start[2] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer )  \"Cell enthalpy\" type: Real [9]
         condenser.flow_b.h[3]:VARIABLE(start = condenser.flow_b.h_start[3] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer )  \"Cell enthalpy\" type: Real [9]
         condenser.flow_b.h[4]:VARIABLE(start = condenser.flow_b.h_start[4] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer )  \"Cell enthalpy\" type: Real [9]
         condenser.flow_b.h[5]:VARIABLE(start = condenser.flow_b.h_start[5] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer )  \"Cell enthalpy\" type: Real [9]
         condenser.flow_b.h[6]:VARIABLE(start = condenser.flow_b.h_start[6] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer )  \"Cell enthalpy\" type: Real [9]
         condenser.flow_b.h[7]:VARIABLE(start = condenser.flow_b.h_start[7] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer )  \"Cell enthalpy\" type: Real [9]
         condenser.flow_b.h[8]:VARIABLE(start = condenser.flow_b.h_start[8] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer )  \"Cell enthalpy\" type: Real [9]
         condenser.flow_b.h[9]:VARIABLE(start = condenser.flow_b.h_start[9] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer )  \"Cell enthalpy\" type: Real [9]
         condenser.flow_b.p[1]:VARIABLE(min = 0.0 start = condenser.flow_b.p_start[1] unit = \"Pa\" fixed = true nominal = 1e5 protected = true )  \"Cell pressure\" type: Real [9]
         condenser.flow_b.p[2]:VARIABLE(min = 0.0 start = condenser.flow_b.p_start[2] unit = \"Pa\" fixed = true nominal = 1e5 protected = true )  \"Cell pressure\" type: Real [9]
         condenser.flow_b.p[3]:VARIABLE(min = 0.0 start = condenser.flow_b.p_start[3] unit = \"Pa\" fixed = true nominal = 1e5 protected = true )  \"Cell pressure\" type: Real [9]
         condenser.flow_b.p[4]:VARIABLE(min = 0.0 start = condenser.flow_b.p_start[4] unit = \"Pa\" fixed = true nominal = 1e5 protected = true )  \"Cell pressure\" type: Real [9]
         condenser.flow_b.p[5]:VARIABLE(min = 0.0 start = condenser.flow_b.p_start[5] unit = \"Pa\" fixed = true nominal = 1e5 protected = true )  \"Cell pressure\" type: Real [9]
         condenser.flow_b.p[6]:VARIABLE(min = 0.0 start = condenser.flow_b.p_start[6] unit = \"Pa\" fixed = true nominal = 1e5 protected = true )  \"Cell pressure\" type: Real [9]
         condenser.flow_b.p[7]:VARIABLE(min = 0.0 start = condenser.flow_b.p_start[7] unit = \"Pa\" fixed = true nominal = 1e5 protected = true )  \"Cell pressure\" type: Real [9]
         condenser.flow_b.p[8]:VARIABLE(min = 0.0 start = condenser.flow_b.p_start[8] unit = \"Pa\" fixed = true nominal = 1e5 protected = true )  \"Cell pressure\" type: Real [9]
         condenser.flow_b.p[9]:VARIABLE(min = 0.0 start = condenser.flow_b.p_start[9] unit = \"Pa\" fixed = true nominal = 1e5 protected = true )  \"Cell pressure\" type: Real [9]
         steamSeparator.volume.h_liq:VARIABLE(start = steamSeparator.volume.h_liq_start unit = \"J/kg\" fixed = true nominal = 1000.0 )  \"Specific enthalpy of liquid phase\" type: Real
         steamSeparator.volume.h_vap:VARIABLE(start = steamSeparator.volume.h_vap_start unit = \"J/kg\" fixed = true nominal = 1000.0 )  \"Specific enthalpy of vapour phase\" type: Real
         steamSeparator.volume.p_vap:VARIABLE(min = 0.0 start = steamSeparator.volume.p_start unit = \"Pa\" fixed = true nominal = 1e5 stateSelect=StateSelect.prefer )  \"Vapour pressure\" type: Real
Notification: Performance of preBalanceInitialSystem (initialization_lambda0): time 0.07148/6.582, allocations: 41.48 MB / 2.586 GB, free: 29.94 MB / 0.842 GB
Notification: Performance of partitionIndependentBlocks (initialization_lambda0): time 0.06356/6.646, allocations: 39.73 MB / 2.625 GB, free: 3.457 MB / 0.8577 GB
Notification: Performance of analyzeInitialSystem (initialization_lambda0): time 1.099/7.745, allocations: 245.9 MB / 2.865 GB, free: 72.96 MB / 0.8577 GB
Notification: Performance of solveInitialSystemEqSystem (initialization_lambda0): time 0.0002251/7.745, allocations: 48 kB / 2.865 GB, free: 72.91 MB / 0.8577 GB
Notification: Performance of matching and sorting (n=3948) (initialization_lambda0): time 0.1533/7.898, allocations: 79.68 MB / 2.943 GB, free: 10.46 MB / 0.8733 GB
Notification: Performance of prepare postOptimizeDAE: time 0.0001835/7.899, allocations: 81.09 kB / 2.943 GB, free: 10.38 MB / 0.8733 GB
Notification: Performance of postOpt simplifyComplexFunction (initialization): time 0.5044/8.403, allocations: 71.57 MB / 3.013 GB, free: 247.3 MB / 0.8733 GB
Notification: Performance of postOpt tearingSystem (initialization): time 0.01519/8.418, allocations: 5.224 MB / 3.018 GB, free: 245.7 MB / 0.8733 GB
Notification: Performance of postOpt solveSimpleEquations (initialization): time 0.04513/8.463, allocations: 8.26 MB / 3.026 GB, free: 245.4 MB / 0.8733 GB
Notification: Performance of postOpt calculateStrongComponentJacobians (initialization): time 0.06592/8.529, allocations: 104.4 MB / 3.128 GB, free: 142.4 MB / 0.8733 GB
Notification: Performance of postOpt simplifyAllExpressions (initialization): time 0.02748/8.557, allocations: 1.265 MB / 3.129 GB, free: 141.2 MB / 0.8733 GB
Notification: Performance of postOpt collapseArrayExpressions (initialization): time 0.01126/8.568, allocations: 2.097 MB / 3.131 GB, free: 139.1 MB / 0.8733 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: 779
 * 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 (3861):
 * Single equations (assignments): 3795
 * 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 0.01957/8.588, allocations: 2.3 MB / 3.134 GB, free: 137.1 MB / 0.8733 GB
Notification: Performance of postOpt lateInlineFunction (simulation): time 0.0151/8.603, allocations: 2.628 MB / 3.136 GB, free: 136 MB / 0.8733 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 0.09899/8.702, allocations: 53.76 MB / 3.189 GB, free: 83.73 MB / 0.8733 GB
Error: post-optimization module wrapFunctionCalls (simulation) failed.
"
[Timeout remaining time 791]
[Calling sys.exit(0), Time elapsed: 12.808820068021305]
Failed to read output from testmodel.py, exit status != 0:
9.160805903025903 9.178058822 7.906879994
Calling exit ...
<OMPython.OMCSessionZMQ object at 0x7fd0682a73a0>