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 0.01044/0.01044, allocations: 1.752 MB / 21.38 MB, free: 0.5625 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 0.0013/0.0013, allocations: 108.1 kB / 24.98 MB, free: 2.156 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 0.00169/0.00169, allocations: 203.2 kB / 28.7 MB, free: 3.445 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 1.393/1.393, allocations: 230.6 MB / 262.9 MB, free: 6.004 MB / 206.1 MB
"
[Timeout remaining time 178]
loadFile("/home/hudson/saved_omc/libraries/.openmodelica/libraries/ClaRa 1.9.0/package.mo", uses=false) [Timeout 180]
"Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/ClaRa 1.9.0/package.mo): time 1.027/1.027, allocations: 130.7 MB / 450.5 MB, free: 6.609 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 0.03143/0.03143, allocations: 20.6 MB / 0.6363 GB, free: 5.363 MB / 462.1 MB
Notification: Performance of FrontEnd - Absyn->SCode: time 0.159/0.1904, allocations: 81.91 MB / 0.7163 GB, free: 3.363 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 0.5007/0.6912, allocations: 76.57 MB / 0.7911 GB, free: 14.44 MB / 0.5763 GB
Notification: Performance of NFInst.instExpressions: time 0.08143/0.7726, allocations: 46.36 MB / 0.8363 GB, free: 8.516 MB / 0.6075 GB
Notification: Performance of NFInst.updateImplicitVariability: time 0.01364/0.7862, allocations: 250.2 kB / 0.8366 GB, free: 8.27 MB / 0.6075 GB
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/ClaRa 1.9.0/SimCenter.mo:71:5-72:35:writable] Warning: Connector cycleSumPort is not balanced: The number of potential variables (0) is not equal to the number of flow variables (4).
Notification: Performance of NFTyping.typeComponents: time 0.01595/0.8022, allocations: 5.656 MB / 0.8421 GB, free: 2.605 MB / 0.6075 GB
Notification: Performance of NFTyping.typeBindings: time 0.02833/0.8305, allocations: 9.696 MB / 0.8516 GB, free: 8.938 MB / 0.6232 GB
Notification: Performance of NFTyping.typeClassSections: time 0.02697/0.8575, allocations: 10.23 MB / 0.8616 GB, free: 14.75 MB / 0.6388 GB
Notification: Performance of NFFlatten.flatten: time 0.05756/0.915, allocations: 42.06 MB / 0.9026 GB, free: 4.617 MB / 0.67 GB
Notification: Performance of NFFlatten.resolveConnections: time 0.02427/0.9393, allocations: 13.38 MB / 0.9157 GB, free: 7.117 MB / 0.6857 GB
Notification: Performance of NFEvalConstants.evaluate: time 0.03338/0.9727, allocations: 16.34 MB / 0.9317 GB, free: 6.738 MB / 0.7013 GB
Notification: Performance of NFSimplifyModel.simplify: time 0.0394/1.012, allocations: 22.38 MB / 0.9535 GB, free: 308 kB / 0.7169 GB
Notification: Performance of NFPackage.collectConstants: time 0.01425/1.026, allocations: 4.535 MB / 0.9579 GB, free: 11.76 MB / 0.7325 GB
Notification: Performance of NFFlatten.collectFunctions: time 0.03127/1.058, allocations: 11.69 MB / 0.9694 GB, free: 88 kB / 0.7325 GB
Notification: Performance of NFScalarize.scalarize: time 0.02851/1.086, allocations: 16.96 MB / 0.9859 GB, free: 15.1 MB / 0.7638 GB
Notification: Performance of NFVerifyModel.verify: time 0.0519/1.138, allocations: 20.3 MB / 1.006 GB, free: 10.71 MB / 0.7794 GB
Notification: Performance of NFConvertDAE.convert: time 1.016/2.154, allocations: 66.75 MB / 1.071 GB, free: 108.4 MB / 0.8264 GB
Notification: Performance of FrontEnd - DAE generated: time 8.476e-06/2.154, allocations: 0 / 1.071 GB, free: 108.4 MB / 0.8264 GB
Notification: Performance of FrontEnd: time 1.853e-06/2.154, allocations: 2.578 kB / 1.071 GB, free: 108.4 MB / 0.8264 GB
Notification: Performance of Transformations before backend: time 0.002216/2.156, allocations: 0 / 1.071 GB, free: 108.4 MB / 0.8264 GB
Notification: Model statistics after passing the front-end and creating the data structures used by the back-end:
 * Number of equations: 5822
 * Number of variables: 5822
Notification: Performance of Generate backend data structure: time 0.1503/2.306, allocations: 42.8 MB / 1.113 GB, free: 95.52 MB / 0.8264 GB
Notification: Performance of prepare preOptimizeDAE: time 4.784e-05/2.307, allocations: 12.47 kB / 1.113 GB, free: 95.52 MB / 0.8264 GB
Notification: Performance of preOpt introduceOutputRealDerivatives (simulation): time 0.0004786/2.307, allocations: 427.4 kB / 1.113 GB, free: 95.49 MB / 0.8264 GB
Notification: Performance of preOpt introduceOutputAliases (simulation): time 0.01724/2.324, allocations: 2.739 MB / 1.116 GB, free: 95.31 MB / 0.8264 GB
Notification: Performance of preOpt normalInlineFunction (simulation): time 0.02486/2.349, allocations: 3.564 MB / 1.119 GB, free: 93.48 MB / 0.8264 GB
Notification: Performance of preOpt evaluateParameters (simulation): time 0.07841/2.428, allocations: 37.76 MB / 1.156 GB, free: 88.53 MB / 0.8264 GB
Notification: Performance of preOpt simplifyIfEquations (simulation): time 0.001293/2.429, allocations: 1.086 MB / 1.157 GB, free: 88.42 MB / 0.8264 GB
Notification: Performance of preOpt expandDerOperator (simulation): time 0.01217/2.441, allocations: 1.436 MB / 1.159 GB, free: 87.95 MB / 0.8264 GB
Notification: Performance of preOpt clockPartitioning (simulation): time 0.1428/2.584, allocations: 64.18 MB / 1.221 GB, free: 25.77 MB / 0.8264 GB
Notification: Performance of preOpt findStateOrder (simulation): time 0.000745/2.585, allocations: 106.1 kB / 1.221 GB, free: 25.73 MB / 0.8264 GB
Notification: Performance of preOpt replaceEdgeChange (simulation): time 0.01198/2.596, allocations: 0.6867 MB / 1.222 GB, free: 25.08 MB / 0.8264 GB
Notification: Performance of preOpt inlineArrayEqn (simulation): time 0.002798/2.599, allocations: 2.735 MB / 1.225 GB, free: 22.35 MB / 0.8264 GB
Notification: Performance of preOpt removeEqualRHS (simulation): time 0.1891/2.788, allocations: 95.2 MB / 1.318 GB, free: 7.664 MB / 0.9045 GB
Warning: The model contains alias variables with redundant start and/or conflicting nominal values. It is recommended to resolve the conflicts, because otherwise the system could be hard to solve. To print the conflicting alias sets and the chosen candidates please use -d=aliasConflicts.
Notification: Performance of preOpt removeSimpleEquations (simulation): time 0.8268/3.615, allocations: 215.9 MB / 1.529 GB, free: 353.3 MB / 1.014 GB
Notification: Performance of preOpt comSubExp (simulation): time 0.09888/3.714, allocations: 51.93 MB / 1.579 GB, free: 332.7 MB / 1.014 GB
Notification: Performance of preOpt resolveLoops (simulation): time 0.04097/3.755, allocations: 30.72 MB / 1.609 GB, free: 319.5 MB / 1.014 GB
Notification: Performance of preOpt evalFunc (simulation): time 0.00541/3.76, allocations: 1.222 MB / 1.61 GB, free: 319.3 MB / 1.014 GB
Notification: Performance of preOpt encapsulateWhenConditions (simulation): time 0.0002705/3.761, allocations: 299.4 kB / 1.611 GB, free: 319.1 MB / 1.014 GB
Notification: Performance of pre-optimization done (n=3004): time 2.347e-05/3.761, allocations: 0 / 1.611 GB, free: 319.1 MB / 1.014 GB
Notification: Performance of matching and sorting (n=3005): time 0.7637/4.524, allocations: 324 MB / 1.927 GB, free: 11.07 MB / 1.014 GB
Notification: Performance of inlineWhenForInitialization (initialization): time 0.0007088/4.525, allocations: 2.382 MB / 1.929 GB, free: 8.18 MB / 1.014 GB
Notification: Performance of selectInitializationVariablesDAE (initialization): time 0.4186/4.944, allocations: 24.47 MB / 1.953 GB, free: 437.9 MB / 1.014 GB
Notification: Performance of collectPreVariables (initialization): time 0.008865/4.953, allocations: 368.4 kB / 1.954 GB, free: 437.7 MB / 1.014 GB
Notification: Performance of collectInitialEqns (initialization): time 0.01151/4.964, allocations: 10.75 MB / 1.964 GB, free: 431.6 MB / 1.014 GB
Notification: Performance of collectInitialBindings (initialization): time 0.01704/4.981, allocations: 10.57 MB / 1.974 GB, free: 424.6 MB / 1.014 GB
Notification: Performance of simplifyInitialFunctions (initialization): time 0.03415/5.015, allocations: 6.697 MB / 1.981 GB, free: 422.4 MB / 1.014 GB
Notification: Performance of setup shared object (initialization): time 5.386e-05/5.015, allocations: 301.8 kB / 1.981 GB, free: 422.1 MB / 1.014 GB
Notification: Performance of preBalanceInitialSystem (initialization): time 0.04896/5.064, allocations: 32.9 MB / 2.013 GB, free: 409.4 MB / 1.014 GB
Notification: Performance of partitionIndependentBlocks (initialization): time 0.05616/5.12, allocations: 39.35 MB / 2.052 GB, free: 389.4 MB / 1.014 GB
Notification: Performance of analyzeInitialSystem (initialization): time 0.6993/5.82, allocations: 247.3 MB / 2.293 GB, free: 150.8 MB / 1.014 GB
Notification: Performance of solveInitialSystemEqSystem (initialization): time 0.0001753/5.82, allocations: 51.75 kB / 2.293 GB, free: 150.8 MB / 1.014 GB
Notification: Performance of matching and sorting (n=3948) (initialization): time 0.1465/5.966, allocations: 81.16 MB / 2.373 GB, free: 69.36 MB / 1.014 GB
Notification: Performance of prepare postOptimizeDAE: time 0.0001229/5.967, allocations: 79.94 kB / 2.373 GB, free: 69.28 MB / 1.014 GB
Notification: Performance of postOpt simplifyComplexFunction (initialization): time 0.5408/6.507, allocations: 73.06 MB / 2.444 GB, free: 410.2 MB / 1.014 GB
Notification: Performance of postOpt tearingSystem (initialization): time 0.01567/6.523, allocations: 5.285 MB / 2.449 GB, free: 408.5 MB / 1.014 GB
Notification: Performance of postOpt solveSimpleEquations (initialization): time 0.0496/6.573, allocations: 8.328 MB / 2.457 GB, free: 408.2 MB / 1.014 GB
Notification: Performance of postOpt calculateStrongComponentJacobians (initialization): time 0.06712/6.64, allocations: 105.5 MB / 2.56 GB, free: 316.2 MB / 1.014 GB
Notification: Performance of postOpt simplifyAllExpressions (initialization): time 0.03177/6.672, allocations: 1.299 MB / 2.562 GB, free: 315.8 MB / 1.014 GB
Notification: Performance of postOpt collapseArrayExpressions (initialization): time 0.01096/6.682, allocations: 2.129 MB / 2.564 GB, free: 315.5 MB / 1.014 GB
Warning: Assuming fixed start value for the following 65 variables:
         tube.h[1]:VARIABLE(start = tube.mechanicalEquilibrium.h_start[1] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true )  \"Cell enthalpy\" type: Real [3]
         tube.h[2]:VARIABLE(start = tube.mechanicalEquilibrium.h_start[2] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true )  \"Cell enthalpy\" type: Real [3]
         tube.h[3]:VARIABLE(start = tube.mechanicalEquilibrium.h_start[3] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true )  \"Cell enthalpy\" type: Real [3]
         tube.p[1]:VARIABLE(min = 0.0 start = tube.p_start_internal[1] unit = \"Pa\" fixed = true nominal = 1e5 protected = true )  \"Cell pressure\" type: Real [3]
         tube.p[2]:VARIABLE(min = 0.0 start = tube.p_start_internal[2] unit = \"Pa\" fixed = true nominal = 1e5 protected = true )  \"Cell pressure\" type: Real [3]
         tube.p[3]:VARIABLE(min = 0.0 start = tube.p_start_internal[3] unit = \"Pa\" fixed = true nominal = 1e5 protected = true )  \"Cell pressure\" type: Real [3]
         plateHEX.flow_a.h[1]:VARIABLE(start = plateHEX.flow_a.mechanicalEquilibrium.h_start[1] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true )  \"Cell enthalpy\" type: Real [5]
         plateHEX.flow_a.h[2]:VARIABLE(start = plateHEX.flow_a.mechanicalEquilibrium.h_start[2] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true )  \"Cell enthalpy\" type: Real [5]
         plateHEX.flow_a.h[3]:VARIABLE(start = plateHEX.flow_a.mechanicalEquilibrium.h_start[3] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true )  \"Cell enthalpy\" type: Real [5]
         plateHEX.flow_a.h[4]:VARIABLE(start = plateHEX.flow_a.mechanicalEquilibrium.h_start[4] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true )  \"Cell enthalpy\" type: Real [5]
         plateHEX.flow_a.h[5]:VARIABLE(start = plateHEX.flow_a.mechanicalEquilibrium.h_start[5] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true )  \"Cell enthalpy\" type: Real [5]
         plateHEX.flow_a.p[1]:VARIABLE(min = 0.0 start = plateHEX.flow_a.p_start_internal[1] unit = \"Pa\" fixed = true nominal = 1e5 protected = true )  \"Cell pressure\" type: Real [5]
         plateHEX.flow_a.p[2]:VARIABLE(min = 0.0 start = plateHEX.flow_a.p_start_internal[2] unit = \"Pa\" fixed = true nominal = 1e5 protected = true )  \"Cell pressure\" type: Real [5]
         plateHEX.flow_a.p[3]:VARIABLE(min = 0.0 start = plateHEX.flow_a.p_start_internal[3] unit = \"Pa\" fixed = true nominal = 1e5 protected = true )  \"Cell pressure\" type: Real [5]
         plateHEX.flow_a.p[4]:VARIABLE(min = 0.0 start = plateHEX.flow_a.p_start_internal[4] unit = \"Pa\" fixed = true nominal = 1e5 protected = true )  \"Cell pressure\" type: Real [5]
         plateHEX.flow_a.p[5]:VARIABLE(min = 0.0 start = plateHEX.flow_a.p_start_internal[5] unit = \"Pa\" fixed = true nominal = 1e5 protected = true )  \"Cell pressure\" type: Real [5]
         plateHEX.flow_b.h[1]:VARIABLE(start = plateHEX.flow_b.mechanicalEquilibrium.h_start[1] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true )  \"Cell enthalpy\" type: Real [5]
         plateHEX.flow_b.h[2]:VARIABLE(start = plateHEX.flow_b.mechanicalEquilibrium.h_start[2] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true )  \"Cell enthalpy\" type: Real [5]
         plateHEX.flow_b.h[3]:VARIABLE(start = plateHEX.flow_b.mechanicalEquilibrium.h_start[3] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true )  \"Cell enthalpy\" type: Real [5]
         plateHEX.flow_b.h[4]:VARIABLE(start = plateHEX.flow_b.mechanicalEquilibrium.h_start[4] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true )  \"Cell enthalpy\" type: Real [5]
         plateHEX.flow_b.h[5]:VARIABLE(start = plateHEX.flow_b.mechanicalEquilibrium.h_start[5] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true )  \"Cell enthalpy\" type: Real [5]
         plateHEX.flow_b.p[1]:VARIABLE(min = 0.0 start = plateHEX.flow_b.p_start_internal[1] unit = \"Pa\" fixed = true nominal = 1e5 protected = true )  \"Cell pressure\" type: Real [5]
         plateHEX.flow_b.p[2]:VARIABLE(min = 0.0 start = plateHEX.flow_b.p_start_internal[2] unit = \"Pa\" fixed = true nominal = 1e5 protected = true )  \"Cell pressure\" type: Real [5]
         plateHEX.flow_b.p[3]:VARIABLE(min = 0.0 start = plateHEX.flow_b.p_start_internal[3] unit = \"Pa\" fixed = true nominal = 1e5 protected = true )  \"Cell pressure\" type: Real [5]
         plateHEX.flow_b.p[4]:VARIABLE(min = 0.0 start = plateHEX.flow_b.p_start_internal[4] unit = \"Pa\" fixed = true nominal = 1e5 protected = true )  \"Cell pressure\" type: Real [5]
         plateHEX.flow_b.p[5]:VARIABLE(min = 0.0 start = plateHEX.flow_b.p_start_internal[5] unit = \"Pa\" fixed = true nominal = 1e5 protected = true )  \"Cell pressure\" type: Real [5]
         condenser.flow_a.h[1]:VARIABLE(start = condenser.flow_a.mechanicalEquilibrium.h_start[1] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true )  \"Cell enthalpy\" type: Real [9]
         condenser.flow_a.h[2]:VARIABLE(start = condenser.flow_a.mechanicalEquilibrium.h_start[2] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true )  \"Cell enthalpy\" type: Real [9]
         condenser.flow_a.h[3]:VARIABLE(start = condenser.flow_a.mechanicalEquilibrium.h_start[3] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true )  \"Cell enthalpy\" type: Real [9]
         condenser.flow_a.h[4]:VARIABLE(start = condenser.flow_a.mechanicalEquilibrium.h_start[4] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true )  \"Cell enthalpy\" type: Real [9]
         condenser.flow_a.h[5]:VARIABLE(start = condenser.flow_a.mechanicalEquilibrium.h_start[5] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true )  \"Cell enthalpy\" type: Real [9]
         condenser.flow_a.h[6]:VARIABLE(start = condenser.flow_a.mechanicalEquilibrium.h_start[6] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true )  \"Cell enthalpy\" type: Real [9]
         condenser.flow_a.h[7]:VARIABLE(start = condenser.flow_a.mechanicalEquilibrium.h_start[7] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true )  \"Cell enthalpy\" type: Real [9]
         condenser.flow_a.h[8]:VARIABLE(start = condenser.flow_a.mechanicalEquilibrium.h_start[8] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true )  \"Cell enthalpy\" type: Real [9]
         condenser.flow_a.h[9]:VARIABLE(start = condenser.flow_a.mechanicalEquilibrium.h_start[9] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true )  \"Cell enthalpy\" type: Real [9]
         condenser.flow_a.p[1]:VARIABLE(min = 0.0 start = condenser.flow_a.p_start_internal[1] unit = \"Pa\" fixed = true nominal = 1e5 protected = true )  \"Cell pressure\" type: Real [9]
         condenser.flow_a.p[2]:VARIABLE(min = 0.0 start = condenser.flow_a.p_start_internal[2] unit = \"Pa\" fixed = true nominal = 1e5 protected = true )  \"Cell pressure\" type: Real [9]
         condenser.flow_a.p[3]:VARIABLE(min = 0.0 start = condenser.flow_a.p_start_internal[3] unit = \"Pa\" fixed = true nominal = 1e5 protected = true )  \"Cell pressure\" type: Real [9]
         condenser.flow_a.p[4]:VARIABLE(min = 0.0 start = condenser.flow_a.p_start_internal[4] unit = \"Pa\" fixed = true nominal = 1e5 protected = true )  \"Cell pressure\" type: Real [9]
         condenser.flow_a.p[5]:VARIABLE(min = 0.0 start = condenser.flow_a.p_start_internal[5] unit = \"Pa\" fixed = true nominal = 1e5 protected = true )  \"Cell pressure\" type: Real [9]
         condenser.flow_a.p[6]:VARIABLE(min = 0.0 start = condenser.flow_a.p_start_internal[6] unit = \"Pa\" fixed = true nominal = 1e5 protected = true )  \"Cell pressure\" type: Real [9]
         condenser.flow_a.p[7]:VARIABLE(min = 0.0 start = condenser.flow_a.p_start_internal[7] unit = \"Pa\" fixed = true nominal = 1e5 protected = true )  \"Cell pressure\" type: Real [9]
         condenser.flow_a.p[8]:VARIABLE(min = 0.0 start = condenser.flow_a.p_start_internal[8] unit = \"Pa\" fixed = true nominal = 1e5 protected = true )  \"Cell pressure\" type: Real [9]
         condenser.flow_a.p[9]:VARIABLE(min = 0.0 start = condenser.flow_a.p_start_internal[9] unit = \"Pa\" fixed = true nominal = 1e5 protected = true )  \"Cell pressure\" type: Real [9]
         condenser.flow_b.h[1]:VARIABLE(start = condenser.flow_b.h_start[1] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer )  \"Cell enthalpy\" type: Real [9]
         condenser.flow_b.h[2]:VARIABLE(start = condenser.flow_b.h_start[2] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer )  \"Cell enthalpy\" type: Real [9]
         condenser.flow_b.h[3]:VARIABLE(start = condenser.flow_b.h_start[3] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer )  \"Cell enthalpy\" type: Real [9]
         condenser.flow_b.h[4]:VARIABLE(start = condenser.flow_b.h_start[4] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer )  \"Cell enthalpy\" type: Real [9]
         condenser.flow_b.h[5]:VARIABLE(start = condenser.flow_b.h_start[5] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer )  \"Cell enthalpy\" type: Real [9]
         condenser.flow_b.h[6]:VARIABLE(start = condenser.flow_b.h_start[6] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer )  \"Cell enthalpy\" type: Real [9]
         condenser.flow_b.h[7]:VARIABLE(start = condenser.flow_b.h_start[7] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer )  \"Cell enthalpy\" type: Real [9]
         condenser.flow_b.h[8]:VARIABLE(start = condenser.flow_b.h_start[8] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer )  \"Cell enthalpy\" type: Real [9]
         condenser.flow_b.h[9]:VARIABLE(start = condenser.flow_b.h_start[9] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer )  \"Cell enthalpy\" type: Real [9]
         condenser.flow_b.p[1]:VARIABLE(min = 0.0 start = condenser.flow_b.p_start[1] unit = \"Pa\" fixed = true nominal = 1e5 protected = true )  \"Cell pressure\" type: Real [9]
         condenser.flow_b.p[2]:VARIABLE(min = 0.0 start = condenser.flow_b.p_start[2] unit = \"Pa\" fixed = true nominal = 1e5 protected = true )  \"Cell pressure\" type: Real [9]
         condenser.flow_b.p[3]:VARIABLE(min = 0.0 start = condenser.flow_b.p_start[3] unit = \"Pa\" fixed = true nominal = 1e5 protected = true )  \"Cell pressure\" type: Real [9]
         condenser.flow_b.p[4]:VARIABLE(min = 0.0 start = condenser.flow_b.p_start[4] unit = \"Pa\" fixed = true nominal = 1e5 protected = true )  \"Cell pressure\" type: Real [9]
         condenser.flow_b.p[5]:VARIABLE(min = 0.0 start = condenser.flow_b.p_start[5] unit = \"Pa\" fixed = true nominal = 1e5 protected = true )  \"Cell pressure\" type: Real [9]
         condenser.flow_b.p[6]:VARIABLE(min = 0.0 start = condenser.flow_b.p_start[6] unit = \"Pa\" fixed = true nominal = 1e5 protected = true )  \"Cell pressure\" type: Real [9]
         condenser.flow_b.p[7]:VARIABLE(min = 0.0 start = condenser.flow_b.p_start[7] unit = \"Pa\" fixed = true nominal = 1e5 protected = true )  \"Cell pressure\" type: Real [9]
         condenser.flow_b.p[8]:VARIABLE(min = 0.0 start = condenser.flow_b.p_start[8] unit = \"Pa\" fixed = true nominal = 1e5 protected = true )  \"Cell pressure\" type: Real [9]
         condenser.flow_b.p[9]:VARIABLE(min = 0.0 start = condenser.flow_b.p_start[9] unit = \"Pa\" fixed = true nominal = 1e5 protected = true )  \"Cell pressure\" type: Real [9]
         steamSeparator.volume.h_liq:VARIABLE(start = steamSeparator.volume.h_liq_start unit = \"J/kg\" fixed = true nominal = 1000.0 )  \"Specific enthalpy of liquid phase\" type: Real
         steamSeparator.volume.h_vap:VARIABLE(start = steamSeparator.volume.h_vap_start unit = \"J/kg\" fixed = true nominal = 1000.0 )  \"Specific enthalpy of vapour phase\" type: Real
         steamSeparator.volume.p_vap:VARIABLE(min = 0.0 start = steamSeparator.volume.p_start unit = \"Pa\" fixed = true nominal = 1e5 stateSelect=StateSelect.prefer )  \"Vapour pressure\" type: Real
Notification: Performance of preBalanceInitialSystem (initialization_lambda0): time 0.06936/6.752, allocations: 41.46 MB / 2.604 GB, free: 280.4 MB / 1.014 GB
Notification: Performance of partitionIndependentBlocks (initialization_lambda0): time 0.05167/6.804, allocations: 38.68 MB / 2.642 GB, free: 239.3 MB / 1.014 GB
Notification: Performance of analyzeInitialSystem (initialization_lambda0): time 1.137/7.94, allocations: 244.5 MB / 2.881 GB, free: 384.7 MB / 1.014 GB
Notification: Performance of solveInitialSystemEqSystem (initialization_lambda0): time 0.0002261/7.941, allocations: 49.19 kB / 2.881 GB, free: 384.7 MB / 1.014 GB
Notification: Performance of matching and sorting (n=3948) (initialization_lambda0): time 0.1477/8.088, allocations: 79.68 MB / 2.959 GB, free: 365 MB / 1.014 GB
Notification: Performance of prepare postOptimizeDAE: time 0.0001509/8.089, allocations: 77.66 kB / 2.959 GB, free: 365 MB / 1.014 GB
Notification: Performance of postOpt simplifyComplexFunction (initialization): time 0.1234/8.212, allocations: 71.57 MB / 3.029 GB, free: 324.5 MB / 1.014 GB
Notification: Performance of postOpt tearingSystem (initialization): time 0.01519/8.227, allocations: 5.226 MB / 3.034 GB, free: 320.3 MB / 1.014 GB
Notification: Performance of postOpt solveSimpleEquations (initialization): time 0.04635/8.274, allocations: 8.253 MB / 3.042 GB, free: 312 MB / 1.014 GB
Notification: Performance of postOpt calculateStrongComponentJacobians (initialization): time 0.06573/8.339, allocations: 104.9 MB / 3.144 GB, free: 200.5 MB / 1.014 GB
Notification: Performance of postOpt simplifyAllExpressions (initialization): time 0.02989/8.369, allocations: 1.263 MB / 3.145 GB, free: 199.3 MB / 1.014 GB
Notification: Performance of postOpt collapseArrayExpressions (initialization): time 0.01032/8.379, allocations: 2.097 MB / 3.148 GB, free: 197.2 MB / 1.014 GB
Warning: Assuming fixed start value for the following 65 variables:
         tube.h[1]:VARIABLE(start = tube.mechanicalEquilibrium.h_start[1] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true )  \"Cell enthalpy\" type: Real [3]
         tube.h[2]:VARIABLE(start = tube.mechanicalEquilibrium.h_start[2] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true )  \"Cell enthalpy\" type: Real [3]
         tube.h[3]:VARIABLE(start = tube.mechanicalEquilibrium.h_start[3] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true )  \"Cell enthalpy\" type: Real [3]
         tube.p[1]:VARIABLE(min = 0.0 start = tube.p_start_internal[1] unit = \"Pa\" fixed = true nominal = 1e5 protected = true )  \"Cell pressure\" type: Real [3]
         tube.p[2]:VARIABLE(min = 0.0 start = tube.p_start_internal[2] unit = \"Pa\" fixed = true nominal = 1e5 protected = true )  \"Cell pressure\" type: Real [3]
         tube.p[3]:VARIABLE(min = 0.0 start = tube.p_start_internal[3] unit = \"Pa\" fixed = true nominal = 1e5 protected = true )  \"Cell pressure\" type: Real [3]
         plateHEX.flow_a.h[1]:VARIABLE(start = plateHEX.flow_a.mechanicalEquilibrium.h_start[1] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true )  \"Cell enthalpy\" type: Real [5]
         plateHEX.flow_a.h[2]:VARIABLE(start = plateHEX.flow_a.mechanicalEquilibrium.h_start[2] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true )  \"Cell enthalpy\" type: Real [5]
         plateHEX.flow_a.h[3]:VARIABLE(start = plateHEX.flow_a.mechanicalEquilibrium.h_start[3] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true )  \"Cell enthalpy\" type: Real [5]
         plateHEX.flow_a.h[4]:VARIABLE(start = plateHEX.flow_a.mechanicalEquilibrium.h_start[4] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true )  \"Cell enthalpy\" type: Real [5]
         plateHEX.flow_a.h[5]:VARIABLE(start = plateHEX.flow_a.mechanicalEquilibrium.h_start[5] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true )  \"Cell enthalpy\" type: Real [5]
         plateHEX.flow_a.p[1]:VARIABLE(min = 0.0 start = plateHEX.flow_a.p_start_internal[1] unit = \"Pa\" fixed = true nominal = 1e5 protected = true )  \"Cell pressure\" type: Real [5]
         plateHEX.flow_a.p[2]:VARIABLE(min = 0.0 start = plateHEX.flow_a.p_start_internal[2] unit = \"Pa\" fixed = true nominal = 1e5 protected = true )  \"Cell pressure\" type: Real [5]
         plateHEX.flow_a.p[3]:VARIABLE(min = 0.0 start = plateHEX.flow_a.p_start_internal[3] unit = \"Pa\" fixed = true nominal = 1e5 protected = true )  \"Cell pressure\" type: Real [5]
         plateHEX.flow_a.p[4]:VARIABLE(min = 0.0 start = plateHEX.flow_a.p_start_internal[4] unit = \"Pa\" fixed = true nominal = 1e5 protected = true )  \"Cell pressure\" type: Real [5]
         plateHEX.flow_a.p[5]:VARIABLE(min = 0.0 start = plateHEX.flow_a.p_start_internal[5] unit = \"Pa\" fixed = true nominal = 1e5 protected = true )  \"Cell pressure\" type: Real [5]
         plateHEX.flow_b.h[1]:VARIABLE(start = plateHEX.flow_b.mechanicalEquilibrium.h_start[1] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true )  \"Cell enthalpy\" type: Real [5]
         plateHEX.flow_b.h[2]:VARIABLE(start = plateHEX.flow_b.mechanicalEquilibrium.h_start[2] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true )  \"Cell enthalpy\" type: Real [5]
         plateHEX.flow_b.h[3]:VARIABLE(start = plateHEX.flow_b.mechanicalEquilibrium.h_start[3] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true )  \"Cell enthalpy\" type: Real [5]
         plateHEX.flow_b.h[4]:VARIABLE(start = plateHEX.flow_b.mechanicalEquilibrium.h_start[4] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true )  \"Cell enthalpy\" type: Real [5]
         plateHEX.flow_b.h[5]:VARIABLE(start = plateHEX.flow_b.mechanicalEquilibrium.h_start[5] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true )  \"Cell enthalpy\" type: Real [5]
         plateHEX.flow_b.p[1]:VARIABLE(min = 0.0 start = plateHEX.flow_b.p_start_internal[1] unit = \"Pa\" fixed = true nominal = 1e5 protected = true )  \"Cell pressure\" type: Real [5]
         plateHEX.flow_b.p[2]:VARIABLE(min = 0.0 start = plateHEX.flow_b.p_start_internal[2] unit = \"Pa\" fixed = true nominal = 1e5 protected = true )  \"Cell pressure\" type: Real [5]
         plateHEX.flow_b.p[3]:VARIABLE(min = 0.0 start = plateHEX.flow_b.p_start_internal[3] unit = \"Pa\" fixed = true nominal = 1e5 protected = true )  \"Cell pressure\" type: Real [5]
         plateHEX.flow_b.p[4]:VARIABLE(min = 0.0 start = plateHEX.flow_b.p_start_internal[4] unit = \"Pa\" fixed = true nominal = 1e5 protected = true )  \"Cell pressure\" type: Real [5]
         plateHEX.flow_b.p[5]:VARIABLE(min = 0.0 start = plateHEX.flow_b.p_start_internal[5] unit = \"Pa\" fixed = true nominal = 1e5 protected = true )  \"Cell pressure\" type: Real [5]
         condenser.flow_a.h[1]:VARIABLE(start = condenser.flow_a.mechanicalEquilibrium.h_start[1] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true )  \"Cell enthalpy\" type: Real [9]
         condenser.flow_a.h[2]:VARIABLE(start = condenser.flow_a.mechanicalEquilibrium.h_start[2] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true )  \"Cell enthalpy\" type: Real [9]
         condenser.flow_a.h[3]:VARIABLE(start = condenser.flow_a.mechanicalEquilibrium.h_start[3] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true )  \"Cell enthalpy\" type: Real [9]
         condenser.flow_a.h[4]:VARIABLE(start = condenser.flow_a.mechanicalEquilibrium.h_start[4] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true )  \"Cell enthalpy\" type: Real [9]
         condenser.flow_a.h[5]:VARIABLE(start = condenser.flow_a.mechanicalEquilibrium.h_start[5] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true )  \"Cell enthalpy\" type: Real [9]
         condenser.flow_a.h[6]:VARIABLE(start = condenser.flow_a.mechanicalEquilibrium.h_start[6] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true )  \"Cell enthalpy\" type: Real [9]
         condenser.flow_a.h[7]:VARIABLE(start = condenser.flow_a.mechanicalEquilibrium.h_start[7] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true )  \"Cell enthalpy\" type: Real [9]
         condenser.flow_a.h[8]:VARIABLE(start = condenser.flow_a.mechanicalEquilibrium.h_start[8] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true )  \"Cell enthalpy\" type: Real [9]
         condenser.flow_a.h[9]:VARIABLE(start = condenser.flow_a.mechanicalEquilibrium.h_start[9] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer protected = true )  \"Cell enthalpy\" type: Real [9]
         condenser.flow_a.p[1]:VARIABLE(min = 0.0 start = condenser.flow_a.p_start_internal[1] unit = \"Pa\" fixed = true nominal = 1e5 protected = true )  \"Cell pressure\" type: Real [9]
         condenser.flow_a.p[2]:VARIABLE(min = 0.0 start = condenser.flow_a.p_start_internal[2] unit = \"Pa\" fixed = true nominal = 1e5 protected = true )  \"Cell pressure\" type: Real [9]
         condenser.flow_a.p[3]:VARIABLE(min = 0.0 start = condenser.flow_a.p_start_internal[3] unit = \"Pa\" fixed = true nominal = 1e5 protected = true )  \"Cell pressure\" type: Real [9]
         condenser.flow_a.p[4]:VARIABLE(min = 0.0 start = condenser.flow_a.p_start_internal[4] unit = \"Pa\" fixed = true nominal = 1e5 protected = true )  \"Cell pressure\" type: Real [9]
         condenser.flow_a.p[5]:VARIABLE(min = 0.0 start = condenser.flow_a.p_start_internal[5] unit = \"Pa\" fixed = true nominal = 1e5 protected = true )  \"Cell pressure\" type: Real [9]
         condenser.flow_a.p[6]:VARIABLE(min = 0.0 start = condenser.flow_a.p_start_internal[6] unit = \"Pa\" fixed = true nominal = 1e5 protected = true )  \"Cell pressure\" type: Real [9]
         condenser.flow_a.p[7]:VARIABLE(min = 0.0 start = condenser.flow_a.p_start_internal[7] unit = \"Pa\" fixed = true nominal = 1e5 protected = true )  \"Cell pressure\" type: Real [9]
         condenser.flow_a.p[8]:VARIABLE(min = 0.0 start = condenser.flow_a.p_start_internal[8] unit = \"Pa\" fixed = true nominal = 1e5 protected = true )  \"Cell pressure\" type: Real [9]
         condenser.flow_a.p[9]:VARIABLE(min = 0.0 start = condenser.flow_a.p_start_internal[9] unit = \"Pa\" fixed = true nominal = 1e5 protected = true )  \"Cell pressure\" type: Real [9]
         condenser.flow_b.h[1]:VARIABLE(start = condenser.flow_b.h_start[1] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer )  \"Cell enthalpy\" type: Real [9]
         condenser.flow_b.h[2]:VARIABLE(start = condenser.flow_b.h_start[2] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer )  \"Cell enthalpy\" type: Real [9]
         condenser.flow_b.h[3]:VARIABLE(start = condenser.flow_b.h_start[3] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer )  \"Cell enthalpy\" type: Real [9]
         condenser.flow_b.h[4]:VARIABLE(start = condenser.flow_b.h_start[4] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer )  \"Cell enthalpy\" type: Real [9]
         condenser.flow_b.h[5]:VARIABLE(start = condenser.flow_b.h_start[5] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer )  \"Cell enthalpy\" type: Real [9]
         condenser.flow_b.h[6]:VARIABLE(start = condenser.flow_b.h_start[6] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer )  \"Cell enthalpy\" type: Real [9]
         condenser.flow_b.h[7]:VARIABLE(start = condenser.flow_b.h_start[7] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer )  \"Cell enthalpy\" type: Real [9]
         condenser.flow_b.h[8]:VARIABLE(start = condenser.flow_b.h_start[8] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer )  \"Cell enthalpy\" type: Real [9]
         condenser.flow_b.h[9]:VARIABLE(start = condenser.flow_b.h_start[9] unit = \"J/kg\" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer )  \"Cell enthalpy\" type: Real [9]
         condenser.flow_b.p[1]:VARIABLE(min = 0.0 start = condenser.flow_b.p_start[1] unit = \"Pa\" fixed = true nominal = 1e5 protected = true )  \"Cell pressure\" type: Real [9]
         condenser.flow_b.p[2]:VARIABLE(min = 0.0 start = condenser.flow_b.p_start[2] unit = \"Pa\" fixed = true nominal = 1e5 protected = true )  \"Cell pressure\" type: Real [9]
         condenser.flow_b.p[3]:VARIABLE(min = 0.0 start = condenser.flow_b.p_start[3] unit = \"Pa\" fixed = true nominal = 1e5 protected = true )  \"Cell pressure\" type: Real [9]
         condenser.flow_b.p[4]:VARIABLE(min = 0.0 start = condenser.flow_b.p_start[4] unit = \"Pa\" fixed = true nominal = 1e5 protected = true )  \"Cell pressure\" type: Real [9]
         condenser.flow_b.p[5]:VARIABLE(min = 0.0 start = condenser.flow_b.p_start[5] unit = \"Pa\" fixed = true nominal = 1e5 protected = true )  \"Cell pressure\" type: Real [9]
         condenser.flow_b.p[6]:VARIABLE(min = 0.0 start = condenser.flow_b.p_start[6] unit = \"Pa\" fixed = true nominal = 1e5 protected = true )  \"Cell pressure\" type: Real [9]
         condenser.flow_b.p[7]:VARIABLE(min = 0.0 start = condenser.flow_b.p_start[7] unit = \"Pa\" fixed = true nominal = 1e5 protected = true )  \"Cell pressure\" type: Real [9]
         condenser.flow_b.p[8]:VARIABLE(min = 0.0 start = condenser.flow_b.p_start[8] unit = \"Pa\" fixed = true nominal = 1e5 protected = true )  \"Cell pressure\" type: Real [9]
         condenser.flow_b.p[9]:VARIABLE(min = 0.0 start = condenser.flow_b.p_start[9] unit = \"Pa\" fixed = true nominal = 1e5 protected = true )  \"Cell pressure\" type: Real [9]
         steamSeparator.volume.h_liq:VARIABLE(start = steamSeparator.volume.h_liq_start unit = \"J/kg\" fixed = true nominal = 1000.0 )  \"Specific enthalpy of liquid phase\" type: Real
         steamSeparator.volume.h_vap:VARIABLE(start = steamSeparator.volume.h_vap_start unit = \"J/kg\" fixed = true nominal = 1000.0 )  \"Specific enthalpy of vapour phase\" type: Real
         steamSeparator.volume.p_vap:VARIABLE(min = 0.0 start = steamSeparator.volume.p_start unit = \"Pa\" fixed = true nominal = 1e5 stateSelect=StateSelect.prefer )  \"Vapour pressure\" type: Real
Notification: 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 0.01942/8.399, allocations: 2.296 MB / 3.15 GB, free: 195 MB / 1.014 GB
Notification: Performance of postOpt lateInlineFunction (simulation): time 0.01676/8.416, allocations: 2.628 MB / 3.152 GB, free: 193.9 MB / 1.014 GB
Warning: After manipulating the system with postOptModule wrapFunctionCalls the system is unbalanced. This indicates that the original system is singular. You can use -d=dumpCSE and -d=dumpCSE_verbose for more information.
Error: Too many equations, over-determined system. The model has 3887 equation(s) and 3767 variable(s).
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia main/VLEFluid/MixtureCompatible/VLEFluid_ph.mo:55:3-60:21:writable] Error: (tube.steamQuality[1], tube.fluid[1].cp, tube.fluid[1].cv, tube.fluid[1].beta, tube.fluid[1].kappa, tube.fluid[1].drhodp_hxi, tube.fluid[1].drhodh_pxi, _, tube.fluid[1].w, tube.fluid[1].gamma) = ($cse342, $cse343, $cse344, $cse345, $cse346, $cse347, $cse348, $cse349, $cse350, $cse351) has size 9 but 3 variables (pumpVLE_L1_simple.outlet.h_outflow, quadruple1.m_flow, steamSeparator.volume.outlet[2].h_outflow)
Error: Internal error Transformation Module PFPlusExt index Reduction Method Pantelides failed!
Notification: Performance of <failed> postOpt wrapFunctionCalls (simulation): time 0.09849/8.514, allocations: 53.75 MB / 3.205 GB, free: 140.9 MB / 1.014 GB
Error: post-optimization module wrapFunctionCalls (simulation) failed.
"
[Timeout remaining time 791]
[Calling sys.exit(0), Time elapsed: 12.199321460095234]
Failed to read output from testmodel.py, exit status != 0:
8.66794985102024 8.681710119 6.522287882
Calling exit ...
<OMPython.OMCSessionZMQ object at 0x7fa4ab2ef3a0>