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 0.01029/0.01029, allocations: 1.769 MB / 18.12 MB, free: 4.906 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 0.001165/0.001165, allocations: 103.7 kB / 21.36 MB, free: 1.684 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 0.001723/0.001723, allocations: 220.6 kB / 24.75 MB, free: 3.695 MB / 14.72 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 1.662/1.662, allocations: 230.6 MB / 258.5 MB, free: 13.29 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 1.219/1.219, allocations: 130.6 MB / 445.6 MB, free: 14.72 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="me",version="2.0",platforms={"static"}) "" <> buildModelFMU(ClaRa.Examples.VapourCycle_01,fileNamePrefix="ClaRa_ClaRa_Examples_VapourCycle_01",fmuType="me",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: Automatically loaded package TILMedia 1.9.0 ClaRa due to uses annotation from ClaRa. 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. 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 0.4612/0.4612, allocations: 46.15 MB / 0.6544 GB, free: 29.91 MB / 0.4982 GB Notification: Performance of FrontEnd - Absyn->SCode: time 0.2/0.6612, allocations: 89.05 MB / 0.7414 GB, free: 2.742 MB / 0.545 GB Notification: Performance of NFInst.instantiate(ClaRa.Examples.VapourCycle_01): time 0.05172/0.7129, allocations: 43.58 MB / 0.784 GB, free: 6.996 MB / 0.5919 GB Notification: Performance of NFInst.instExpressions: time 0.08132/0.7943, allocations: 45.88 MB / 0.8288 GB, free: 8.98 MB / 0.6388 GB Notification: Performance of NFInst.updateImplicitVariability: time 0.01313/0.8074, allocations: 246.2 kB / 0.829 GB, free: 8.738 MB / 0.6388 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 0.01532/0.8227, allocations: 5.524 MB / 0.8344 GB, free: 3.188 MB / 0.6388 GB Notification: Performance of NFTyping.typeBindings: time 0.02887/0.8516, allocations: 9.415 MB / 0.8436 GB, free: 9.73 MB / 0.6544 GB Notification: Performance of NFTyping.typeClassSections: time 0.03191/0.8835, allocations: 9.802 MB / 0.8532 GB, free: 15.91 MB / 0.67 GB Notification: Performance of NFFlatten.flatten: time 0.5923/1.476, allocations: 41.84 MB / 0.894 GB, free: 19.15 MB / 0.67 GB Notification: Performance of NFFlatten.resolveConnections: time 0.03114/1.507, allocations: 14.78 MB / 0.9085 GB, free: 18.53 MB / 0.67 GB Notification: Performance of NFEvalConstants.evaluate: time 0.03934/1.546, allocations: 16.32 MB / 0.9244 GB, free: 16.88 MB / 0.67 GB Notification: Performance of NFSimplifyModel.simplify: time 0.04324/1.59, allocations: 22.24 MB / 0.9461 GB, free: 7.957 MB / 0.67 GB Notification: Performance of NFPackage.collectConstants: time 0.0175/1.607, allocations: 4.541 MB / 0.9506 GB, free: 7.957 MB / 0.67 GB Notification: Performance of NFFlatten.collectFunctions: time 0.03701/1.644, allocations: 11.14 MB / 0.9614 GB, free: 3.68 MB / 0.67 GB Notification: Performance of NFScalarize.scalarize: time 0.03292/1.677, allocations: 16.89 MB / 0.9779 GB, free: 3.09 MB / 0.6857 GB Notification: Performance of NFVerifyModel.verify: time 0.06107/1.738, allocations: 20.28 MB / 0.9977 GB, free: 14.94 MB / 0.7169 GB Notification: Performance of NFConvertDAE.convert: time 0.1356/1.874, allocations: 66.6 MB / 1.063 GB, free: 14.41 MB / 0.7794 GB Notification: Performance of FrontEnd - DAE generated: time 6.742e-06/1.874, allocations: 0 / 1.063 GB, free: 14.41 MB / 0.7794 GB Notification: Performance of FrontEnd: time 2.384e-06/1.874, allocations: 0 / 1.063 GB, free: 14.41 MB / 0.7794 GB Notification: Performance of Transformations before backend: time 0.001877/1.875, allocations: 0 / 1.063 GB, free: 14.41 MB / 0.7794 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 0.1652/2.041, allocations: 42.87 MB / 1.105 GB, free: 4.109 MB / 0.8107 GB Notification: Performance of prepare preOptimizeDAE: time 6.059e-05/2.041, allocations: 8.031 kB / 1.105 GB, free: 4.102 MB / 0.8107 GB Notification: Performance of preOpt introduceOutputAliases (simulation): time 0.01842/2.059, allocations: 2.732 MB / 1.107 GB, free: 1.395 MB / 0.8107 GB Notification: Performance of preOpt normalInlineFunction (simulation): time 0.02899/2.088, allocations: 3.567 MB / 1.111 GB, free: 13.81 MB / 0.8263 GB Notification: Performance of preOpt evaluateParameters (simulation): time 0.09768/2.186, allocations: 37.49 MB / 1.147 GB, free: 9.289 MB / 0.8575 GB Notification: Performance of preOpt simplifyIfEquations (simulation): time 0.001779/2.188, allocations: 1.062 MB / 1.148 GB, free: 8.262 MB / 0.8575 GB Notification: Performance of preOpt expandDerOperator (simulation): time 0.01312/2.201, allocations: 1.436 MB / 1.15 GB, free: 6.863 MB / 0.8575 GB Notification: Performance of preOpt clockPartitioning (simulation): time 1.036/3.237, allocations: 64.19 MB / 1.213 GB, free: 252.4 MB / 0.9045 GB Notification: Performance of preOpt findStateOrder (simulation): time 0.0008201/3.238, allocations: 108.8 kB / 1.213 GB, free: 252.4 MB / 0.9045 GB Notification: Performance of preOpt replaceEdgeChange (simulation): time 0.01062/3.248, allocations: 0.6837 MB / 1.213 GB, free: 252.4 MB / 0.9045 GB Notification: Performance of preOpt inlineArrayEqn (simulation): time 0.003747/3.252, allocations: 2.735 MB / 1.216 GB, free: 252.3 MB / 0.9045 GB Notification: Performance of preOpt removeEqualRHS (simulation): time 0.1642/3.416, allocations: 95.2 MB / 1.309 GB, free: 214.5 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 0.3057/3.722, allocations: 215.9 MB / 1.52 GB, free: 15.27 MB / 0.9202 GB Notification: Performance of preOpt comSubExp (simulation): time 0.5942/4.316, allocations: 51.93 MB / 1.57 GB, free: 286.8 MB / 0.9514 GB Notification: Performance of preOpt resolveLoops (simulation): time 0.05305/4.369, allocations: 30.72 MB / 1.6 GB, free: 276.6 MB / 0.9514 GB Notification: Performance of preOpt evalFunc (simulation): time 0.008402/4.378, allocations: 1.305 MB / 1.602 GB, free: 276.3 MB / 0.9514 GB Notification: Performance of preOpt encapsulateWhenConditions (simulation): time 0.0005942/4.378, allocations: 298.8 kB / 1.602 GB, free: 276.1 MB / 0.9514 GB Notification: Performance of pre-optimization done (n=3004): time 3.013e-05/4.378, allocations: 0.5625 kB / 1.602 GB, free: 276.1 MB / 0.9514 GB Notification: Performance of matching and sorting (n=3005): time 1.288/5.666, allocations: 329 MB / 1.923 GB, free: 278.8 MB / 0.9514 GB Notification: Performance of inlineWhenForInitialization (initialization): time 0.0009783/5.667, allocations: 2.378 MB / 1.926 GB, free: 276.1 MB / 0.9514 GB Notification: Performance of selectInitializationVariablesDAE (initialization): time 0.07093/5.738, allocations: 24.48 MB / 1.95 GB, free: 268.2 MB / 0.9514 GB Notification: Performance of collectPreVariables (initialization): time 0.009261/5.747, allocations: 368.6 kB / 1.95 GB, free: 267.9 MB / 0.9514 GB Notification: Performance of collectInitialEqns (initialization): time 0.0128/5.76, allocations: 10.75 MB / 1.96 GB, free: 262.6 MB / 0.9514 GB Notification: Performance of collectInitialBindings (initialization): time 0.01861/5.778, allocations: 10.57 MB / 1.971 GB, free: 256.3 MB / 0.9514 GB Notification: Performance of simplifyInitialFunctions (initialization): time 0.03986/5.818, allocations: 6.706 MB / 1.977 GB, free: 254.1 MB / 0.9514 GB Notification: Performance of setup shared object (initialization): time 7.969e-05/5.818, allocations: 306.2 kB / 1.978 GB, free: 253.8 MB / 0.9514 GB Notification: Performance of preBalanceInitialSystem (initialization): time 0.05033/5.869, allocations: 32.91 MB / 2.01 GB, free: 241 MB / 0.9514 GB Notification: Performance of partitionIndependentBlocks (initialization): time 0.05894/5.928, allocations: 39.36 MB / 2.048 GB, free: 218.6 MB / 0.9514 GB Notification: Performance of analyzeInitialSystem (initialization): time 1.264/7.192, allocations: 247.3 MB / 2.29 GB, free: 260.1 MB / 0.9514 GB Notification: Performance of solveInitialSystemEqSystem (initialization): time 0.0002624/7.192, allocations: 49.59 kB / 2.29 GB, free: 260.1 MB / 0.9514 GB Notification: Performance of matching and sorting (n=3948) (initialization): time 0.1748/7.367, allocations: 81.16 MB / 2.369 GB, free: 229.9 MB / 0.9514 GB Notification: Performance of prepare postOptimizeDAE: time 0.0001155/7.367, allocations: 77.41 kB / 2.369 GB, free: 229.9 MB / 0.9514 GB Notification: Performance of postOpt simplifyComplexFunction (initialization): time 0.1293/7.496, allocations: 73.07 MB / 2.44 GB, free: 177 MB / 0.9514 GB Notification: Performance of postOpt tearingSystem (initialization): time 0.01543/7.512, allocations: 5.276 MB / 2.446 GB, free: 171.7 MB / 0.9514 GB Notification: Performance of postOpt solveSimpleEquations (initialization): time 0.05136/7.563, allocations: 8.334 MB / 2.454 GB, free: 163.4 MB / 0.9514 GB Notification: Performance of postOpt calculateStrongComponentJacobians (initialization): time 0.07122/7.634, allocations: 112.1 MB / 2.563 GB, free: 42.91 MB / 0.9514 GB Notification: Performance of postOpt simplifyAllExpressions (initialization): time 0.03381/7.668, allocations: 1.305 MB / 2.564 GB, free: 41.71 MB / 0.9514 GB Notification: Performance of postOpt collapseArrayExpressions (initialization): time 0.01371/7.682, allocations: 2.128 MB / 2.566 GB, free: 39.58 MB / 0.9514 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 0.07312/7.755, allocations: 41.46 MB / 2.607 GB, free: 14.21 MB / 0.967 GB Notification: Performance of partitionIndependentBlocks (initialization_lambda0): time 0.6653/8.42, allocations: 38.68 MB / 2.645 GB, free: 270.4 MB / 0.9827 GB Notification: Performance of analyzeInitialSystem (initialization_lambda0): time 0.7467/9.167, allocations: 244.5 MB / 2.884 GB, free: 118.4 MB / 0.9827 GB Notification: Performance of solveInitialSystemEqSystem (initialization_lambda0): time 0.000321/9.167, allocations: 48 kB / 2.884 GB, free: 118.4 MB / 0.9827 GB Notification: Performance of matching and sorting (n=3948) (initialization_lambda0): time 0.1557/9.323, allocations: 79.68 MB / 2.961 GB, free: 40.55 MB / 0.9827 GB Notification: Performance of prepare postOptimizeDAE: time 0.0001403/9.323, allocations: 84.77 kB / 2.961 GB, free: 40.47 MB / 0.9827 GB Notification: Performance of postOpt simplifyComplexFunction (initialization): time 0.6726/9.996, allocations: 71.56 MB / 3.031 GB, free: 276.1 MB / 0.9983 GB Notification: Performance of postOpt tearingSystem (initialization): time 0.01811/10.01, allocations: 5.229 MB / 3.036 GB, free: 274.9 MB / 0.9983 GB Notification: Performance of postOpt solveSimpleEquations (initialization): time 0.05197/10.07, allocations: 8.26 MB / 3.045 GB, free: 274.7 MB / 0.9983 GB Notification: Performance of postOpt calculateStrongComponentJacobians (initialization): time 0.07376/10.14, allocations: 111.5 MB / 3.153 GB, free: 175.6 MB / 0.9983 GB Notification: Performance of postOpt simplifyAllExpressions (initialization): time 0.03759/10.18, allocations: 1.265 MB / 3.155 GB, free: 175.1 MB / 0.9983 GB Notification: Performance of postOpt collapseArrayExpressions (initialization): time 0.01648/10.19, allocations: 2.095 MB / 3.157 GB, free: 174.9 MB / 0.9983 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 0.02305/10.22, allocations: 2.299 MB / 3.159 GB, free: 173.9 MB / 0.9983 GB Notification: Performance of postOpt lateInlineFunction (simulation): time 0.01912/10.24, allocations: 2.626 MB / 3.162 GB, free: 173.9 MB / 0.9983 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 postOpt wrapFunctionCalls (simulation): time 0.1159/10.35, allocations: 53.76 MB / 3.214 GB, free: 150.8 MB / 0.9983 GB Error: post-optimization module wrapFunctionCalls (simulation) failed. " [Timeout remaining time 790] [Calling sys.exit(0), Time elapsed: 14.381479579998995] Failed to read output from testmodel.py, exit status != 0: 10.361655547007103 10.373498837 8.494787071 Calling exit ...