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 0.5.1/package.mo", uses=false) [Timeout 180] "Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/SMArtInt 0.5.1/package.mo): time 0.006364/0.006364, allocations: 1.34 MB / 11.13 MB, free: 3.035 MB / 13.93 MB Notification: Performance of NFInstanceAPI.mkTop(): time 0.001331/0.007695, allocations: 0.8268 MB / 11.95 MB, free: 2.203 MB / 13.93 MB " [Timeout remaining time 180] loadFile("/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.9.0-ClaRa/package.mo", uses=false) [Timeout 180] "Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.9.0-ClaRa/package.mo): time 0.07968/0.07968, allocations: 18.25 MB / 30.93 MB, free: 4.926 MB / 33.03 MB Notification: Performance of NFInstanceAPI.mkTop(): time 0.007311/0.08699, allocations: 7.681 MB / 38.62 MB, free: 8.23 MB / 44.04 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 0.0008525/0.0008525, allocations: 80.02 kB / 39.42 MB, free: 7.426 MB / 44.04 MB Notification: Performance of NFInstanceAPI.mkTop(): time 0.001452/0.002305, allocations: 451.1 kB / 39.86 MB, free: 6.996 MB / 44.04 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 0.001087/0.001087, allocations: 156.6 kB / 40.75 MB, free: 6.113 MB / 44.04 MB Notification: Performance of NFInstanceAPI.mkTop(): time 0.001257/0.002344, allocations: 474.5 kB / 41.21 MB, free: 5.648 MB / 44.04 MB " [Timeout remaining time 180] loadFile("/home/hudson/saved_omc/libraries/.openmodelica/libraries/Modelica 4.1.0+maint.om/package.mo", uses=false) [Timeout 180] "Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/Modelica 4.1.0+maint.om/package.mo): time 0.974/0.974, allocations: 177.2 MB / 219.1 MB, free: 11.38 MB / 218.7 MB Notification: Performance of NFInstanceAPI.mkTop(): time 0.07614/1.05, allocations: 53.65 MB / 272.8 MB, free: 5.738 MB / 266.7 MB " [Timeout remaining time 179] 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 0.6916/0.6916, allocations: 102.4 MB / 375.9 MB, free: 8.914 MB / 362.8 MB Notification: Performance of NFInstanceAPI.mkTop(): time 0.03922/0.7308, allocations: 28.58 MB / 404.5 MB, free: 12.45 MB / 394.8 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 TILMedia with version 1.9.0 ClaRa (/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.9.0-ClaRa/package.mo) Using package SMArtInt with version 0.5.1 (/home/hudson/saved_omc/libraries/.openmodelica/libraries/SMArtInt 0.5.1/package.mo) Running command: setCommandLineOptions("--fmiFlags=s:cvode") Running command: "" <> buildModelFMU(ClaRa.Examples.VapourCycle_01,fileNamePrefix="ClaRa_ClaRa_Examples_VapourCycle_01",fmuType="me_cs",version="2.0+3.0",platforms={"static"}) "" <> buildModelFMU(ClaRa.Examples.VapourCycle_01,fileNamePrefix="ClaRa_ClaRa_Examples_VapourCycle_01",fmuType="me_cs",version="2.0+3.0",platforms={"static"}) [Timeout 800] "Notification: Performance of FrontEnd - loaded program: time 1.042e-06/1.042e-06, allocations: 0 / 406.3 MB, free: 10.7 MB / 394.8 MB Notification: Performance of FrontEnd - Absyn->SCode: time 6.853e-06/7.895e-06, allocations: 5.688 kB / 406.3 MB, free: 10.69 MB / 394.8 MB Notification: Performance of NFInst.instantiate(ClaRa.Examples.VapourCycle_01): time 0.02759/0.02759, allocations: 42.32 MB / 448.6 MB, free: 220 kB / 426.8 MB Notification: Performance of NFInst.instExpressions: time 0.05128/0.07887, allocations: 46.39 MB / 495 MB, free: 1.676 MB / 474.8 MB Notification: Performance of NFInst.updateImplicitVariability: time 0.007098/0.08597, allocations: 250.2 kB / 495.2 MB, free: 1.43 MB / 474.8 MB [/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 0.008136/0.0941, allocations: 5.55 MB / 0.4891 GB, free: 11.85 MB / 490.8 MB Notification: Performance of NFTyping.typeBindings: time 0.0134/0.1075, allocations: 9.884 MB / 0.4987 GB, free: 1.914 MB / 490.8 MB Notification: Performance of NFTyping.typeClassSections: time 0.01403/0.1215, allocations: 10.2 MB / 0.5087 GB, free: 7.691 MB / 0.4949 GB Notification: Performance of NFFlatten.flatten: time 0.2436/0.3651, allocations: 43.01 MB / 0.5507 GB, free: 16.08 MB / 0.5105 GB Notification: Performance of NFFlatten.resolveConnections: time 0.01833/0.3834, allocations: 14.73 MB / 0.5651 GB, free: 31.3 MB / 0.5262 GB Notification: Performance of NFEvalConstants.evaluate: time 0.1549/0.5384, allocations: 69.7 MB / 0.6331 GB, free: 13.15 MB / 0.5418 GB Notification: Performance of NFSimplifyModel.simplify: time 0.02796/0.5663, allocations: 20.58 MB / 0.6532 GB, free: 9.742 MB / 0.5574 GB Notification: Performance of NFPackage.collectConstants: time 0.01084/0.5772, allocations: 4.488 MB / 0.6576 GB, free: 5.254 MB / 0.5574 GB Notification: Performance of NFFlatten.collectFunctions: time 0.02066/0.5978, allocations: 9.259 MB / 0.6666 GB, free: 12.66 MB / 0.573 GB Notification: Performance of NFScalarize.scalarize: time 0.02109/0.6189, allocations: 14.77 MB / 0.6811 GB, free: 14.02 MB / 0.5887 GB Notification: Performance of NFVerifyModel.verify: time 0.03462/0.6535, allocations: 11.17 MB / 0.692 GB, free: 2.832 MB / 0.5887 GB Notification: Performance of NFConvertDAE.convert: time 0.05609/0.7096, allocations: 39.83 MB / 0.7309 GB, free: 12.86 MB / 0.6355 GB Notification: Performance of FrontEnd - DAE generated: time 1.886e-05/0.7097, allocations: 0 / 0.7309 GB, free: 12.86 MB / 0.6355 GB Notification: Performance of FrontEnd: time 2.165e-06/0.7097, allocations: 4 kB / 0.7309 GB, free: 12.85 MB / 0.6355 GB Notification: Performance of Transformations before backend: time 0.001245/0.7109, allocations: 0 / 0.7309 GB, free: 12.85 MB / 0.6355 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 0.0758/0.7867, allocations: 43.05 MB / 0.7729 GB, free: 3.621 MB / 0.6668 GB Notification: Performance of prepare preOptimizeDAE: time 3.949e-05/0.7867, allocations: 12.02 kB / 0.7729 GB, free: 3.609 MB / 0.6668 GB Notification: Performance of preOpt introduceOutputAliases (simulation): time 0.007308/0.794, allocations: 2.75 MB / 0.7756 GB, free: 1.773 MB / 0.6668 GB Notification: Performance of preOpt normalInlineFunction (simulation): time 0.2312/1.025, allocations: 2.867 MB / 0.7784 GB, free: 142.5 MB / 0.6668 GB Notification: Performance of preOpt evaluateParameters (simulation): time 0.03499/1.06, allocations: 19.79 MB / 0.7977 GB, free: 140.4 MB / 0.6668 GB Notification: Performance of preOpt simplifyIfEquations (simulation): time 0.0008677/1.061, allocations: 1.084 MB / 0.7988 GB, free: 140.4 MB / 0.6668 GB Notification: Performance of preOpt expandDerOperator (simulation): time 0.00581/1.067, allocations: 1.627 MB / 0.8004 GB, free: 140.3 MB / 0.6668 GB Notification: Performance of preOpt clockPartitioning (simulation): time 0.0565/1.123, allocations: 41.83 MB / 0.8412 GB, free: 116.7 MB / 0.6668 GB Notification: Performance of preOpt findStateOrder (simulation): time 0.000401/1.124, allocations: 108.1 kB / 0.8413 GB, free: 116.7 MB / 0.6668 GB Notification: Performance of preOpt replaceEdgeChange (simulation): time 0.004528/1.128, allocations: 0.6875 MB / 0.842 GB, free: 116.7 MB / 0.6668 GB Notification: Performance of preOpt inlineArrayEqn (simulation): time 0.001847/1.13, allocations: 2.759 MB / 0.8447 GB, free: 116.7 MB / 0.6668 GB Notification: Performance of preOpt removeEqualRHS (simulation): time 0.06835/1.199, allocations: 23.68 MB / 0.8678 GB, free: 113.6 MB / 0.6668 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 0.1645/1.363, allocations: 133.6 MB / 0.9983 GB, free: 3.262 MB / 0.6824 GB Notification: Performance of preOpt comSubExp (simulation): time 0.04201/1.405, allocations: 20.07 MB / 1.018 GB, free: 15.33 MB / 0.7137 GB Notification: Performance of preOpt resolveLoops (simulation): time 0.01426/1.419, allocations: 6.2 MB / 1.024 GB, free: 9.047 MB / 0.7137 GB Notification: Performance of preOpt evalFunc (simulation): time 0.00348/1.423, allocations: 1.11 MB / 1.025 GB, free: 7.941 MB / 0.7137 GB Notification: Performance of preOpt encapsulateWhenConditions (simulation): time 0.0004651/1.423, allocations: 351.5 kB / 1.025 GB, free: 7.602 MB / 0.7137 GB Notification: Performance of pre-optimization done (n=3004): time 3.302e-05/1.423, allocations: 0 / 1.025 GB, free: 7.602 MB / 0.7137 GB Notification: Performance of matching and sorting (n=3005): time 0.3645/1.788, allocations: 56.83 MB / 1.081 GB, free: 158.4 MB / 0.7137 GB Notification: Performance of inlineWhenForInitialization (initialization): time 0.0007811/1.789, allocations: 7.178 MB / 1.088 GB, free: 149.9 MB / 0.7137 GB Notification: Performance of selectInitializationVariablesDAE (initialization): time 0.01635/1.805, allocations: 17.77 MB / 1.105 GB, free: 148.5 MB / 0.7137 GB Notification: Performance of collectPreVariables (initialization): time 0.003084/1.808, allocations: 399.7 kB / 1.106 GB, free: 148.5 MB / 0.7137 GB Notification: Performance of collectInitialEqns (initialization): time 0.002526/1.811, allocations: 6.832 MB / 1.112 GB, free: 146.1 MB / 0.7137 GB Notification: Performance of collectInitialBindings (initialization): time 0.005255/1.816, allocations: 10.5 MB / 1.123 GB, free: 139 MB / 0.7137 GB Notification: Performance of simplifyInitialFunctions (initialization): time 0.006784/1.823, allocations: 5.3 MB / 1.128 GB, free: 138.6 MB / 0.7137 GB Notification: Performance of setup shared object (initialization): time 2.443e-05/1.823, allocations: 304.7 kB / 1.128 GB, free: 138.3 MB / 0.7137 GB Notification: Performance of preBalanceInitialSystem (initialization): time 0.01087/1.834, allocations: 7.001 MB / 1.135 GB, free: 138 MB / 0.7137 GB Notification: Performance of partitionIndependentBlocks (initialization): time 0.01355/1.847, allocations: 19.67 MB / 1.154 GB, free: 116.6 MB / 0.7137 GB Notification: Performance of analyzeInitialSystem (initialization): time 0.03618/1.883, allocations: 29.74 MB / 1.183 GB, free: 91.41 MB / 0.7137 GB Notification: Performance of solveInitialSystemEqSystem (initialization): time 8.597e-05/1.883, allocations: 51.47 kB / 1.183 GB, free: 91.36 MB / 0.7137 GB Notification: Performance of matching and sorting (n=4066) (initialization): time 0.03535/1.919, allocations: 22.93 MB / 1.206 GB, free: 74.4 MB / 0.7137 GB Notification: Performance of prepare postOptimizeDAE: time 7.689e-05/1.919, allocations: 84.06 kB / 1.206 GB, free: 74.32 MB / 0.7137 GB Notification: Performance of postOpt simplifyComplexFunction (initialization): time 0.0005589/1.919, allocations: 0.5789 MB / 1.206 GB, free: 73.88 MB / 0.7137 GB Notification: Performance of postOpt tearingSystem (initialization): time 0.01054/1.93, allocations: 5.432 MB / 1.212 GB, free: 69.32 MB / 0.7137 GB Notification: Performance of postOpt solveSimpleEquations (initialization): time 0.0333/1.963, allocations: 13.96 MB / 1.225 GB, free: 56.04 MB / 0.7137 GB Notification: Performance of postOpt calculateStrongComponentJacobians (initialization): time 0.02842/1.992, allocations: 82.66 MB / 1.306 GB, free: 0.8984 MB / 0.7449 GB Notification: Performance of postOpt simplifyAllExpressions (initialization): time 0.01596/2.008, allocations: 0.8521 MB / 1.307 GB, free: 44 kB / 0.7449 GB Notification: Performance of postOpt collapseArrayExpressions (initialization): time 0.2258/2.233, allocations: 1.318 MB / 1.308 GB, free: 164.2 MB / 0.7449 GB Warning: Assuming fixed start value for the following 65 variables: tube.h[1]:VARIABLE(start = tube.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.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.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.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.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.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.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.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.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.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.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.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.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.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.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.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.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.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.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.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.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.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 0.0217/2.255, allocations: 7.814 MB / 1.316 GB, free: 164 MB / 0.7449 GB Notification: Performance of partitionIndependentBlocks (initialization_lambda0): time 0.01467/2.27, allocations: 19.51 MB / 1.335 GB, free: 148.5 MB / 0.7449 GB Notification: Performance of analyzeInitialSystem (initialization_lambda0): time 0.03533/2.305, allocations: 29.06 MB / 1.363 GB, free: 141.3 MB / 0.7449 GB Notification: Performance of solveInitialSystemEqSystem (initialization_lambda0): time 8.271e-05/2.305, allocations: 47.56 kB / 1.363 GB, free: 141.3 MB / 0.7449 GB Notification: Performance of matching and sorting (n=4066) (initialization_lambda0): time 0.03495/2.34, allocations: 22.62 MB / 1.385 GB, free: 139.9 MB / 0.7449 GB Notification: Performance of prepare postOptimizeDAE: time 7.842e-05/2.34, allocations: 78.72 kB / 1.385 GB, free: 139.9 MB / 0.7449 GB Notification: Performance of postOpt simplifyComplexFunction (initialization): time 0.000611/2.341, allocations: 0.5762 MB / 1.386 GB, free: 139.9 MB / 0.7449 GB Notification: Performance of postOpt tearingSystem (initialization): time 0.008742/2.35, allocations: 4.104 MB / 1.39 GB, free: 139 MB / 0.7449 GB Notification: Performance of postOpt solveSimpleEquations (initialization): time 0.03468/2.384, allocations: 13.88 MB / 1.403 GB, free: 137 MB / 0.7449 GB Notification: Performance of postOpt calculateStrongComponentJacobians (initialization): time 0.02469/2.409, allocations: 82.1 MB / 1.484 GB, free: 53.66 MB / 0.7449 GB Notification: Performance of postOpt simplifyAllExpressions (initialization): time 0.01659/2.425, allocations: 0.8995 MB / 1.484 GB, free: 53.27 MB / 0.7449 GB Notification: Performance of postOpt collapseArrayExpressions (initialization): time 0.003307/2.429, allocations: 1.3 MB / 1.486 GB, free: 52.27 MB / 0.7449 GB Warning: Assuming fixed start value for the following 65 variables: tube.h[1]:VARIABLE(start = tube.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.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.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.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.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.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.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.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.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.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.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.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.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.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.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.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.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.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.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.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.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.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: 785 * 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 (2979): * Single equations (assignments): 2745 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 168 * 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 0.00671/2.436, allocations: 2.182 MB / 1.488 GB, free: 51.43 MB / 0.7449 GB Notification: Performance of postOpt lateInlineFunction (simulation): time 0.006315/2.442, allocations: 2.002 MB / 1.49 GB, free: 50.19 MB / 0.7449 GB Notification: Performance of postOpt wrapFunctionCalls (simulation): time 0.04475/2.487, allocations: 47.82 MB / 1.536 GB, free: 20.35 MB / 0.7449 GB Notification: Performance of postOpt inlineArrayEqn (simulation): time 0.0001595/2.487, allocations: 224 kB / 1.537 GB, free: 20.13 MB / 0.7449 GB Notification: Performance of postOpt constantLinearSystem (simulation): time 5.18e-05/2.487, allocations: 20 kB / 1.537 GB, free: 20.11 MB / 0.7449 GB Notification: Performance of postOpt simplifysemiLinear (simulation): time 0.0191/2.506, allocations: 14.05 MB / 1.55 GB, free: 5.82 MB / 0.7449 GB Notification: Performance of postOpt removeSimpleEquations (simulation): time 0.05447/2.56, allocations: 39.5 MB / 1.589 GB, free: 0.9609 MB / 0.7762 GB Notification: Performance of postOpt simplifyComplexFunction (simulation): time 0.0004761/2.561, allocations: 359.6 kB / 1.589 GB, free: 0.6094 MB / 0.7762 GB Notification: Performance of postOpt solveSimpleEquations (simulation): time 0.2829/2.844, allocations: 13.23 MB / 1.602 GB, free: 169.4 MB / 0.7762 GB Notification: Performance of postOpt removeConstants (simulation): time 0.01704/2.861, allocations: 7.144 MB / 1.609 GB, free: 169.2 MB / 0.7762 GB Notification: Performance of postOpt tearingSystem (simulation): time 0.01512/2.876, allocations: 4.741 MB / 1.614 GB, free: 168.3 MB / 0.7762 GB Notification: Performance of postOpt inputDerivativesUsed (simulation): time 0.006304/2.882, allocations: 0.7267 MB / 1.615 GB, free: 168.3 MB / 0.7762 GB Notification: Performance of postOpt calculateStrongComponentJacobians (simulation): time 0.03463/2.917, allocations: 81.67 MB / 1.694 GB, free: 90.79 MB / 0.7762 GB Notification: Performance of postOpt calculateStateSetsJacobians (simulation): time 4.771e-05/2.917, allocations: 3.938 kB / 1.694 GB, free: 90.79 MB / 0.7762 GB Notification: Performance of postOpt symbolicJacobian (simulation): time 0.05943/2.976, allocations: 25.23 MB / 1.719 GB, free: 88.71 MB / 0.7762 GB Notification: Performance of postOpt simplifyTimeIndepFuncCalls (simulation): time 0.01033/2.987, allocations: 0.6552 MB / 1.72 GB, free: 88.71 MB / 0.7762 GB Notification: Performance of postOpt simplifyAllExpressions (simulation): time 0.0167/3.003, allocations: 433.1 kB / 1.72 GB, free: 88.7 MB / 0.7762 GB Notification: Performance of postOpt findZeroCrossings (simulation): time 0.007192/3.011, allocations: 1.383 MB / 1.721 GB, free: 88.68 MB / 0.7762 GB Notification: Performance of postOpt collapseArrayExpressions (simulation): time 0.0051/3.016, allocations: 0.8595 MB / 1.722 GB, free: 88.68 MB / 0.7762 GB Notification: Performance of sorting global known variables: time 0.01268/3.028, allocations: 8.748 MB / 1.731 GB, free: 88.14 MB / 0.7762 GB Notification: Performance of sort global known variables: time 4.01e-07/3.028, allocations: 0 / 1.731 GB, free: 88.14 MB / 0.7762 GB Notification: Performance of remove unused functions: time 0.05868/3.087, allocations: 16.15 MB / 1.747 GB, free: 88.14 MB / 0.7762 GB Notification: Model statistics after passing the back-end for simulation: * Number of independent subsystems: 3 * Number of states: 170 (tube.h[1],tube.h[2],tube.h[3],tube.p[1],tube.p[2],tube.p[3],plateHEX.flow_a.h[1],plateHEX.flow_a.h[2],plateHEX.flow_a.h[3],plateHEX.flow_a.h[4],plateHEX.flow_a.h[5],plateHEX.flow_a.p[1],plateHEX.flow_a.p[2],plateHEX.flow_a.p[3],plateHEX.flow_a.p[4],plateHEX.flow_a.p[5],plateHEX.flow_b.h[1],plateHEX.flow_b.h[2],plateHEX.flow_b.h[3],plateHEX.flow_b.h[4],plateHEX.flow_b.h[5],plateHEX.flow_b.p[1],plateHEX.flow_b.p[2],plateHEX.flow_b.p[3],plateHEX.flow_b.p[4],plateHEX.flow_b.p[5],plateHEX.thinWall.U[1],plateHEX.thinWall.U[2],plateHEX.thinWall.U[3],plateHEX.thinWall.U[4],plateHEX.thinWall.U[5],condenser.flow_a.h[1],condenser.flow_a.h[2],condenser.flow_a.h[3],condenser.flow_a.h[4],condenser.flow_a.h[5],condenser.flow_a.h[6],condenser.flow_a.h[7],condenser.flow_a.h[8],condenser.flow_a.h[9],condenser.flow_a.p[1],condenser.flow_a.p[2],condenser.flow_a.p[3],condenser.flow_a.p[4],condenser.flow_a.p[5],condenser.flow_a.p[6],condenser.flow_a.p[7],condenser.flow_a.p[8],condenser.flow_a.p[9],condenser.flow_b.h[1],condenser.flow_b.h[2],condenser.flow_b.h[3],condenser.flow_b.h[4],condenser.flow_b.h[5],condenser.flow_b.h[6],condenser.flow_b.h[7],condenser.flow_b.h[8],condenser.flow_b.h[9],condenser.flow_b.p[1],condenser.flow_b.p[2],condenser.flow_b.p[3],condenser.flow_b.p[4],condenser.flow_b.p[5],condenser.flow_b.p[6],condenser.flow_b.p[7],condenser.flow_b.p[8],condenser.flow_b.p[9],condenser.flow_b.xi[1,1],condenser.flow_b.xi[1,2],condenser.flow_b.xi[1,3],condenser.flow_b.xi[1,4],condenser.flow_b.xi[1,5],condenser.flow_b.xi[1,6],condenser.flow_b.xi[1,7],condenser.flow_b.xi[1,8],condenser.flow_b.xi[1,9],condenser.flow_b.xi[2,1],condenser.flow_b.xi[2,2],condenser.flow_b.xi[2,3],condenser.flow_b.xi[2,4],condenser.flow_b.xi[2,5],condenser.flow_b.xi[2,6],condenser.flow_b.xi[2,7],condenser.flow_b.xi[2,8],condenser.flow_b.xi[2,9],condenser.flow_b.xi[3,1],condenser.flow_b.xi[3,2],condenser.flow_b.xi[3,3],condenser.flow_b.xi[3,4],condenser.flow_b.xi[3,5],condenser.flow_b.xi[3,6],condenser.flow_b.xi[3,7],condenser.flow_b.xi[3,8],condenser.flow_b.xi[3,9],condenser.flow_b.xi[4,1],condenser.flow_b.xi[4,2],condenser.flow_b.xi[4,3],condenser.flow_b.xi[4,4],condenser.flow_b.xi[4,5],condenser.flow_b.xi[4,6],condenser.flow_b.xi[4,7],condenser.flow_b.xi[4,8],condenser.flow_b.xi[4,9],condenser.flow_b.xi[5,1],condenser.flow_b.xi[5,2],condenser.flow_b.xi[5,3],condenser.flow_b.xi[5,4],condenser.flow_b.xi[5,5],condenser.flow_b.xi[5,6],condenser.flow_b.xi[5,7],condenser.flow_b.xi[5,8],condenser.flow_b.xi[5,9],condenser.flow_b.xi[6,1],condenser.flow_b.xi[6,2],condenser.flow_b.xi[6,3],condenser.flow_b.xi[6,4],condenser.flow_b.xi[6,5],condenser.flow_b.xi[6,6],condenser.flow_b.xi[6,7],condenser.flow_b.xi[6,8],condenser.flow_b.xi[6,9],condenser.flow_b.xi[7,1],condenser.flow_b.xi[7,2],condenser.flow_b.xi[7,3],condenser.flow_b.xi[7,4],condenser.flow_b.xi[7,5],condenser.flow_b.xi[7,6],condenser.flow_b.xi[7,7],condenser.flow_b.xi[7,8],condenser.flow_b.xi[7,9],condenser.flow_b.xi[8,1],condenser.flow_b.xi[8,2],condenser.flow_b.xi[8,3],condenser.flow_b.xi[8,4],condenser.flow_b.xi[8,5],condenser.flow_b.xi[8,6],condenser.flow_b.xi[8,7],condenser.flow_b.xi[8,8],condenser.flow_b.xi[8,9],condenser.flow_b.xi[9,1],condenser.flow_b.xi[9,2],condenser.flow_b.xi[9,3],condenser.flow_b.xi[9,4],condenser.flow_b.xi[9,5],condenser.flow_b.xi[9,6],condenser.flow_b.xi[9,7],condenser.flow_b.xi[9,8],condenser.flow_b.xi[9,9],condenser.tubeWall.U[1],condenser.tubeWall.U[2],condenser.tubeWall.U[3],condenser.tubeWall.U[4],condenser.tubeWall.U[5],condenser.tubeWall.U[6],condenser.tubeWall.U[7],condenser.tubeWall.U[8],condenser.tubeWall.U[9],condenser.finWall.U[1],condenser.finWall.U[2],condenser.finWall.U[3],condenser.finWall.U[4],condenser.finWall.U[5],condenser.finWall.U[6],condenser.finWall.U[7],condenser.finWall.U[8],condenser.finWall.U[9],steamSeparator.volume.h_liq,steamSeparator.volume.h_vap,steamSeparator.volume.volume_vap,steamSeparator.volume.p_vap) * Number of discrete variables: 0 () * Number of discrete states: 0 () * Number of clocked states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for simulation (1897): * Single equations (assignments): 1706 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 125 * When equations: 0 * If-equations: 0 * Equation systems (not torn): 0 * Torn equation systems: 66 * Mixed (continuous/discrete) equation systems: 0 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%), (1,2,100.0%), (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%), (4,3,87.5%), (1,6,100.0%), (1,6,100.0%), (1,6,100.0%)} * Non-linear torn systems (#iteration vars, #inner vars): 2 systems {(1,3), (1,4)} Notification: Performance of Backend phase and start with SimCode phase: time 0.07042/3.157, allocations: 29.1 MB / 1.775 GB, free: 68.66 MB / 0.7762 GB [/home/hudson/saved_omc/libraries/.openmodelica/libraries/ClaRa 1.9.0/Basics/ControlVolumes/FluidVolumes/VolumeVLE_L3_TwoZonesNPort.mo:130:3-130:139:writable] Warning: Variable $DER.steamSeparator.volume.volume_vap has attribute stateSelect=StateSelect.always, but can't be selected as a state. Notification: Performance of simCode: created initialization part: time 0.07693/3.234, allocations: 54.87 MB / 1.829 GB, free: 19.19 MB / 0.7762 GB Notification: Performance of simCode: created event and clocks part: time 0.000475/3.235, allocations: 278.2 kB / 1.829 GB, free: 18.9 MB / 0.7762 GB Notification: Performance of simCode: created simulation system equations: time 0.02331/3.258, allocations: 19.58 MB / 1.848 GB, free: 15.1 MB / 0.7918 GB Notification: Performance of simCode: created of all other equations (e.g. parameter, nominal, assert, etc): time 0.03894/3.297, allocations: 11.09 MB / 1.859 GB, free: 5.68 MB / 0.7918 GB Notification: Performance of simCode: created linear, non-linear and system jacobian parts: time 0.4946/3.792, allocations: 145.3 MB / 2.001 GB, free: 146.3 MB / 0.8074 GB Notification: Performance of simCode: some other stuff during SimCode phase: time 0.01143/3.803, allocations: 6.935 MB / 2.007 GB, free: 145.6 MB / 0.8074 GB Notification: Performance of simCode: alias equations: time 0.02953/3.833, allocations: 7.488 MB / 2.015 GB, free: 144.9 MB / 0.8074 GB Notification: Performance of simCode: all other stuff during SimCode phase: time 0.05461/3.887, allocations: 20.24 MB / 2.034 GB, free: 134.7 MB / 0.8074 GB Notification: Performance of SimCode: time 1.853e-06/3.887, allocations: 0 / 2.034 GB, free: 134.7 MB / 0.8074 GB Notification: FMU-only work: backend 0.05876, simCode 0.1434, templates 0 Notification: Performance of buildModelFMU: Generate the FMI files: time 1.742/5.629, allocations: 1.01 GB / 3.044 GB, free: 20.28 MB / 0.8543 GB Notification: Building FMU for platform 'static' (1/1). Notification: Finished FMU for platform 'static' (1/1). Notification: Performance of buildModelFMU: Generate platform static: time 17.81/23.44, allocations: 17.02 kB / 3.044 GB, free: 20.27 MB / 0.8543 GB " [Timeout remaining time 776] (rm -f ClaRa_ClaRa.Examples.VapourCycle_01.pipe ; mkfifo ClaRa_ClaRa.Examples.VapourCycle_01.pipe ; head -c 1048576 < ClaRa_ClaRa.Examples.VapourCycle_01.pipe >> ../files/ClaRa_ClaRa.Examples.VapourCycle_01.sim & (cd run_OMSimulator && /home/hudson/saved_omc/OMSimulator/install/bin/OMSimulator --resultFile=../ClaRa_ClaRa.Examples.VapourCycle_01_res.mat --stripRoot --tempDir=temp_ClaRa_ClaRa_Examples_VapourCycle_01_fmu --startTime=0 --stopTime=10000 --stepSize=4 --mode=me --timeout=240 --tolerance=1e-05 ../ClaRa_ClaRa_Examples_VapourCycle_01.fmu) > ClaRa_ClaRa.Examples.VapourCycle_01.pipe 2>&1) [Timeout 252.0] diffSimulationResults("ClaRa_ClaRa.Examples.VapourCycle_01_res.mat","/var/lib/jenkins/ws/OpenModelicaLibraryTestingWork/OpenModelicaLibraryTesting/ReferenceFiles/ClaRa/ReferenceResults/ClaRa.Examples.VapourCycle_01.mat","",relTol=0.003,relTolDiffMinMax=0.003,rangeDelta=0.001) [Timeout 800] "" [Timeout remaining time 800] Reference file matches (rm -f ClaRa_ClaRa.Examples.VapourCycle_01_OMSimulator-cs-cvode.pipe ; mkfifo ClaRa_ClaRa.Examples.VapourCycle_01_OMSimulator-cs-cvode.pipe ; head -c 1048576 < ClaRa_ClaRa.Examples.VapourCycle_01_OMSimulator-cs-cvode.pipe >> /var/lib/jenkins/ws/OpenModelicaLibraryTestingWork/OpenModelicaLibraryTesting/files/ClaRa_ClaRa.Examples.VapourCycle_01_OMSimulator-cs-cvode.sim & (cd run_OMSimulator-cs-cvode && /home/hudson/saved_omc/OMSimulator/install/bin/OMSimulator --resultFile=../ClaRa_ClaRa.Examples.VapourCycle_01_OMSimulator-cs-cvode_res.mat --stripRoot --tempDir=temp_ClaRa_ClaRa_Examples_VapourCycle_01_OMSimulator-cs-cvode_fmu --startTime=0 --stopTime=10000 --stepSize=4 --mode=cs --timeout=240 --tolerance=1e-05 ../ClaRa_ClaRa_Examples_VapourCycle_01_OMSimulator-cs-cvode.fmu) > ClaRa_ClaRa.Examples.VapourCycle_01_OMSimulator-cs-cvode.pipe 2>&1) [Timeout 252.0] diffSimulationResults("ClaRa_ClaRa.Examples.VapourCycle_01_OMSimulator-cs-cvode_res.mat","/var/lib/jenkins/ws/OpenModelicaLibraryTestingWork/OpenModelicaLibraryTesting/ReferenceFiles/ClaRa/ReferenceResults/ClaRa.Examples.VapourCycle_01.mat","",relTol=0.003,relTolDiffMinMax=0.003,rangeDelta=0.001) [Timeout 800] "" [Timeout remaining time 800] Reference file matches (rm -f ClaRa_ClaRa.Examples.VapourCycle_01_OMSimulator-cs-euler.pipe ; mkfifo ClaRa_ClaRa.Examples.VapourCycle_01_OMSimulator-cs-euler.pipe ; head -c 1048576 < ClaRa_ClaRa.Examples.VapourCycle_01_OMSimulator-cs-euler.pipe >> /var/lib/jenkins/ws/OpenModelicaLibraryTestingWork/OpenModelicaLibraryTesting/files/ClaRa_ClaRa.Examples.VapourCycle_01_OMSimulator-cs-euler.sim & (cd run_OMSimulator-cs-euler && /home/hudson/saved_omc/OMSimulator/install/bin/OMSimulator --resultFile=../ClaRa_ClaRa.Examples.VapourCycle_01_OMSimulator-cs-euler_res.mat --stripRoot --tempDir=temp_ClaRa_ClaRa_Examples_VapourCycle_01_OMSimulator-cs-euler_fmu --startTime=0 --stopTime=10000 --stepSize=4 --mode=cs --timeout=240 --tolerance=1e-05 ../ClaRa_ClaRa_Examples_VapourCycle_01_OMSimulator-cs-euler.fmu) > ClaRa_ClaRa.Examples.VapourCycle_01_OMSimulator-cs-euler.pipe 2>&1) [Timeout 252.0] OMSimulator-cs-euler timed out simulating the FMU (rm -f ClaRa_ClaRa.Examples.VapourCycle_01_fmpy.pipe ; mkfifo ClaRa_ClaRa.Examples.VapourCycle_01_fmpy.pipe ; head -c 1048576 < ClaRa_ClaRa.Examples.VapourCycle_01_fmpy.pipe >> /var/lib/jenkins/ws/OpenModelicaLibraryTestingWork/OpenModelicaLibraryTesting/files/ClaRa_ClaRa.Examples.VapourCycle_01_fmpy.sim & (cd run_fmpy && python3 -m fmpy simulate --output-file ../ClaRa_ClaRa.Examples.VapourCycle_01_fmpy_res.csv --output-variables 'condenser.finWall.U[1]' 'condenser.finWall.U[2]' 'condenser.finWall.U[3]' 'condenser.finWall.U[4]' 'condenser.finWall.U[5]' 'condenser.finWall.U[6]' 'condenser.finWall.U[7]' 'condenser.finWall.U[8]' 'condenser.finWall.U[9]' 'condenser.flow_a.h[1]' 'condenser.flow_a.h[2]' 'condenser.flow_a.h[3]' 'condenser.flow_a.h[4]' 'condenser.flow_a.h[5]' 'condenser.flow_a.h[6]' 'condenser.flow_a.h[7]' 'condenser.flow_a.h[8]' 'condenser.flow_a.h[9]' 'condenser.flow_a.p[1]' 'condenser.flow_a.p[2]' 'condenser.flow_a.p[3]' 'condenser.flow_a.p[4]' 'condenser.flow_a.p[5]' 'condenser.flow_a.p[6]' 'condenser.flow_a.p[7]' 'condenser.flow_a.p[8]' 'condenser.flow_a.p[9]' 'condenser.flow_b.h[1]' 'condenser.flow_b.h[2]' 'condenser.flow_b.h[3]' 'condenser.flow_b.h[4]' 'condenser.flow_b.h[5]' 'condenser.flow_b.h[6]' 'condenser.flow_b.h[7]' 'condenser.flow_b.h[8]' 'condenser.flow_b.h[9]' 'condenser.flow_b.p[1]' 'condenser.flow_b.p[2]' 'condenser.flow_b.p[3]' 'condenser.flow_b.p[4]' 'condenser.flow_b.p[5]' 'condenser.flow_b.p[6]' 'condenser.flow_b.p[7]' 'condenser.flow_b.p[8]' 'condenser.flow_b.p[9]' 'condenser.flow_b.xi[1,1]' 'condenser.flow_b.xi[1,2]' 'condenser.flow_b.xi[1,3]' 'condenser.flow_b.xi[1,4]' 'condenser.flow_b.xi[1,5]' 'condenser.flow_b.xi[1,6]' 'condenser.flow_b.xi[1,7]' 'condenser.flow_b.xi[1,8]' 'condenser.flow_b.xi[1,9]' 'condenser.flow_b.xi[2,1]' 'condenser.flow_b.xi[2,2]' 'condenser.flow_b.xi[2,3]' 'condenser.flow_b.xi[2,4]' 'condenser.flow_b.xi[2,5]' 'condenser.flow_b.xi[2,6]' 'condenser.flow_b.xi[2,7]' 'condenser.flow_b.xi[2,8]' 'condenser.flow_b.xi[2,9]' 'condenser.flow_b.xi[3,1]' 'condenser.flow_b.xi[3,2]' 'condenser.flow_b.xi[3,3]' 'condenser.flow_b.xi[3,4]' 'condenser.flow_b.xi[3,5]' 'condenser.flow_b.xi[3,6]' 'condenser.flow_b.xi[3,7]' 'condenser.flow_b.xi[3,8]' 'condenser.flow_b.xi[3,9]' 'condenser.flow_b.xi[4,1]' 'condenser.flow_b.xi[4,2]' 'condenser.flow_b.xi[4,3]' 'condenser.flow_b.xi[4,4]' 'condenser.flow_b.xi[4,5]' 'condenser.flow_b.xi[4,6]' 'condenser.flow_b.xi[4,7]' 'condenser.flow_b.xi[4,8]' 'condenser.flow_b.xi[4,9]' 'condenser.flow_b.xi[5,1]' 'condenser.flow_b.xi[5,2]' 'condenser.flow_b.xi[5,3]' 'condenser.flow_b.xi[5,4]' 'condenser.flow_b.xi[5,5]' 'condenser.flow_b.xi[5,6]' 'condenser.flow_b.xi[5,7]' 'condenser.flow_b.xi[5,8]' 'condenser.flow_b.xi[5,9]' 'condenser.flow_b.xi[6,1]' 'condenser.flow_b.xi[6,2]' 'condenser.flow_b.xi[6,3]' 'condenser.flow_b.xi[6,4]' 'condenser.flow_b.xi[6,5]' 'condenser.flow_b.xi[6,6]' 'condenser.flow_b.xi[6,7]' 'condenser.flow_b.xi[6,8]' 'condenser.flow_b.xi[6,9]' 'condenser.flow_b.xi[7,1]' 'condenser.flow_b.xi[7,2]' 'condenser.flow_b.xi[7,3]' 'condenser.flow_b.xi[7,4]' 'condenser.flow_b.xi[7,5]' 'condenser.flow_b.xi[7,6]' 'condenser.flow_b.xi[7,7]' 'condenser.flow_b.xi[7,8]' 'condenser.flow_b.xi[7,9]' 'condenser.flow_b.xi[8,1]' 'condenser.flow_b.xi[8,2]' 'condenser.flow_b.xi[8,3]' 'condenser.flow_b.xi[8,4]' 'condenser.flow_b.xi[8,5]' 'condenser.flow_b.xi[8,6]' 'condenser.flow_b.xi[8,7]' 'condenser.flow_b.xi[8,8]' 'condenser.flow_b.xi[8,9]' 'condenser.flow_b.xi[9,1]' 'condenser.flow_b.xi[9,2]' 'condenser.flow_b.xi[9,3]' 'condenser.flow_b.xi[9,4]' 'condenser.flow_b.xi[9,5]' 'condenser.flow_b.xi[9,6]' 'condenser.flow_b.xi[9,7]' 'condenser.flow_b.xi[9,8]' 'condenser.flow_b.xi[9,9]' 'condenser.tubeWall.U[1]' 'condenser.tubeWall.U[2]' 'condenser.tubeWall.U[3]' 'condenser.tubeWall.U[4]' 'condenser.tubeWall.U[5]' 'condenser.tubeWall.U[6]' 'condenser.tubeWall.U[7]' 'condenser.tubeWall.U[8]' 'condenser.tubeWall.U[9]' 'plateHEX.flow_a.h[1]' 'plateHEX.flow_a.h[2]' 'plateHEX.flow_a.h[3]' 'plateHEX.flow_a.h[4]' 'plateHEX.flow_a.h[5]' 'plateHEX.flow_a.p[1]' 'plateHEX.flow_a.p[2]' 'plateHEX.flow_a.p[3]' 'plateHEX.flow_a.p[4]' 'plateHEX.flow_a.p[5]' 'plateHEX.flow_b.h[1]' 'plateHEX.flow_b.h[2]' 'plateHEX.flow_b.h[3]' 'plateHEX.flow_b.h[4]' 'plateHEX.flow_b.h[5]' 'plateHEX.flow_b.p[1]' 'plateHEX.flow_b.p[2]' 'plateHEX.flow_b.p[3]' 'plateHEX.flow_b.p[4]' 'plateHEX.flow_b.p[5]' 'plateHEX.thinWall.U[1]' 'plateHEX.thinWall.U[2]' 'plateHEX.thinWall.U[3]' 'plateHEX.thinWall.U[4]' 'plateHEX.thinWall.U[5]' steamSeparator.volume.h_liq steamSeparator.volume.h_vap steamSeparator.volume.p_vap steamSeparator.volume.volume_vap 'tube.h[1]' 'tube.h[2]' 'tube.h[3]' 'tube.p[1]' 'tube.p[2]' 'tube.p[3]' --start-time 0 --stop-time 10000 --timeout 240 --relative-tolerance 1e-05 --interface-type ModelExchange --solver CVode --output-interval 4 ../ClaRa_ClaRa_Examples_VapourCycle_01.fmu) > ClaRa_ClaRa.Examples.VapourCycle_01_fmpy.pipe 2>&1) [Timeout 252.0] diffSimulationResults("ClaRa_ClaRa.Examples.VapourCycle_01_fmpy_res.csv","/var/lib/jenkins/ws/OpenModelicaLibraryTestingWork/OpenModelicaLibraryTesting/ReferenceFiles/ClaRa/ReferenceResults/ClaRa.Examples.VapourCycle_01.mat","",relTol=0.003,relTolDiffMinMax=0.003,rangeDelta=0.001) [Timeout 800] "" [Timeout remaining time 800] Reference file matches (rm -f ClaRa_ClaRa.Examples.VapourCycle_01_fmpy-fmi3-cs-cvode.pipe ; mkfifo ClaRa_ClaRa.Examples.VapourCycle_01_fmpy-fmi3-cs-cvode.pipe ; head -c 1048576 < ClaRa_ClaRa.Examples.VapourCycle_01_fmpy-fmi3-cs-cvode.pipe >> /var/lib/jenkins/ws/OpenModelicaLibraryTestingWork/OpenModelicaLibraryTesting/files/ClaRa_ClaRa.Examples.VapourCycle_01_fmpy-fmi3-cs-cvode.sim & (cd run_fmpy-fmi3-cs-cvode && python3 -m fmpy simulate --output-file ../ClaRa_ClaRa.Examples.VapourCycle_01_fmpy-fmi3-cs-cvode_res.csv --output-variables 'condenser.finWall.U[1]' 'condenser.finWall.U[2]' 'condenser.finWall.U[3]' 'condenser.finWall.U[4]' 'condenser.finWall.U[5]' 'condenser.finWall.U[6]' 'condenser.finWall.U[7]' 'condenser.finWall.U[8]' 'condenser.finWall.U[9]' 'condenser.flow_a.h[1]' 'condenser.flow_a.h[2]' 'condenser.flow_a.h[3]' 'condenser.flow_a.h[4]' 'condenser.flow_a.h[5]' 'condenser.flow_a.h[6]' 'condenser.flow_a.h[7]' 'condenser.flow_a.h[8]' 'condenser.flow_a.h[9]' 'condenser.flow_a.p[1]' 'condenser.flow_a.p[2]' 'condenser.flow_a.p[3]' 'condenser.flow_a.p[4]' 'condenser.flow_a.p[5]' 'condenser.flow_a.p[6]' 'condenser.flow_a.p[7]' 'condenser.flow_a.p[8]' 'condenser.flow_a.p[9]' 'condenser.flow_b.h[1]' 'condenser.flow_b.h[2]' 'condenser.flow_b.h[3]' 'condenser.flow_b.h[4]' 'condenser.flow_b.h[5]' 'condenser.flow_b.h[6]' 'condenser.flow_b.h[7]' 'condenser.flow_b.h[8]' 'condenser.flow_b.h[9]' 'condenser.flow_b.p[1]' 'condenser.flow_b.p[2]' 'condenser.flow_b.p[3]' 'condenser.flow_b.p[4]' 'condenser.flow_b.p[5]' 'condenser.flow_b.p[6]' 'condenser.flow_b.p[7]' 'condenser.flow_b.p[8]' 'condenser.flow_b.p[9]' 'condenser.flow_b.xi[1,1]' 'condenser.flow_b.xi[1,2]' 'condenser.flow_b.xi[1,3]' 'condenser.flow_b.xi[1,4]' 'condenser.flow_b.xi[1,5]' 'condenser.flow_b.xi[1,6]' 'condenser.flow_b.xi[1,7]' 'condenser.flow_b.xi[1,8]' 'condenser.flow_b.xi[1,9]' 'condenser.flow_b.xi[2,1]' 'condenser.flow_b.xi[2,2]' 'condenser.flow_b.xi[2,3]' 'condenser.flow_b.xi[2,4]' 'condenser.flow_b.xi[2,5]' 'condenser.flow_b.xi[2,6]' 'condenser.flow_b.xi[2,7]' 'condenser.flow_b.xi[2,8]' 'condenser.flow_b.xi[2,9]' 'condenser.flow_b.xi[3,1]' 'condenser.flow_b.xi[3,2]' 'condenser.flow_b.xi[3,3]' 'condenser.flow_b.xi[3,4]' 'condenser.flow_b.xi[3,5]' 'condenser.flow_b.xi[3,6]' 'condenser.flow_b.xi[3,7]' 'condenser.flow_b.xi[3,8]' 'condenser.flow_b.xi[3,9]' 'condenser.flow_b.xi[4,1]' 'condenser.flow_b.xi[4,2]' 'condenser.flow_b.xi[4,3]' 'condenser.flow_b.xi[4,4]' 'condenser.flow_b.xi[4,5]' 'condenser.flow_b.xi[4,6]' 'condenser.flow_b.xi[4,7]' 'condenser.flow_b.xi[4,8]' 'condenser.flow_b.xi[4,9]' 'condenser.flow_b.xi[5,1]' 'condenser.flow_b.xi[5,2]' 'condenser.flow_b.xi[5,3]' 'condenser.flow_b.xi[5,4]' 'condenser.flow_b.xi[5,5]' 'condenser.flow_b.xi[5,6]' 'condenser.flow_b.xi[5,7]' 'condenser.flow_b.xi[5,8]' 'condenser.flow_b.xi[5,9]' 'condenser.flow_b.xi[6,1]' 'condenser.flow_b.xi[6,2]' 'condenser.flow_b.xi[6,3]' 'condenser.flow_b.xi[6,4]' 'condenser.flow_b.xi[6,5]' 'condenser.flow_b.xi[6,6]' 'condenser.flow_b.xi[6,7]' 'condenser.flow_b.xi[6,8]' 'condenser.flow_b.xi[6,9]' 'condenser.flow_b.xi[7,1]' 'condenser.flow_b.xi[7,2]' 'condenser.flow_b.xi[7,3]' 'condenser.flow_b.xi[7,4]' 'condenser.flow_b.xi[7,5]' 'condenser.flow_b.xi[7,6]' 'condenser.flow_b.xi[7,7]' 'condenser.flow_b.xi[7,8]' 'condenser.flow_b.xi[7,9]' 'condenser.flow_b.xi[8,1]' 'condenser.flow_b.xi[8,2]' 'condenser.flow_b.xi[8,3]' 'condenser.flow_b.xi[8,4]' 'condenser.flow_b.xi[8,5]' 'condenser.flow_b.xi[8,6]' 'condenser.flow_b.xi[8,7]' 'condenser.flow_b.xi[8,8]' 'condenser.flow_b.xi[8,9]' 'condenser.flow_b.xi[9,1]' 'condenser.flow_b.xi[9,2]' 'condenser.flow_b.xi[9,3]' 'condenser.flow_b.xi[9,4]' 'condenser.flow_b.xi[9,5]' 'condenser.flow_b.xi[9,6]' 'condenser.flow_b.xi[9,7]' 'condenser.flow_b.xi[9,8]' 'condenser.flow_b.xi[9,9]' 'condenser.tubeWall.U[1]' 'condenser.tubeWall.U[2]' 'condenser.tubeWall.U[3]' 'condenser.tubeWall.U[4]' 'condenser.tubeWall.U[5]' 'condenser.tubeWall.U[6]' 'condenser.tubeWall.U[7]' 'condenser.tubeWall.U[8]' 'condenser.tubeWall.U[9]' 'plateHEX.flow_a.h[1]' 'plateHEX.flow_a.h[2]' 'plateHEX.flow_a.h[3]' 'plateHEX.flow_a.h[4]' 'plateHEX.flow_a.h[5]' 'plateHEX.flow_a.p[1]' 'plateHEX.flow_a.p[2]' 'plateHEX.flow_a.p[3]' 'plateHEX.flow_a.p[4]' 'plateHEX.flow_a.p[5]' 'plateHEX.flow_b.h[1]' 'plateHEX.flow_b.h[2]' 'plateHEX.flow_b.h[3]' 'plateHEX.flow_b.h[4]' 'plateHEX.flow_b.h[5]' 'plateHEX.flow_b.p[1]' 'plateHEX.flow_b.p[2]' 'plateHEX.flow_b.p[3]' 'plateHEX.flow_b.p[4]' 'plateHEX.flow_b.p[5]' 'plateHEX.thinWall.U[1]' 'plateHEX.thinWall.U[2]' 'plateHEX.thinWall.U[3]' 'plateHEX.thinWall.U[4]' 'plateHEX.thinWall.U[5]' steamSeparator.volume.h_liq steamSeparator.volume.h_vap steamSeparator.volume.p_vap steamSeparator.volume.volume_vap 'tube.h[1]' 'tube.h[2]' 'tube.h[3]' 'tube.p[1]' 'tube.p[2]' 'tube.p[3]' condenser.finWall.U condenser.flow_a.h condenser.flow_a.p condenser.flow_b.h condenser.flow_b.p condenser.flow_b.xi condenser.tubeWall.U plateHEX.flow_a.h plateHEX.flow_a.p plateHEX.flow_b.h plateHEX.flow_b.p plateHEX.thinWall.U tube.h tube.p --start-time 0 --stop-time 10000 --timeout 240 --relative-tolerance 1e-05 --interface-type CoSimulation --output-interval 4 ../ClaRa_ClaRa_Examples_VapourCycle_01_fmpy-fmi3-cs-cvode.fmu) > ClaRa_ClaRa.Examples.VapourCycle_01_fmpy-fmi3-cs-cvode.pipe 2>&1) [Timeout 252.0] diffSimulationResults("ClaRa_ClaRa.Examples.VapourCycle_01_fmpy-fmi3-cs-cvode_res.csv","/var/lib/jenkins/ws/OpenModelicaLibraryTestingWork/OpenModelicaLibraryTesting/ReferenceFiles/ClaRa/ReferenceResults/ClaRa.Examples.VapourCycle_01.mat","",relTol=0.003,relTolDiffMinMax=0.003,rangeDelta=0.001) [Timeout 800] "" [Timeout remaining time 800] Reference file matches [Calling sys.exit(0), Time elapsed: 37.07822980172932]