Running: ./testmodel.py --libraries=/home/hudson/saved_omc/libraries/.openmodelica/libraries/ --ompython_omhome=/usr ThermoPower_ThermoPower.Examples.RankineCycle.Simulators.ClosedLoop.conf.json loadFile("/home/hudson/saved_omc/libraries/.openmodelica/libraries/Complex 3.2.3+maint.om/package.mo", uses=false) loadFile("/home/hudson/saved_omc/libraries/.openmodelica/libraries/Modelica 3.2.3+maint.om/package.mo", uses=false) loadFile("/home/hudson/saved_omc/libraries/.openmodelica/libraries/ModelicaServices 3.2.3+maint.om/package.mo", uses=false) loadFile("/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermoPower 3.1.0-master/package.mo", uses=false) Using package ThermoPower with version 3.1 (/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermoPower 3.1.0-master/package.mo) Using package ModelicaServices with version 3.2.3 (/home/hudson/saved_omc/libraries/.openmodelica/libraries/ModelicaServices 3.2.3+maint.om/package.mo) Using package Modelica with version 3.2.3 (/home/hudson/saved_omc/libraries/.openmodelica/libraries/Modelica 3.2.3+maint.om/package.mo) Using package Complex with version 3.2.3 (/home/hudson/saved_omc/libraries/.openmodelica/libraries/Complex 3.2.3+maint.om/package.mo) Running command: "" <> buildModelFMU(ThermoPower.Examples.RankineCycle.Simulators.ClosedLoop,fileNamePrefix="ThermoPower_ThermoPower_Examples_RankineCycle_Simulators_ClosedLoop",fmuType="me",version="2.0",platforms={"static"}) "" <> buildModelFMU(ThermoPower.Examples.RankineCycle.Simulators.ClosedLoop,fileNamePrefix="ThermoPower_ThermoPower_Examples_RankineCycle_Simulators_ClosedLoop",fmuType="me",version="2.0",platforms={"static"}) Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/Complex 3.2.3+maint.om/package.mo): time 0.001543/0.001543, allocations: 177.1 kB / 8.35 MB, free: 0.7266 MB / 5.871 MB Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/Modelica 3.2.3+maint.om/package.mo): time 1.983/1.983, allocations: 205.3 MB / 214.1 MB, free: 14.13 MB / 187.1 MB Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/ModelicaServices 3.2.3+maint.om/package.mo): time 0.0009059/0.0009058, allocations: 91.53 kB / 262.1 MB, free: 13.87 MB / 219.1 MB Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermoPower 3.1.0-master/package.mo): time 0.543/0.543, allocations: 48.77 MB / 358.8 MB, free: 53.16 MB / 299.1 MB Notification: Performance of FrontEnd - loaded program: time 2.034e-05/2.037e-05, allocations: 224 / 425.4 MB, free: 8.152 MB / 315.1 MB Notification: Performance of FrontEnd - Absyn->SCode: time 0.151/0.1511, allocations: 60.26 MB / 485.6 MB, free: 11.74 MB / 379.1 MB Notification: Performance of FrontEnd - scodeFlatten: time 9.251/9.402, allocations: 3.838 GB / 4.312 GB, free: 51.52 MB / 0.5108 GB Notification: Performance of FrontEnd - mkProgramGraph: time 0.0002486/9.402, allocations: 91.95 kB / 4.313 GB, free: 51.43 MB / 0.5108 GB [/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermoPower 3.1.0-master/Examples.mo:2509:70-2509:81:writable] Error: Variable q_nom not found in scope ThermoPower.Examples.RankineCycle.Models. [/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermoPower 3.1.0-master/Examples.mo:2517:21-2517:69:writable] Error: Cyclically dependent constants or parameters found in scope : {q_nom}, {head_nom} (ignore with -d=ignoreCycles). Notification: Performance of FrontEnd - DAE generated: time 9.559/18.96, allocations: 2.684 GB / 6.997 GB, free: 18.37 MB / 0.6358 GB Notification: Performance of FrontEnd: time 1.754e-06/18.96, allocations: 3.969 kB / 6.997 GB, free: 18.37 MB / 0.6358 GB Notification: Performance of Transformations before backend: time 0.000825/18.96, allocations: 206.4 kB / 6.997 GB, free: 18.34 MB / 0.6358 GB Notification: Model statistics after passing the front-end and creating the data structures used by the back-end: * Number of equations: 2419 * Number of variables: 2419 Notification: Performance of Generate backend data structure: time 0.04532/19.01, allocations: 11.11 MB / 7.008 GB, free: 9.621 MB / 0.6358 GB Notification: Performance of prepare preOptimizeDAE: time 4.184e-05/19.01, allocations: 8.031 kB / 7.008 GB, free: 9.613 MB / 0.6358 GB Notification: Performance of preOpt normalInlineFunction (simulation): time 0.03172/19.04, allocations: 5.629 MB / 7.013 GB, free: 6.426 MB / 0.6358 GB Notification: Performance of preOpt evaluateParameters (simulation): time 0.02473/19.06, allocations: 8.78 MB / 7.022 GB, free: 15.58 MB / 0.6515 GB Notification: Performance of preOpt simplifyIfEquations (simulation): time 0.0009409/19.06, allocations: 411.6 kB / 7.022 GB, free: 15.17 MB / 0.6515 GB Notification: Performance of preOpt expandDerOperator (simulation): time 0.006471/19.07, allocations: 0.5737 MB / 7.023 GB, free: 14.59 MB / 0.6515 GB Notification: Performance of preOpt removeEqualFunctionCalls (simulation): time 0.9442/20.02, allocations: 20.55 MB / 7.043 GB, free: 38.11 MB / 0.6515 GB Notification: Performance of preOpt clockPartitioning (simulation): time 0.05163/20.07, allocations: 18.74 MB / 7.061 GB, free: 37.43 MB / 0.6515 GB Notification: Performance of preOpt findStateOrder (simulation): time 0.0003884/20.07, allocations: 4.781 kB / 7.061 GB, free: 37.43 MB / 0.6515 GB Notification: Performance of preOpt replaceEdgeChange (simulation): time 0.005539/20.07, allocations: 16.31 kB / 7.061 GB, free: 37.43 MB / 0.6515 GB Notification: Performance of preOpt inlineArrayEqn (simulation): time 0.0004879/20.07, allocations: 0.5054 MB / 7.062 GB, free: 37.41 MB / 0.6515 GB Warning: The model contains alias variables with conflicting start and/or 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 0.2341/20.31, allocations: 127.7 MB / 7.186 GB, free: 31.74 MB / 0.6984 GB Notification: Performance of preOpt comSubExp (simulation): time 0.0229/20.33, allocations: 15.77 MB / 7.202 GB, free: 30.57 MB / 0.6984 GB Notification: Performance of preOpt resolveLoops (simulation): time 0.01585/20.35, allocations: 9.771 MB / 7.211 GB, free: 30.48 MB / 0.6984 GB Notification: Performance of preOpt evalFunc (simulation): time 0.8413/21.19, allocations: 129.8 MB / 7.338 GB, free: 135.9 MB / 0.7453 GB Notification: Performance of preOpt encapsulateWhenConditions (simulation): time 0.0002134/21.19, allocations: 162.3 kB / 7.338 GB, free: 135.9 MB / 0.7453 GB Notification: Performance of pre-optimization done (n=825): time 1.213e-05/21.19, allocations: 0.9375 kB / 7.338 GB, free: 135.9 MB / 0.7453 GB Notification: Performance of matching and sorting (n=845): time 0.1645/21.35, allocations: 52.83 MB / 7.39 GB, free: 134 MB / 0.7453 GB Notification: Performance of inlineWhenForInitialization (initialization): time 0.000167/21.35, allocations: 247.6 kB / 7.39 GB, free: 133.8 MB / 0.7453 GB Notification: Performance of selectInitializationVariablesDAE (initialization): time 0.005345/21.36, allocations: 2.142 MB / 7.392 GB, free: 133.6 MB / 0.7453 GB Notification: Performance of collectPreVariables (initialization): time 0.004462/21.36, allocations: 36.42 kB / 7.392 GB, free: 133.6 MB / 0.7453 GB Notification: Performance of collectInitialEqns (initialization): time 0.003491/21.37, allocations: 2.946 MB / 7.395 GB, free: 132.6 MB / 0.7453 GB Notification: Performance of collectInitialBindings (initialization): time 0.008564/21.38, allocations: 2.844 MB / 7.398 GB, free: 130.7 MB / 0.7453 GB Notification: Performance of simplifyInitialFunctions (initialization): time 0.004005/21.38, allocations: 1.375 kB / 7.398 GB, free: 130.7 MB / 0.7453 GB Notification: Performance of setup shared object (initialization): time 0.001105/21.38, allocations: 0.626 MB / 7.398 GB, free: 130.3 MB / 0.7453 GB Notification: Performance of preBalanceInitialSystem (initialization): time 0.01632/21.4, allocations: 9.118 MB / 7.407 GB, free: 130.3 MB / 0.7453 GB Notification: Performance of partitionIndependentBlocks (initialization): time 0.019/21.42, allocations: 10.3 MB / 7.417 GB, free: 129.3 MB / 0.7453 GB Notification: Performance of analyzeInitialSystem (initialization): time 0.3946/21.81, allocations: 117.9 MB / 7.533 GB, free: 101.8 MB / 0.7453 GB Notification: Performance of solveInitialSystemEqSystem (initialization): time 7.413e-05/21.81, allocations: 11.78 kB / 7.533 GB, free: 101.8 MB / 0.7453 GB Notification: Performance of matching and sorting (n=1018) (initialization): time 0.7615/22.57, allocations: 32.18 MB / 7.564 GB, free: 129.1 MB / 0.7453 GB Notification: Performance of prepare postOptimizeDAE: time 0.002166/22.57, allocations: 8.471 MB / 7.572 GB, free: 120.3 MB / 0.7453 GB Notification: Performance of postOpt simplifyComplexFunction (initialization): time 7.158e-05/22.57, allocations: 18.97 kB / 7.572 GB, free: 120.3 MB / 0.7453 GB Notification: Performance of postOpt tearingSystem (initialization): time 0.3425/22.92, allocations: 107.6 MB / 7.677 GB, free: 119 MB / 0.7453 GB Notification: Performance of postOpt solveSimpleEquations (initialization): time 0.00427/22.92, allocations: 0.7233 MB / 7.678 GB, free: 119 MB / 0.7453 GB Notification: Performance of postOpt calculateStrongComponentJacobians (initialization): time 0.1288/23.05, allocations: 47.53 MB / 7.724 GB, free: 114 MB / 0.7453 GB Notification: Performance of postOpt simplifyAllExpressions (initialization): time 0.01982/23.07, allocations: 1.412 MB / 7.726 GB, free: 114 MB / 0.7453 GB Notification: Performance of postOpt collapseArrayExpressions (initialization): time 0.004984/23.07, allocations: 0.5029 MB / 7.726 GB, free: 114 MB / 0.7453 GB Notification: Performance of prepare postOptimizeDAE: time 1.802e-05/23.07, allocations: 4.438 kB / 7.726 GB, free: 114 MB / 0.7453 GB Notification: Performance of postOpt replaceHomotopyWithSimplified (initialization): time 0.117/23.19, allocations: 31.39 MB / 7.757 GB, free: 104.2 MB / 0.7453 GB Notification: Performance of postOpt simplifyComplexFunction (initialization): time 0.0002154/23.19, allocations: 23 kB / 7.757 GB, free: 104.2 MB / 0.7453 GB Notification: Performance of postOpt tearingSystem (initialization): time 0.1495/23.34, allocations: 38.12 MB / 7.794 GB, free: 82.52 MB / 0.7453 GB Notification: Performance of postOpt solveSimpleEquations (initialization): time 0.005869/23.35, allocations: 0.985 MB / 7.795 GB, free: 81.62 MB / 0.7453 GB Notification: Performance of postOpt calculateStrongComponentJacobians (initialization): time 0.7993/24.15, allocations: 42.6 MB / 7.837 GB, free: 126.3 MB / 0.7453 GB Notification: Performance of postOpt simplifyAllExpressions (initialization): time 0.01636/24.16, allocations: 1.358 MB / 7.838 GB, free: 126.3 MB / 0.7453 GB Notification: Performance of postOpt collapseArrayExpressions (initialization): time 0.00431/24.17, allocations: 0.4919 MB / 7.839 GB, free: 126.3 MB / 0.7453 GB Warning: The initial conditions are over specified. The following 3 initial equations are redundant, so they are removed from the initialization sytem: $DER.plant.evaporator.gasFlow.p = 0.0 $DER.plant.economizer.fluidFlow.p = 0.0 $DER.plant.economizer.gasFlow.p = 0.0. Warning: Iteration variables with default zero start attribute in torn nonlinear equation system: plant.evaporator.gasFlow.drbdT2[3]:VARIABLE(unit = "kg/(m3.K)" protected = true ) "Derivative of average density by right temperature" type: Real [3] plant.evaporator.gasFlow.drbdp[3]:VARIABLE(unit = "s2/m2" protected = true ) "Derivative of average density by pressure" type: Real [3] plant.evaporator.gasFlow.drbdX2[3,1]:VARIABLE(unit = "kg/m3" protected = true ) "Derivative of average density by right composition" type: Real [3,5] plant.evaporator.gasFlow.drbdX2[3,2]:VARIABLE(unit = "kg/m3" protected = true ) "Derivative of average density by right composition" type: Real [3,5] plant.evaporator.gasFlow.drbdX2[3,3]:VARIABLE(unit = "kg/m3" protected = true ) "Derivative of average density by right composition" type: Real [3,5] plant.evaporator.gasFlow.drbdX2[3,4]:VARIABLE(unit = "kg/m3" protected = true ) "Derivative of average density by right composition" type: Real [3,5] plant.economizer.gasFlow.drbdT2[5]:VARIABLE(unit = "kg/(m3.K)" protected = true ) "Derivative of average density by right temperature" type: Real [5] plant.economizer.gasFlow.drbdp[5]:VARIABLE(unit = "s2/m2" protected = true ) "Derivative of average density by pressure" type: Real [5] plant.economizer.gasFlow.drbdX2[5,1]:VARIABLE(unit = "kg/m3" protected = true ) "Derivative of average density by right composition" type: Real [5,5] plant.economizer.gasFlow.drbdX2[5,2]:VARIABLE(unit = "kg/m3" protected = true ) "Derivative of average density by right composition" type: Real [5,5] plant.economizer.gasFlow.drbdX2[5,3]:VARIABLE(unit = "kg/m3" protected = true ) "Derivative of average density by right composition" type: Real [5,5] plant.economizer.gasFlow.drbdX2[5,4]:VARIABLE(unit = "kg/m3" protected = true ) "Derivative of average density by right composition" type: Real [5,5] plant.economizer.gasFlow.drbdX2[5,5]:VARIABLE(unit = "kg/m3" protected = true ) "Derivative of average density by right composition" type: Real [5,5] plant.evaporator.gasFlow.drbdX2[3,5]:VARIABLE(unit = "kg/m3" protected = true ) "Derivative of average density by right composition" type: Real [3,5] plant.superheater.gasFlow.drbdT2[6]:VARIABLE(unit = "kg/(m3.K)" protected = true ) "Derivative of average density by right temperature" type: Real [6] plant.superheater.gasFlow.drbdp[6]:VARIABLE(unit = "s2/m2" protected = true ) "Derivative of average density by pressure" type: Real [6] plant.superheater.gasFlow.drbdX2[6,1]:VARIABLE(unit = "kg/m3" protected = true ) "Derivative of average density by right composition" type: Real [6,5] plant.superheater.gasFlow.drbdX2[6,2]:VARIABLE(unit = "kg/m3" protected = true ) "Derivative of average density by right composition" type: Real [6,5] plant.superheater.gasFlow.drbdX2[6,3]:VARIABLE(unit = "kg/m3" protected = true ) "Derivative of average density by right composition" type: Real [6,5] plant.superheater.gasFlow.drbdX2[6,4]:VARIABLE(unit = "kg/m3" protected = true ) "Derivative of average density by right composition" type: Real [6,5] plant.superheater.gasFlow.drbdX2[6,5]:VARIABLE(unit = "kg/m3" protected = true ) "Derivative of average density by right composition" type: Real [6,5] plant.superheater.gasFlow.drbdp[5]:VARIABLE(unit = "s2/m2" protected = true ) "Derivative of average density by pressure" type: Real [6] plant.superheater.gasFlow.drbdp[4]:VARIABLE(unit = "s2/m2" protected = true ) "Derivative of average density by pressure" type: Real [6] plant.superheater.gasFlow.drbdp[3]:VARIABLE(unit = "s2/m2" protected = true ) "Derivative of average density by pressure" type: Real [6] plant.superheater.gasFlow.drbdp[2]:VARIABLE(unit = "s2/m2" protected = true ) "Derivative of average density by pressure" type: Real [6] plant.superheater.gasFlow.drbdp[1]:VARIABLE(unit = "s2/m2" protected = true ) "Derivative of average density by pressure" type: Real [6] plant.superheater.gasFlow.drbdT2[1]:VARIABLE(unit = "kg/(m3.K)" protected = true ) "Derivative of average density by right temperature" type: Real [6] plant.superheater.gasFlow.drbdX2[1,1]:VARIABLE(unit = "kg/m3" protected = true ) "Derivative of average density by right composition" type: Real [6,5] plant.superheater.gasFlow.drbdX2[1,2]:VARIABLE(unit = "kg/m3" protected = true ) "Derivative of average density by right composition" type: Real [6,5] plant.superheater.gasFlow.drbdX2[1,3]:VARIABLE(unit = "kg/m3" protected = true ) "Derivative of average density by right composition" type: Real [6,5] plant.superheater.gasFlow.drbdX2[1,4]:VARIABLE(unit = "kg/m3" protected = true ) "Derivative of average density by right composition" type: Real [6,5] plant.superheater.gasFlow.drbdX2[1,5]:VARIABLE(unit = "kg/m3" protected = true ) "Derivative of average density by right composition" type: Real [6,5] plant.evaporator.gasFlow.drbdp[2]:VARIABLE(unit = "s2/m2" protected = true ) "Derivative of average density by pressure" type: Real [3] plant.evaporator.gasFlow.drbdp[1]:VARIABLE(unit = "s2/m2" protected = true ) "Derivative of average density by pressure" type: Real [3] plant.evaporator.gasFlow.drbdT2[1]:VARIABLE(unit = "kg/(m3.K)" protected = true ) "Derivative of average density by right temperature" type: Real [3] plant.evaporator.gasFlow.drbdX2[1,1]:VARIABLE(unit = "kg/m3" protected = true ) "Derivative of average density by right composition" type: Real [3,5] plant.evaporator.gasFlow.drbdX2[1,2]:VARIABLE(unit = "kg/m3" protected = true ) "Derivative of average density by right composition" type: Real [3,5] plant.evaporator.gasFlow.drbdX2[1,3]:VARIABLE(unit = "kg/m3" protected = true ) "Derivative of average density by right composition" type: Real [3,5] plant.evaporator.gasFlow.drbdX2[1,4]:VARIABLE(unit = "kg/m3" protected = true ) "Derivative of average density by right composition" type: Real [3,5] plant.evaporator.gasFlow.drbdX2[1,5]:VARIABLE(unit = "kg/m3" protected = true ) "Derivative of average density by right composition" type: Real [3,5] plant.economizer.gasFlow.drbdp[4]:VARIABLE(unit = "s2/m2" protected = true ) "Derivative of average density by pressure" type: Real [5] plant.economizer.gasFlow.drbdp[3]:VARIABLE(unit = "s2/m2" protected = true ) "Derivative of average density by pressure" type: Real [5] plant.economizer.gasFlow.drbdp[2]:VARIABLE(unit = "s2/m2" protected = true ) "Derivative of average density by pressure" type: Real [5] plant.economizer.gasFlow.drbdp[1]:VARIABLE(unit = "s2/m2" protected = true ) "Derivative of average density by pressure" type: Real [5] plant.economizer.gasFlow.drbdT2[1]:VARIABLE(unit = "kg/(m3.K)" protected = true ) "Derivative of average density by right temperature" type: Real [5] plant.economizer.gasFlow.drbdX2[1,1]:VARIABLE(unit = "kg/m3" protected = true ) "Derivative of average density by right composition" type: Real [5,5] plant.economizer.gasFlow.drbdX2[1,2]:VARIABLE(unit = "kg/m3" protected = true ) "Derivative of average density by right composition" type: Real [5,5] plant.economizer.gasFlow.drbdX2[1,3]:VARIABLE(unit = "kg/m3" protected = true ) "Derivative of average density by right composition" type: Real [5,5] plant.economizer.gasFlow.drbdX2[1,4]:VARIABLE(unit = "kg/m3" protected = true ) "Derivative of average density by right composition" type: Real [5,5] plant.economizer.gasFlow.drbdX2[1,5]:VARIABLE(unit = "kg/m3" protected = true ) "Derivative of average density by right composition" type: Real [5,5] plant.superheater.gasFlow.drbdT1[3]:VARIABLE(unit = "kg/(m3.K)" protected = true ) "Derivative of average density by left temperature" type: Real [6] plant.superheater.gasFlow.drbdX1[3,1]:VARIABLE(unit = "kg/m3" protected = true ) "Derivative of average density by left composition" type: Real [6,5] plant.superheater.gasFlow.drbdX1[3,2]:VARIABLE(unit = "kg/m3" protected = true ) "Derivative of average density by left composition" type: Real [6,5] plant.superheater.gasFlow.drbdX1[3,3]:VARIABLE(unit = "kg/m3" protected = true ) "Derivative of average density by left composition" type: Real [6,5] plant.evaporator.gasFlow.drbdT1[3]:VARIABLE(unit = "kg/(m3.K)" protected = true ) "Derivative of average density by left temperature" type: Real [3] plant.evaporator.gasFlow.drbdX1[3,1]:VARIABLE(unit = "kg/m3" protected = true ) "Derivative of average density by left composition" type: Real [3,5] plant.evaporator.gasFlow.drbdX1[3,2]:VARIABLE(unit = "kg/m3" protected = true ) "Derivative of average density by left composition" type: Real [3,5] plant.evaporator.gasFlow.drbdX1[3,3]:VARIABLE(unit = "kg/m3" protected = true ) "Derivative of average density by left composition" type: Real [3,5] plant.evaporator.gasFlow.drbdX1[3,4]:VARIABLE(unit = "kg/m3" protected = true ) "Derivative of average density by left composition" type: Real [3,5] plant.evaporator.gasFlow.drbdX1[3,5]:VARIABLE(unit = "kg/m3" protected = true ) "Derivative of average density by left composition" type: Real [3,5] plant.economizer.gasFlow.drbdT1[3]:VARIABLE(unit = "kg/(m3.K)" protected = true ) "Derivative of average density by left temperature" type: Real [5] plant.economizer.gasFlow.drbdX1[3,1]:VARIABLE(unit = "kg/m3" protected = true ) "Derivative of average density by left composition" type: Real [5,5] plant.economizer.gasFlow.drbdX1[3,2]:VARIABLE(unit = "kg/m3" protected = true ) "Derivative of average density by left composition" type: Real [5,5] plant.economizer.gasFlow.drbdX1[3,4]:VARIABLE(unit = "kg/m3" protected = true ) "Derivative of average density by left composition" type: Real [5,5] plant.economizer.gasFlow.drbdT1[4]:VARIABLE(unit = "kg/(m3.K)" protected = true ) "Derivative of average density by left temperature" type: Real [5] plant.economizer.gasFlow.drbdX1[4,1]:VARIABLE(unit = "kg/m3" protected = true ) "Derivative of average density by left composition" type: Real [5,5] plant.economizer.gasFlow.drbdX1[4,2]:VARIABLE(unit = "kg/m3" protected = true ) "Derivative of average density by left composition" type: Real [5,5] plant.economizer.gasFlow.drbdX1[4,3]:VARIABLE(unit = "kg/m3" protected = true ) "Derivative of average density by left composition" type: Real [5,5] plant.economizer.gasFlow.drbdX1[3,5]:VARIABLE(unit = "kg/m3" protected = true ) "Derivative of average density by left composition" type: Real [5,5] plant.economizer.gasFlow.drbdX1[3,3]:VARIABLE(unit = "kg/m3" protected = true ) "Derivative of average density by left composition" type: Real [5,5] plant.economizer.gasFlow.drbdX1[4,5]:VARIABLE(unit = "kg/m3" protected = true ) "Derivative of average density by left composition" type: Real [5,5] plant.economizer.gasFlow.drbdT1[5]:VARIABLE(unit = "kg/(m3.K)" protected = true ) "Derivative of average density by left temperature" type: Real [5] plant.economizer.gasFlow.drbdX1[5,1]:VARIABLE(unit = "kg/m3" protected = true ) "Derivative of average density by left composition" type: Real [5,5] plant.economizer.gasFlow.drbdX1[5,2]:VARIABLE(unit = "kg/m3" protected = true ) "Derivative of average density by left composition" type: Real [5,5] plant.economizer.gasFlow.drbdX1[5,3]:VARIABLE(unit = "kg/m3" protected = true ) "Derivative of average density by left composition" type: Real [5,5] plant.economizer.gasFlow.drbdX1[5,4]:VARIABLE(unit = "kg/m3" protected = true ) "Derivative of average density by left composition" type: Real [5,5] plant.economizer.gasFlow.drbdX1[4,4]:VARIABLE(unit = "kg/m3" protected = true ) "Derivative of average density by left composition" type: Real [5,5] plant.economizer.gasFlow.drbdX1[5,5]:VARIABLE(unit = "kg/m3" protected = true ) "Derivative of average density by left composition" type: Real [5,5] plant.superheater.gasFlow.drbdX1[3,4]:VARIABLE(unit = "kg/m3" protected = true ) "Derivative of average density by left composition" type: Real [6,5] plant.superheater.gasFlow.drbdT1[4]:VARIABLE(unit = "kg/(m3.K)" protected = true ) "Derivative of average density by left temperature" type: Real [6] plant.superheater.gasFlow.drbdX1[4,1]:VARIABLE(unit = "kg/m3" protected = true ) "Derivative of average density by left composition" type: Real [6,5] plant.superheater.gasFlow.drbdX1[4,2]:VARIABLE(unit = "kg/m3" protected = true ) "Derivative of average density by left composition" type: Real [6,5] plant.superheater.gasFlow.drbdX1[4,3]:VARIABLE(unit = "kg/m3" protected = true ) "Derivative of average density by left composition" type: Real [6,5] plant.superheater.gasFlow.drbdX1[4,4]:VARIABLE(unit = "kg/m3" protected = true ) "Derivative of average density by left composition" type: Real [6,5] plant.superheater.gasFlow.drbdT1[5]:VARIABLE(unit = "kg/(m3.K)" protected = true ) "Derivative of average density by left temperature" type: Real [6] plant.superheater.gasFlow.drbdX1[5,1]:VARIABLE(unit = "kg/m3" protected = true ) "Derivative of average density by left composition" type: Real [6,5] plant.superheater.gasFlow.drbdX1[5,2]:VARIABLE(unit = "kg/m3" protected = true ) "Derivative of average density by left composition" type: Real [6,5] plant.superheater.gasFlow.drbdX1[5,3]:VARIABLE(unit = "kg/m3" protected = true ) "Derivative of average density by left composition" type: Real [6,5] plant.superheater.gasFlow.drbdX1[5,4]:VARIABLE(unit = "kg/m3" protected = true ) "Derivative of average density by left composition" type: Real [6,5] plant.superheater.gasFlow.drbdX1[4,5]:VARIABLE(unit = "kg/m3" protected = true ) "Derivative of average density by left composition" type: Real [6,5] plant.superheater.gasFlow.drbdX1[3,5]:VARIABLE(unit = "kg/m3" protected = true ) "Derivative of average density by left composition" type: Real [6,5] plant.superheater.gasFlow.drbdX1[5,5]:VARIABLE(unit = "kg/m3" protected = true ) "Derivative of average density by left composition" type: Real [6,5] plant.superheater.gasFlow.drbdT1[6]:VARIABLE(unit = "kg/(m3.K)" protected = true ) "Derivative of average density by left temperature" type: Real [6] plant.superheater.gasFlow.drbdX1[6,1]:VARIABLE(unit = "kg/m3" protected = true ) "Derivative of average density by left composition" type: Real [6,5] plant.superheater.gasFlow.drbdX1[6,2]:VARIABLE(unit = "kg/m3" protected = true ) "Derivative of average density by left composition" type: Real [6,5] plant.superheater.gasFlow.drbdX1[6,3]:VARIABLE(unit = "kg/m3" protected = true ) "Derivative of average density by left composition" type: Real [6,5] plant.superheater.gasFlow.drbdX1[6,4]:VARIABLE(unit = "kg/m3" protected = true ) "Derivative of average density by left composition" type: Real [6,5] plant.superheater.gasFlow.drbdX1[6,5]:VARIABLE(unit = "kg/m3" protected = true ) "Derivative of average density by left composition" type: Real [6,5] Notification: Model statistics after passing the back-end for initialization: * Number of independent subsystems: 89 * Number of states: 0 () * Number of discrete variables: 21 (plant.superheater.fluidFlow.fluidState[7].phase,plant.superheater.fluidFlow.fluidState[6].phase,plant.superheater.fluidFlow.fluidState[5].phase,plant.superheater.fluidFlow.fluidState[4].phase,plant.superheater.fluidFlow.fluidState[3].phase,plant.superheater.fluidFlow.fluidState[2].phase,plant.superheater.fluidFlow.fluidState[1].phase,plant.economizer.fluidFlow.fluidState[6].phase,plant.economizer.fluidFlow.fluidState[5].phase,plant.economizer.fluidFlow.fluidState[4].phase,plant.economizer.fluidFlow.fluidState[3].phase,plant.economizer.fluidFlow.fluidState[2].phase,plant.economizer.fluidFlow.fluidState[1].phase,plant.steamTurbine.steamState_in.phase,plant.prescribedSpeedPump.feedWaterPump.int_Np,plant.stateWaterEconomizer_in.fluidState.phase,plant.stateWaterEvaporator_in.fluidState.phase,plant.stateWaterSuperheater_out.fluidState.phase,plant.stateWaterSuperheater_in.fluidState.phase,plant.steamTurbine.steamState_iso.phase,plant.prescribedSpeedPump.feedWaterPump.inletFluidState.phase) * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for initialization (367): * Single equations (assignments): 360 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 0 * When equations: 0 * If-equations: 0 * Equation systems (linear and non-linear blocks): 5 * Torn equation systems: 2 * Mixed (continuous/discrete) equation systems: 0 Notification: Equation system details: * Constant Jacobian: 0 * Linear Jacobian (size,density): 0 * Non-linear Jacobian: 5 {1,1,1,1,1} * Without analytic Jacobian: 0 Notification: Torn system details for strict tearing set: * Linear torn systems: 1 {(1,100.0%) 3} * Non-linear torn systems: 1 {178 471} Notification: Performance of prepare postOptimizeDAE: time 0.008519/24.18, allocations: 0.5927 MB / 7.839 GB, free: 126.1 MB / 0.7453 GB Notification: Performance of postOpt createAliasVarsForOutputStates (simulation): time 0.0759/24.25, allocations: 25.83 MB / 7.864 GB, free: 125.8 MB / 0.7453 GB Notification: Performance of postOpt lateInlineFunction (simulation): time 0.006689/24.26, allocations: 0.5328 MB / 7.865 GB, free: 125.8 MB / 0.7453 GB Notification: Performance of postOpt wrapFunctionCalls (simulation): time 0.1002/24.36, allocations: 45.71 MB / 7.91 GB, free: 125 MB / 0.7453 GB Notification: Performance of postOpt inlineArrayEqn (simulation): time 0.0002837/24.36, allocations: 139.2 kB / 7.91 GB, free: 125 MB / 0.7453 GB Notification: Performance of postOpt constantLinearSystem (simulation): time 0.0001297/24.36, allocations: 6.906 kB / 7.91 GB, free: 125 MB / 0.7453 GB Notification: Performance of postOpt simplifysemiLinear (simulation): time 0.0004913/24.36, allocations: 42.23 kB / 7.91 GB, free: 125 MB / 0.7453 GB Warning: The model contains alias variables with conflicting start and/or 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 postOpt removeSimpleEquations (simulation): time 0.1852/24.55, allocations: 71.89 MB / 7.98 GB, free: 103.1 MB / 0.7453 GB Notification: Performance of postOpt simplifyComplexFunction (simulation): time 0.0002552/24.55, allocations: 0 / 7.98 GB, free: 103.1 MB / 0.7453 GB Notification: Performance of postOpt solveSimpleEquations (simulation): time 0.02257/24.57, allocations: 1.921 MB / 7.982 GB, free: 103 MB / 0.7453 GB Notification: Performance of postOpt tearingSystem (simulation): time 0.02727/24.6, allocations: 7.269 MB / 7.989 GB, free: 101.1 MB / 0.7453 GB Notification: Performance of postOpt inputDerivativesUsed (simulation): time 0.006953/24.6, allocations: 421.7 kB / 7.989 GB, free: 101 MB / 0.7453 GB Notification: Performance of postOpt calculateStrongComponentJacobians (simulation): time 0.04944/24.65, allocations: 42.48 MB / 8.031 GB, free: 73.01 MB / 0.7453 GB Notification: Performance of postOpt calculateStateSetsJacobians (simulation): time 1.001e-05/24.65, allocations: 2.516 kB / 8.031 GB, free: 73.01 MB / 0.7453 GB Notification: Performance of postOpt symbolicJacobian (simulation): time 0.8641/25.52, allocations: 41.39 MB / 8.071 GB, free: 122.6 MB / 0.7453 GB Notification: Performance of postOpt removeConstants (simulation): time 0.01491/25.53, allocations: 3.016 MB / 8.074 GB, free: 122.5 MB / 0.7453 GB Notification: Performance of postOpt simplifyTimeIndepFuncCalls (simulation): time 0.005735/25.54, allocations: 238.9 kB / 8.074 GB, free: 122.5 MB / 0.7453 GB Notification: Performance of postOpt simplifyAllExpressions (simulation): time 0.02018/25.56, allocations: 1.11 MB / 8.075 GB, free: 122.5 MB / 0.7453 GB Notification: Performance of postOpt findZeroCrossings (simulation): time 0.005561/25.56, allocations: 0.654 MB / 8.076 GB, free: 122.5 MB / 0.7453 GB Notification: Performance of postOpt collapseArrayExpressions (simulation): time 0.005407/25.57, allocations: 493.7 kB / 8.077 GB, free: 122.5 MB / 0.7453 GB Notification: Performance of sorting global known variables: time 0.005317/25.57, allocations: 1.569 MB / 8.078 GB, free: 122.3 MB / 0.7453 GB Notification: Performance of sort global known variables: time 2.6e-07/25.57, allocations: 1.219 kB / 8.078 GB, free: 122.3 MB / 0.7453 GB Notification: Performance of remove unused functions: time 0.05622/25.63, allocations: 6.507 MB / 8.084 GB, free: 122.3 MB / 0.7453 GB Notification: Model statistics after passing the back-end for simulation: * Number of independent subsystems: 5 * Number of states: 64 (plant.condenser.Vl,plant.temperatureActuator.y,plant.powerSensor.y,plant.gasFlowActuator.y,plant.nPumpActuator.y,plant.voidFractionSensor.y,plant.economizer.fluidFlow.htilde[1],plant.economizer.fluidFlow.htilde[2],plant.economizer.fluidFlow.htilde[3],plant.economizer.fluidFlow.htilde[4],plant.economizer.fluidFlow.htilde[5],plant.economizer.metalTube.Tvol[1],plant.economizer.metalTube.Tvol[2],plant.economizer.metalTube.Tvol[3],plant.economizer.metalTube.Tvol[4],plant.economizer.metalTube.Tvol[5],plant.economizer.gasFlow.Ttilde[1],plant.economizer.gasFlow.Ttilde[2],plant.economizer.gasFlow.Ttilde[3],plant.economizer.gasFlow.Ttilde[4],plant.economizer.gasFlow.Ttilde[5],plant.economizer.gasFlow.Xtilde[1,1],plant.economizer.gasFlow.Xtilde[1,2],plant.economizer.gasFlow.Xtilde[1,3],plant.economizer.gasFlow.Xtilde[1,4],plant.economizer.gasFlow.Xtilde[1,5],plant.evaporator.water.Vl,plant.evaporator.water.p,plant.evaporator.gasFlow.Ttilde[1],plant.evaporator.gasFlow.Ttilde[2],plant.evaporator.gasFlow.Ttilde[3],plant.evaporator.gasFlow.Xtilde[1,1],plant.evaporator.gasFlow.Xtilde[1,2],plant.evaporator.gasFlow.Xtilde[1,3],plant.evaporator.gasFlow.Xtilde[1,4],plant.evaporator.gasFlow.Xtilde[1,5],plant.superheater.fluidFlow.p,plant.superheater.fluidFlow.htilde[1],plant.superheater.fluidFlow.htilde[2],plant.superheater.fluidFlow.htilde[3],plant.superheater.fluidFlow.htilde[4],plant.superheater.fluidFlow.htilde[5],plant.superheater.fluidFlow.htilde[6],plant.superheater.metalTube.Tvol[1],plant.superheater.metalTube.Tvol[2],plant.superheater.metalTube.Tvol[3],plant.superheater.metalTube.Tvol[4],plant.superheater.metalTube.Tvol[5],plant.superheater.metalTube.Tvol[6],plant.superheater.gasFlow.Ttilde[1],plant.superheater.gasFlow.Ttilde[2],plant.superheater.gasFlow.Ttilde[3],plant.superheater.gasFlow.Ttilde[4],plant.superheater.gasFlow.Ttilde[5],plant.superheater.gasFlow.Ttilde[6],plant.superheater.gasFlow.Xtilde[1,1],plant.superheater.gasFlow.Xtilde[1,2],plant.superheater.gasFlow.Xtilde[1,3],plant.superheater.gasFlow.Xtilde[1,4],plant.superheater.gasFlow.Xtilde[1,5],plant.superheater.gasFlow.p,plant.constantSpeed.phi,voidFractionController.I,powerController.I) * Number of discrete variables: 36 ($cse1.phase,$cse1.region,$cse2.phase,$cse2.region,$cse3.phase,$cse3.region,$cse4.phase,$cse4.region,$cse7.phase,$cse7.region,$cse8.phase,$cse8.region,$cse9.phase,$cse9.region,$cse10.phase,$cse10.region,$cse11.phase,$cse11.region,$cse12.phase,$cse12.region,$cse15.region3boundary,$cse16.region3boundary,$cse19.phase,$cse19.region,$cse20.phase,$cse20.region,$cse21.phase,$cse21.region,$cse22.phase,$cse22.region,$cse23.phase,$cse23.region,$cse24.phase,$cse24.region,$cse26.phase,$cse26.region) * Number of discrete states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for simulation (750): * Single equations (assignments): 713 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 18 * When equations: 0 * If-equations: 0 * Equation systems (linear and non-linear blocks): 9 * Torn equation systems: 10 * Mixed (continuous/discrete) equation systems: 0 Notification: Equation system details: * Constant Jacobian: 0 * Linear Jacobian (size,density): 0 * Non-linear Jacobian: 9 {1,1,1,1,1,1,1,1,1} * Without analytic Jacobian: 0 Notification: Torn system details for strict tearing set: * Linear torn systems: 7 {(7,69.4%) 12,(1,100.0%) 3,(1,100.0%) 2,(1,100.0%) 2,(1,100.0%) 2,(1,100.0%) 2,(1,100.0%) 2} * Non-linear torn systems: 3 {7 22,10 40,2 13} Notification: Performance of Backend phase and start with SimCode phase: time 0.1452/25.78, allocations: 42.62 MB / 8.126 GB, free: 120 MB / 0.7453 GB Notification: Performance of simCode: created initialization part: time 0.1049/25.88, allocations: 39.13 MB / 8.164 GB, free: 119.3 MB / 0.7453 GB Notification: Performance of simCode: created event and clocks part: time 3.167e-05/25.88, allocations: 15.77 kB / 8.164 GB, free: 119.3 MB / 0.7453 GB Notification: Performance of simCode: created simulation system equations: time 0.02973/25.91, allocations: 12.43 MB / 8.176 GB, free: 118.4 MB / 0.7453 GB Notification: Performance of simCode: created of all other equations (e.g. parameter, nominal, assert, etc): time 0.02155/25.93, allocations: 2.247 MB / 8.179 GB, free: 118.3 MB / 0.7453 GB Notification: Performance of simCode: created linear, non-linear and system jacobian parts: time 0.1125/26.04, allocations: 28.91 MB / 8.207 GB, free: 115 MB / 0.7453 GB Notification: Performance of simCode: some other stuff during SimCode phase: time 0.01697/26.06, allocations: 5.683 MB / 8.212 GB, free: 114.1 MB / 0.7453 GB Notification: Performance of simCode: alias equations: time 0.03257/26.09, allocations: 9.902 MB / 8.222 GB, free: 113.8 MB / 0.7453 GB Notification: Performance of simCode: all other stuff during SimCode phase: time 0.01498/26.11, allocations: 3.856 MB / 8.226 GB, free: 113.8 MB / 0.7453 GB Notification: Performance of SimCode: time 1.193e-06/26.11, allocations: 0 / 8.226 GB, free: 113.8 MB / 0.7453 GB Notification: Performance of buildModelFMU: Generate the FMI files: time 2.253/28.36, allocations: 0.5076 GB / 8.733 GB, free: 139.6 MB / 0.7609 GB Notification: Performance of buildModelFMU: configured platform static using cached values: time 0.0002208/28.36, allocations: 148 kB / 8.734 GB, free: 139.4 MB / 0.7609 GB Notification: Performance of buildModelFMU: Generate platform static: time 18.07/46.44, allocations: 4 kB / 8.734 GB, free: 139.4 MB / 0.7609 GB (rm -f ThermoPower_ThermoPower.Examples.RankineCycle.Simulators.ClosedLoop.pipe ; mkfifo ThermoPower_ThermoPower.Examples.RankineCycle.Simulators.ClosedLoop.pipe ; head -c 1048576 < ThermoPower_ThermoPower.Examples.RankineCycle.Simulators.ClosedLoop.pipe >> ../files/ThermoPower_ThermoPower.Examples.RankineCycle.Simulators.ClosedLoop.sim & /home/hudson/saved_omc/OMSimulator/install/linux/bin/OMSimulator --tempDir=temp_ThermoPower_ThermoPower_Examples_RankineCycle_Simulators_ClosedLoop_fmu --startTime=0 --stopTime=3000 --timeout=50 --tolerance=1e-06 ThermoPower_ThermoPower_Examples_RankineCycle_Simulators_ClosedLoop.fmu > ThermoPower_ThermoPower.Examples.RankineCycle.Simulators.ClosedLoop.pipe 2>&1)