Running: ./testmodel.py --libraries=/home/hudson/saved_omc/libraries/.openmodelica/libraries --ompython_omhome=/usr ClaRa_dev_ClaRa.Basics.ControlVolumes.GasVolumes.Check.TestFlueGasCell_chem.conf.json loadFile("/home/hudson/saved_omc/libraries/.openmodelica/libraries/SMArtIInt 0.2.2-main/package.mo", uses=false) loadFile("/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.8.1-main/package.mo", uses=false) loadFile("/home/hudson/saved_omc/libraries/.openmodelica/libraries/ModelicaServices 4.0.0+maint.om/package.mo", uses=false) loadFile("/home/hudson/saved_omc/libraries/.openmodelica/libraries/Complex 4.0.0+maint.om/package.mo", uses=false) loadFile("/home/hudson/saved_omc/libraries/.openmodelica/libraries/Modelica 4.0.0+maint.om/package.mo", uses=false) loadFile("/home/hudson/saved_omc/libraries/.openmodelica/libraries/ClaRa 1.8.2-main/package.mo", uses=false) Using package ClaRa with version 1.8.2 (/home/hudson/saved_omc/libraries/.openmodelica/libraries/ClaRa 1.8.2-main/package.mo) Using package Modelica with version 4.0.0 (/home/hudson/saved_omc/libraries/.openmodelica/libraries/Modelica 4.0.0+maint.om/package.mo) Using package Complex with version 4.0.0 (/home/hudson/saved_omc/libraries/.openmodelica/libraries/Complex 4.0.0+maint.om/package.mo) Using package ModelicaServices with version 4.0.0 (/home/hudson/saved_omc/libraries/.openmodelica/libraries/ModelicaServices 4.0.0+maint.om/package.mo) Using package TILMedia with version 1.8.1 ClaRa (/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.8.1-main/package.mo) Using package SMArtIInt with version 0.2.2 (/home/hudson/saved_omc/libraries/.openmodelica/libraries/SMArtIInt 0.2.2-main/package.mo) Running command: translateModel(ClaRa.Basics.ControlVolumes.GasVolumes.Check.TestFlueGasCell_chem,tolerance=1e-06,outputFormat="mat",numberOfIntervals=5000,variableFilter="CPUtime|EventCounter|NonlinearSystems.simulation.1..Calls|NonlinearSystems.simulation.1..Iterations|NonlinearSystems.simulation.1..Jacobians|NonlinearSystems.simulation.1..Residues|QFlow.duration|QFlow.height|QFlow.offset|QFlow.startTime|QFlow.y|Temperature.duration|Temperature.height|Temperature.offset|Temperature.startTime|Temperature.y|Time|boundaryGas_pTxi.T_const|boundaryGas_pTxi.contributeToCycleSummary|boundaryGas_pTxi.energyType|boundaryGas_pTxi.eyeOut.T|boundaryGas_pTxi.eyeOut.h|boundaryGas_pTxi.eyeOut.m_flow|boundaryGas_pTxi.eyeOut.p|boundaryGas_pTxi.eyeOut.s|boundaryGas_pTxi.eyeOut.xi.1.|boundaryGas_pTxi.eyeOut.xi.2.|boundaryGas_pTxi.eyeOut.xi.3.|boundaryGas_pTxi.eyeOut.xi.4.|boundaryGas_pTxi.eyeOut.xi.5.|boundaryGas_pTxi.eyeOut.xi.6.|boundaryGas_pTxi.eyeOut.xi.7.|boundaryGas_pTxi.eyeOut.xi.8.|boundaryGas_pTxi.eyeOut.xi.9.|boundaryGas_pTxi.eye_int.1..T|boundaryGas_pTxi.eye_int.1..h|boundaryGas_pTxi.eye_int.1..m_flow|boundaryGas_pTxi.eye_int.1..p|boundaryGas_pTxi.eye_int.1..s|boundaryGas_pTxi.eye_int.1..xi.1.|boundaryGas_pTxi.eye_int.1..xi.2.|boundaryGas_pTxi.eye_int.1..xi.3.|boundaryGas_pTxi.eye_int.1..xi.4.|boundaryGas_pTxi.eye_int.1..xi.5.|boundaryGas_pTxi.eye_int.1..xi.6.|boundaryGas_pTxi.eye_int.1..xi.7.|boundaryGas_pTxi.eye_int.1..xi.8.|boundaryGas_pTxi.eye_int.1..xi.9.|boundaryGas_pTxi.gas_a.T_outflow|boundaryGas_pTxi.gas_a.m_flow|boundaryGas_pTxi.gas_a.p|boundaryGas_pTxi.gas_a.xi_outflow.1.|boundaryGas_pTxi.gas_a.xi_outflow.2.|boundaryGas_pTxi.gas_a.xi_outflow.3.|boundaryGas_pTxi.gas_a.xi_outflow.4.|boundaryGas_pTxi.gas_a.xi_outflow.5.|boundaryGas_pTxi.gas_a.xi_outflow.6.|boundaryGas_pTxi.gas_a.xi_outflow.7.|boundaryGas_pTxi.gas_a.xi_outflow.8.|boundaryGas_pTxi.gas_a.xi_outflow.9.|boundaryGas_pTxi.p|boundaryGas_pTxi.p_const|boundaryGas_pTxi.variable_T|boundaryGas_pTxi.variable_p|boundaryGas_pTxi.variable_xi|boundaryGas_pTxi.xi_const.1.|boundaryGas_pTxi.xi_const.2.|boundaryGas_pTxi.xi_const.3.|boundaryGas_pTxi.xi_const.4.|boundaryGas_pTxi.xi_const.5.|boundaryGas_pTxi.xi_const.6.|boundaryGas_pTxi.xi_const.7.|boundaryGas_pTxi.xi_const.8.|boundaryGas_pTxi.xi_const.9.|dP.duration|dP.height|dP.offset|dP.startTime|dP.y|idealGasFlowSource_XRG.T|idealGasFlowSource_XRG.T_const|idealGasFlowSource_XRG.contributeToCycleSummary|idealGasFlowSource_XRG.energyType|idealGasFlowSource_XRG.eyeOut.T|idealGasFlowSource_XRG.eyeOut.h|idealGasFlowSource_XRG.eyeOut.m_flow|idealGasFlowSource_XRG.eyeOut.p|idealGasFlowSource_XRG.eyeOut.s|idealGasFlowSource_XRG.eyeOut.xi.1.|idealGasFlowSource_XRG.eyeOut.xi.2.|idealGasFlowSource_XRG.eyeOut.xi.3.|idealGasFlowSource_XRG.eyeOut.xi.4.|idealGasFlowSource_XRG.eyeOut.xi.5.|idealGasFlowSource_XRG.eyeOut.xi.6.|idealGasFlowSource_XRG.eyeOut.xi.7.|idealGasFlowSource_XRG.eyeOut.xi.8.|idealGasFlowSource_XRG.eyeOut.xi.9.|idealGasFlowSource_XRG.eye_int.1..T|idealGasFlowSource_XRG.eye_int.1..h|idealGasFlowSource_XRG.eye_int.1..m_flow|idealGasFlowSource_XRG.eye_int.1..p|idealGasFlowSource_XRG.eye_int.1..s|idealGasFlowSource_XRG.eye_int.1..xi.1.|idealGasFlowSource_XRG.eye_int.1..xi.2.|idealGasFlowSource_XRG.eye_int.1..xi.3.|idealGasFlowSource_XRG.eye_int.1..xi.4.|idealGasFlowSource_XRG.eye_int.1..xi.5.|idealGasFlowSource_XRG.eye_int.1..xi.6.|idealGasFlowSource_XRG.eye_int.1..xi.7.|idealGasFlowSource_XRG.eye_int.1..xi.8.|idealGasFlowSource_XRG.eye_int.1..xi.9.|idealGasFlowSource_XRG.gas_a.T_outflow|idealGasFlowSource_XRG.gas_a.m_flow|idealGasFlowSource_XRG.gas_a.p|idealGasFlowSource_XRG.gas_a.xi_outflow.1.|idealGasFlowSource_XRG.gas_a.xi_outflow.2.|idealGasFlowSource_XRG.gas_a.xi_outflow.3.|idealGasFlowSource_XRG.gas_a.xi_outflow.4.|idealGasFlowSource_XRG.gas_a.xi_outflow.5.|idealGasFlowSource_XRG.gas_a.xi_outflow.6.|idealGasFlowSource_XRG.gas_a.xi_outflow.7.|idealGasFlowSource_XRG.gas_a.xi_outflow.8.|idealGasFlowSource_XRG.gas_a.xi_outflow.9.|idealGasFlowSource_XRG.m_flow|idealGasFlowSource_XRG.m_flow_const|idealGasFlowSource_XRG.variable_T|idealGasFlowSource_XRG.variable_m_flow|idealGasFlowSource_XRG.variable_xi|idealGasFlowSource_XRG.xi_const.1.|idealGasFlowSource_XRG.xi_const.2.|idealGasFlowSource_XRG.xi_const.3.|idealGasFlowSource_XRG.xi_const.4.|idealGasFlowSource_XRG.xi_const.5.|idealGasFlowSource_XRG.xi_const.6.|idealGasFlowSource_XRG.xi_const.7.|idealGasFlowSource_XRG.xi_const.8.|idealGasFlowSource_XRG.xi_const.9.|massFlowRate.duration|massFlowRate.height|massFlowRate.offset|massFlowRate.startTime|massFlowRate.y|massFlowRate1.duration|massFlowRate1.height|massFlowRate1.offset|massFlowRate1.startTime|massFlowRate1.y|prescribedHeatFlow.Q_flow|prescribedHeatFlow.T_ref|prescribedHeatFlow.alpha|prescribedHeatFlow.port.Q_flow|prescribedHeatFlow.port.T|simCenter.MaxSimTime|simCenter.T_amb|simCenter.T_amb_start|simCenter.contributeToCycleSummary|simCenter.cycleSumPort.power_aux|simCenter.cycleSumPort.power_in|simCenter.cycleSumPort.pow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ck.TestFlueGasCell_chem") 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ck.TestFlueGasCell_chem") 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0.7368 GB, free: 9.125 MB / 0.5294 GB [/home/hudson/saved_omc/libraries/.openmodelica/libraries/ClaRa 1.8.2-main/SimCenter.mo:69:5-70:35: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 0.003328/0.5685, allocations: 1.035 MB / 0.7378 GB, free: 8.453 MB / 0.5294 GB [/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.8.1-main/GasFunctions.mo:243:23-247:26:writable] Warning: Pure function 'TILMedia.GasFunctions.specificEnthalpy_pTxi' contains a call to impure function 'TILMedia.Internals.GasFunctions.specificEnthalpy_pTxi'. Notification: Performance of NFTyping.typeBindings: time 0.003585/0.5721, allocations: 0.97 MB / 0.7388 GB, free: 7.68 MB / 0.5294 GB Notification: Performance of NFTyping.typeClassSections: time 0.003892/0.576, allocations: 1.306 MB / 0.7401 GB, free: 6.633 MB / 0.5294 GB Notification: Performance of NFFlatten.flatten: time 0.00552/0.5816, allocations: 2.82 MB / 0.7428 GB, free: 4.949 MB / 0.5294 GB Notification: Performance of NFFlatten.resolveConnections: time 0.003194/0.5848, allocations: 2.393 MB / 0.7452 GB, free: 2.504 MB / 0.5294 GB Notification: Performance of NFEvalConstants.evaluate: time 0.002866/0.5877, allocations: 1.523 MB / 0.7466 GB, free: 0.9766 MB / 0.5294 GB Notification: Performance of NFSimplifyModel.simplify: time 0.003628/0.5914, allocations: 2.552 MB / 0.7491 GB, free: 14.42 MB / 0.545 GB Notification: Performance of NFPackage.collectConstants: time 0.001225/0.5926, allocations: 0.6172 MB / 0.7497 GB, free: 13.8 MB / 0.545 GB Notification: Performance of NFFlatten.collectFunctions: time 0.004895/0.5975, allocations: 2.291 MB / 0.752 GB, free: 11.51 MB / 0.545 GB Notification: Performance of NFScalarize.scalarize: time 0.002855/0.6004, allocations: 2.662 MB / 0.7546 GB, free: 8.84 MB / 0.545 GB Notification: Performance of NFVerifyModel.verify: time 0.004456/0.6049, allocations: 2.975 MB / 0.7575 GB, free: 5.852 MB / 0.545 GB Notification: Performance of NFConvertDAE.convert: time 0.01387/0.6188, allocations: 10.12 MB / 0.7674 GB, free: 11.7 MB / 0.5607 GB Notification: Performance of FrontEnd - DAE generated: time 7.534e-06/0.6188, allocations: 4 kB / 0.7674 GB, free: 11.7 MB / 0.5607 GB Notification: Performance of FrontEnd: time 1.924e-06/0.6188, allocations: 0 / 0.7674 GB, free: 11.7 MB / 0.5607 GB Notification: Performance of Transformations before backend: time 0.0002091/0.6191, allocations: 0 / 0.7674 GB, free: 11.7 MB / 0.5607 GB Notification: Model statistics after passing the front-end and creating the data structures used by the back-end: * Number of equations: 550 * Number of variables: 550 Notification: Performance of Generate backend data structure: time 0.01839/0.6375, allocations: 7.038 MB / 0.7742 GB, free: 4.57 MB / 0.5607 GB Notification: Performance of prepare preOptimizeDAE: time 5.004e-05/0.6375, allocations: 12.03 kB / 0.7743 GB, free: 4.559 MB / 0.5607 GB Notification: Performance of preOpt normalInlineFunction (simulation): time 0.002029/0.6396, allocations: 0.6105 MB / 0.7748 GB, free: 3.945 MB / 0.5607 GB Notification: Performance of preOpt evaluateParameters (simulation): time 0.01291/0.6525, allocations: 7.24 MB / 0.7819 GB, free: 12.63 MB / 0.5763 GB Notification: Performance of preOpt simplifyIfEquations (simulation): time 0.0001797/0.6527, allocations: 137 kB / 0.782 GB, free: 12.49 MB / 0.5763 GB Notification: Performance of preOpt expandDerOperator (simulation): time 0.000636/0.6534, allocations: 144.3 kB / 0.7822 GB, free: 12.35 MB / 0.5763 GB Notification: Performance of preOpt clockPartitioning (simulation): time 0.007627/0.661, allocations: 5.754 MB / 0.7878 GB, free: 6 MB / 0.5763 GB Notification: Performance of preOpt findStateOrder (simulation): time 3.034e-05/0.661, allocations: 3.938 kB / 0.7878 GB, free: 5.996 MB / 0.5763 GB Notification: Performance of preOpt replaceEdgeChange (simulation): time 0.000288/0.6613, allocations: 84 kB / 0.7879 GB, free: 5.914 MB / 0.5763 GB Notification: Performance of preOpt inlineArrayEqn (simulation): time 0.0001857/0.6615, allocations: 191.1 kB / 0.7881 GB, free: 5.727 MB / 0.5763 GB Notification: Performance of preOpt removeEqualRHS (simulation): time 0.01001/0.6715, allocations: 6.896 MB / 0.7948 GB, free: 14.82 MB / 0.5919 GB Notification: Performance of preOpt removeSimpleEquations (simulation): time 0.02372/0.6953, allocations: 15.16 MB / 0.8096 GB, free: 15.48 MB / 0.6075 GB Notification: Performance of preOpt comSubExp (simulation): time 0.005219/0.7006, allocations: 4.05 MB / 0.8136 GB, free: 11.39 MB / 0.6075 GB Notification: Performance of preOpt resolveLoops (simulation): time 0.004022/0.7046, allocations: 3.21 MB / 0.8167 GB, free: 8.172 MB / 0.6075 GB Notification: Performance of preOpt evalFunc (simulation): time 0.0003216/0.705, allocations: 53.84 kB / 0.8168 GB, free: 8.125 MB / 0.6075 GB Notification: Performance of preOpt encapsulateWhenConditions (simulation): time 5.053e-05/0.705, allocations: 52.56 kB / 0.8168 GB, free: 8.062 MB / 0.6075 GB Notification: Performance of pre-optimization done (n=296): time 5.03e-06/0.705, allocations: 4 kB / 0.8168 GB, free: 8.059 MB / 0.6075 GB Notification: Performance of matching and sorting (n=297): time 0.03075/0.7358, allocations: 18.73 MB / 0.8351 GB, free: 5.164 MB / 0.6232 GB Notification: Performance of inlineWhenForInitialization (initialization): time 0.0001003/0.7359, allocations: 154.5 kB / 0.8352 GB, free: 4.98 MB / 0.6232 GB Notification: Performance of selectInitializationVariablesDAE (initialization): time 0.006392/0.7423, allocations: 4.328 MB / 0.8395 GB, free: 0.6562 MB / 0.6232 GB Notification: Performance of collectPreVariables (initialization): time 0.0004261/0.7428, allocations: 53.7 kB / 0.8395 GB, free: 0.5977 MB / 0.6232 GB Notification: Performance of collectInitialEqns (initialization): time 0.001516/0.7443, allocations: 1.774 MB / 0.8413 GB, free: 14.82 MB / 0.6388 GB Notification: Performance of collectInitialBindings (initialization): time 0.0009786/0.7453, allocations: 1.015 MB / 0.8422 GB, free: 13.79 MB / 0.6388 GB Notification: Performance of simplifyInitialFunctions (initialization): time 0.0009923/0.7463, allocations: 484.8 kB / 0.8427 GB, free: 13.32 MB / 0.6388 GB Notification: Performance of setup shared object (initialization): time 0.0001172/0.7464, allocations: 301.1 kB / 0.843 GB, free: 13.02 MB / 0.6388 GB Notification: Performance of preBalanceInitialSystem (initialization): time 0.004048/0.7505, allocations: 2.831 MB / 0.8458 GB, free: 10.18 MB / 0.6388 GB Notification: Performance of partitionIndependentBlocks (initialization): time 0.004349/0.7548, allocations: 3.176 MB / 0.8489 GB, free: 6.902 MB / 0.6388 GB Notification: Performance of analyzeInitialSystem (initialization): time 0.09632/0.8512, allocations: 28.71 MB / 0.8769 GB, free: 10.02 MB / 0.67 GB Notification: Performance of solveInitialSystemEqSystem (initialization): time 1.564e-05/0.8512, allocations: 7.938 kB / 0.8769 GB, free: 10.01 MB / 0.67 GB Notification: Performance of matching and sorting (n=349) (initialization): time 0.01491/0.8661, allocations: 7.834 MB / 0.8846 GB, free: 2.141 MB / 0.67 GB Notification: Performance of prepare postOptimizeDAE: time 3.178e-05/0.8662, allocations: 12.25 kB / 0.8846 GB, free: 2.129 MB / 0.67 GB Notification: Performance of postOpt simplifyComplexFunction (initialization): time 7.876e-05/0.8663, allocations: 27.98 kB / 0.8846 GB, free: 2.102 MB / 0.67 GB Notification: Performance of postOpt tearingSystem (initialization): time 0.003928/0.8702, allocations: 1.902 MB / 0.8864 GB, free: 196 kB / 0.67 GB Notification: Performance of postOpt solveSimpleEquations (initialization): time 0.006246/0.8765, allocations: 0.5578 MB / 0.887 GB, free: 15.63 MB / 0.6857 GB Notification: Performance of postOpt calculateStrongComponentJacobians (initialization): time 0.00247/0.879, allocations: 1.94 MB / 0.8889 GB, free: 13.67 MB / 0.6857 GB Notification: Performance of postOpt simplifyAllExpressions (initialization): time 0.003026/0.882, allocations: 111.8 kB / 0.889 GB, free: 13.56 MB / 0.6857 GB Notification: Performance of postOpt collapseArrayExpressions (initialization): time 0.0004183/0.8824, allocations: 100 kB / 0.8891 GB, free: 13.46 MB / 0.6857 GB Warning: Assuming fixed start value for the following 10 variables: volumeGas_L2_chem.bulk.h:VARIABLE(start = volumeGas_L2_chem.h_start unit = "J/kg" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer ) "Specific enthalpy" type: Real volumeGas_L2_chem.bulk.xi[1]:VARIABLE(min = 0.0 max = 1.0 start = volumeGas_L2_chem.xi_start[1] unit = "1" fixed = true nominal = 1.0 stateSelect=StateSelect.prefer ) "Mass fraction" type: Real [9] volumeGas_L2_chem.bulk.xi[2]:VARIABLE(min = 0.0 max = 1.0 start = volumeGas_L2_chem.xi_start[2] unit = "1" fixed = true nominal = 1.0 stateSelect=StateSelect.prefer ) "Mass fraction" type: Real [9] volumeGas_L2_chem.bulk.xi[3]:VARIABLE(min = 0.0 max = 1.0 start = volumeGas_L2_chem.xi_start[3] unit = "1" fixed = true nominal = 1.0 stateSelect=StateSelect.prefer ) "Mass fraction" type: Real [9] volumeGas_L2_chem.bulk.xi[4]:VARIABLE(min = 0.0 max = 1.0 start = volumeGas_L2_chem.xi_start[4] unit = "1" fixed = true nominal = 1.0 stateSelect=StateSelect.prefer ) "Mass fraction" type: Real [9] volumeGas_L2_chem.bulk.xi[5]:VARIABLE(min = 0.0 max = 1.0 start = volumeGas_L2_chem.xi_start[5] unit = "1" fixed = true nominal = 1.0 stateSelect=StateSelect.prefer ) "Mass fraction" type: Real [9] volumeGas_L2_chem.bulk.xi[6]:VARIABLE(min = 0.0 max = 1.0 start = volumeGas_L2_chem.xi_start[6] unit = "1" fixed = true nominal = 1.0 stateSelect=StateSelect.prefer ) "Mass fraction" type: Real [9] volumeGas_L2_chem.bulk.xi[7]:VARIABLE(min = 0.0 max = 1.0 start = volumeGas_L2_chem.xi_start[7] unit = "1" fixed = true nominal = 1.0 stateSelect=StateSelect.prefer ) "Mass fraction" type: Real [9] volumeGas_L2_chem.bulk.xi[8]:VARIABLE(min = 0.0 max = 1.0 start = volumeGas_L2_chem.xi_start[8] unit = "1" fixed = true nominal = 1.0 stateSelect=StateSelect.prefer ) "Mass fraction" type: Real [9] volumeGas_L2_chem.bulk.xi[9]:VARIABLE(min = 0.0 max = 1.0 start = volumeGas_L2_chem.xi_start[9] unit = "1" fixed = true nominal = 1.0 stateSelect=StateSelect.prefer ) "Mass fraction" type: Real [9] Notification: Model statistics after passing the back-end for initialization: * Number of independent subsystems: 32 * 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 (205): * Single equations (assignments): 195 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 9 * When equations: 0 * If-equations: 0 * Equation systems (not torn): 0 * Torn equation systems: 1 * Mixed (continuous/discrete) equation systems: 0 Notification: Torn system details for strict tearing set: * Linear torn systems (#iteration vars, #inner vars, density): 0 systems * Non-linear torn systems (#iteration vars, #inner vars): 1 system {(1,27)} Notification: Performance of prepare postOptimizeDAE: time 0.002904/0.8854, allocations: 1.431 MB / 0.8905 GB, free: 12.03 MB / 0.6857 GB Notification: Performance of postOpt lateInlineFunction (simulation): time 0.001/0.8864, allocations: 484.7 kB / 0.8909 GB, free: 11.55 MB / 0.6857 GB Notification: Performance of postOpt wrapFunctionCalls (simulation): time 0.01203/0.8984, allocations: 7.343 MB / 0.8981 GB, free: 4.156 MB / 0.6857 GB Notification: Performance of postOpt simplifysemiLinear (simulation): time 2.99e-05/0.8985, allocations: 15.94 kB / 0.8981 GB, free: 4.141 MB / 0.6857 GB Notification: Performance of postOpt simplifyComplexFunction (simulation): time 5.299e-05/0.8985, allocations: 19.94 kB / 0.8982 GB, free: 4.121 MB / 0.6857 GB Notification: Performance of postOpt removeConstants (simulation): time 0.002418/0.901, allocations: 1.13 MB / 0.8993 GB, free: 2.969 MB / 0.6857 GB Notification: Performance of postOpt simplifyTimeIndepFuncCalls (simulation): time 0.0005997/0.9016, allocations: 43.98 kB / 0.8993 GB, free: 2.926 MB / 0.6857 GB Notification: Performance of postOpt simplifyAllExpressions (simulation): time 0.001847/0.9034, allocations: 83.91 kB / 0.8994 GB, free: 2.844 MB / 0.6857 GB Notification: Performance of postOpt findZeroCrossings (simulation): time 0.0004977/0.9039, allocations: 133.8 kB / 0.8995 GB, free: 2.711 MB / 0.6857 GB [/var/lib/jenkins1/ws/OpenModelicaLibraryTestingWork/OpenModelica/OMCompiler/Compiler/BackEnd/DAEMode.mo:528:7-530:90:writable] Error: Internal error DAEMode.traverserStrongComponents failed on equation: 1/1 (24): (volumeGas_L2_chem.flueGasOutlet.d, volumeGas_L2_chem.flueGasOutlet.kappa, volumeGas_L2_chem.flueGasOutlet.drhodp_hxi, volumeGas_L2_chem.flueGasOutlet.drhodh_pxi, volumeGas_L2_chem.flueGasOutlet.drhodxi_ph, volumeGas_L2_chem.flueGasOutlet.p_i, volumeGas_L2_chem.flueGasOutlet.xi_gas) = TILMedia.Internals.GasObjectFunctions.additionalProperties_pTxi(volumeGas_L2_chem.bulk.p, volumeGas_L2_chem.flueGasOutlet.T, volumeGas_L2_chem.flueGasOutlet.xi, volumeGas_L2_chem.flueGasOutlet.gasPointer) Variables: 1: volumeGas_L2_chem.flueGasOutlet.p_i[5]:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 ) "Partial pressure" type: Real [10] 2: volumeGas_L2_chem.flueGasOutlet.kappa:VARIABLE(unit = "1/Pa" ) "Isothermal compressibility" type: Real 3: volumeGas_L2_chem.flueGasOutlet.drhodp_hxi:VARIABLE(unit = "s2/m2" ) "Derivative of density wrt pressure at specific enthalpy and mass fraction" type: Real 4: volumeGas_L2_chem.flueGasOutlet.p_i[1]:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 ) "Partial pressure" type: Real [10] 5: volumeGas_L2_chem.flueGasOutlet.drhodxi_ph[4]:VARIABLE(unit = "kg/(m3)" ) "Derivative of density wrt mass fraction of water at constant pressure and specific enthalpy" type: Real [9] 6: volumeGas_L2_chem.flueGasOutlet.p_i[8]:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 ) "Partial pressure" type: Real [10] 7: volumeGas_L2_chem.flueGasOutlet.xi_gas:VARIABLE(min = 0.0 max = 1.0 unit = "1" ) "Mass fraction of gasoues condensing component" type: Real 8: volumeGas_L2_chem.flueGasOutlet.p_i[3]:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 ) "Partial pressure" type: Real [10] 9: volumeGas_L2_chem.flueGasOutlet.p_i[7]:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 ) "Partial pressure" type: Real [10] 10: volumeGas_L2_chem.flueGasOutlet.drhodxi_ph[7]:VARIABLE(unit = "kg/(m3)" ) "Derivative of density wrt mass fraction of water at constant pressure and specific enthalpy" type: Real [9] 11: volumeGas_L2_chem.flueGasOutlet.p_i[6]:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 ) "Partial pressure" type: Real [10] 12: volumeGas_L2_chem.flueGasOutlet.p_i[9]:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 ) "Partial pressure" type: Real [10] 13: volumeGas_L2_chem.flueGasOutlet.drhodxi_ph[1]:VARIABLE(unit = "kg/(m3)" ) "Derivative of density wrt mass fraction of water at constant pressure and specific enthalpy" type: Real [9] 14: volumeGas_L2_chem.flueGasOutlet.p_i[4]:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 ) "Partial pressure" type: Real [10] 15: volumeGas_L2_chem.flueGasOutlet.drhodxi_ph[6]:VARIABLE(unit = "kg/(m3)" ) "Derivative of density wrt mass fraction of water at constant pressure and specific enthalpy" type: Real [9] 16: volumeGas_L2_chem.flueGasOutlet.drhodxi_ph[2]:VARIABLE(unit = "kg/(m3)" ) "Derivative of density wrt mass fraction of water at constant pressure and specific enthalpy" type: Real [9] 17: volumeGas_L2_chem.flueGasOutlet.drhodxi_ph[3]:VARIABLE(unit = "kg/(m3)" ) "Derivative of density wrt mass fraction of water at constant pressure and specific enthalpy" type: Real [9] 18: volumeGas_L2_chem.flueGasOutlet.drhodxi_ph[8]:VARIABLE(unit = "kg/(m3)" ) "Derivative of density wrt mass fraction of water at constant pressure and specific enthalpy" type: Real [9] 19: volumeGas_L2_chem.flueGasOutlet.d:VARIABLE(min = 0.0 unit = "kg/m3" ) "Density" type: Real 20: volumeGas_L2_chem.flueGasOutlet.drhodxi_ph[5]:VARIABLE(unit = "kg/(m3)" ) "Derivative of density wrt mass fraction of water at constant pressure and specific enthalpy" type: Real [9] 21: volumeGas_L2_chem.flueGasOutlet.p_i[2]:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 ) "Partial pressure" type: Real [10] 22: volumeGas_L2_chem.flueGasOutlet.drhodh_pxi:VARIABLE(unit = "kg.s2/m5" ) "Derivative of density wrt specific enthalpy at constant pressure and mass fraction" type: Real 23: volumeGas_L2_chem.flueGasOutlet.drhodxi_ph[9]:VARIABLE(unit = "kg/(m3)" ) "Derivative of density wrt mass fraction of water at constant pressure and specific enthalpy" type: Real [9] 24: volumeGas_L2_chem.flueGasOutlet.p_i[10]:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 ) "Partial pressure" type: Real [10] [/var/lib/jenkins1/ws/OpenModelicaLibraryTestingWork/OpenModelica/OMCompiler/Compiler/BackEnd/DAEMode.mo:528:7-530:90:writable] Error: Internal error DAEMode.traverserStrongComponents failed on equation: 1/1 (1): volumeGas_L2_chem.chemicalReactions.V_flow = if volumeGas_L2_chem.chemicalReactions.m_flow_aux > 0.0 and volumeGas_L2_chem.outlet.m_flow <= 0.0 then volumeGas_L2_chem.iCom.V_flow_in else if volumeGas_L2_chem.chemicalReactions.m_flow_aux > 0.0 then volumeGas_L2_chem.iCom.V_flow_in + volumeGas_L2_chem.iCom.V_flow_out else if volumeGas_L2_chem.chemicalReactions.m_flow_aux <= 0.0 and volumeGas_L2_chem.outlet.m_flow <= 0.0 then 1e-20 else volumeGas_L2_chem.iCom.V_flow_out 2/2 (1): volumeGas_L2_chem.iCom.V_flow_out = abs(volumeGas_L2_chem.outlet.m_flow / volumeGas_L2_chem.flueGasOutlet.d) 3/3 (1): volumeGas_L2_chem.flueGasOutlet.T = if noEvent(volumeGas_L2_chem.outlet.m_flow > 0.0) then boundaryGas_pTxi.T_const else volumeGas_L2_chem.bulk.T 4/4 (24): (volumeGas_L2_chem.flueGasOutlet.d, volumeGas_L2_chem.flueGasOutlet.kappa, volumeGas_L2_chem.flueGasOutlet.drhodp_hxi, volumeGas_L2_chem.flueGasOutlet.drhodh_pxi, volumeGas_L2_chem.flueGasOutlet.drhodxi_ph, volumeGas_L2_chem.flueGasOutlet.p_i, volumeGas_L2_chem.flueGasOutlet.xi_gas) = TILMedia.Internals.GasObjectFunctions.additionalProperties_pTxi(volumeGas_L2_chem.bulk.p, volumeGas_L2_chem.flueGasOutlet.T, volumeGas_L2_chem.flueGasOutlet.xi, volumeGas_L2_chem.flueGasOutlet.gasPointer) 5/28 (1): volumeGas_L2_chem.flueGasOutlet.h = TILMedia.Internals.GasObjectFunctions.specificEnthalpy_pTxi(volumeGas_L2_chem.bulk.p, volumeGas_L2_chem.flueGasOutlet.T, volumeGas_L2_chem.flueGasOutlet.xi, volumeGas_L2_chem.flueGasOutlet.gasPointer) 6/29 (1): der(volumeGas_L2_chem.bulk.h) = (volumeGas_L2_chem.chemicalReactions.m_flow_aux * (volumeGas_L2_chem.chemicalReactions.h_aux - volumeGas_L2_chem.bulk.h) + volumeGas_L2_chem.outlet.m_flow * (volumeGas_L2_chem.flueGasOutlet.h - volumeGas_L2_chem.bulk.h) + volumeGas_L2_chem.geo.volume * $DER.volumeGas_L2_chem.bulk.p + volumeGas_L2_chem.summary.outline.Q_flow_tot + volumeGas_L2_chem.chemicalReactions.m_flow_reaction[1] * (volumeGas_L2_chem.chemicalReactions.h_reaction[1] - volumeGas_L2_chem.bulk.h)) / volumeGas_L2_chem.chemicalReactions.mass 7/30 (1): volumeGas_L2_chem.drhodt = volumeGas_L2_chem.bulk.drhodh_pxi * der(volumeGas_L2_chem.bulk.h) + volumeGas_L2_chem.bulk.drhodp_hxi * $DER.volumeGas_L2_chem.bulk.p + volumeGas_L2_chem.bulk.drhodxi_ph[1] * der(volumeGas_L2_chem.bulk.xi[1]) + volumeGas_L2_chem.bulk.drhodxi_ph[2] * der(volumeGas_L2_chem.bulk.xi[2]) + volumeGas_L2_chem.bulk.drhodxi_ph[3] * der(volumeGas_L2_chem.bulk.xi[3]) + volumeGas_L2_chem.bulk.drhodxi_ph[4] * der(volumeGas_L2_chem.bulk.xi[4]) + volumeGas_L2_chem.bulk.drhodxi_ph[5] * der(volumeGas_L2_chem.bulk.xi[5]) + volumeGas_L2_chem.bulk.drhodxi_ph[6] * der(volumeGas_L2_chem.bulk.xi[6]) + volumeGas_L2_chem.bulk.drhodxi_ph[7] * der(volumeGas_L2_chem.bulk.xi[7]) + volumeGas_L2_chem.bulk.drhodxi_ph[8] * der(volumeGas_L2_chem.bulk.xi[8]) + volumeGas_L2_chem.bulk.drhodxi_ph[9] * der(volumeGas_L2_chem.bulk.xi[9]) 8/31 (1): der(volumeGas_L2_chem.bulk.xi[2]) = (volumeGas_L2_chem.chemicalReactions.m_flow_aux * (volumeGas_L2_chem.chemicalReactions.xi_aux[2] - volumeGas_L2_chem.bulk.xi[2]) + volumeGas_L2_chem.outlet.m_flow * (volumeGas_L2_chem.flueGasOutlet.xi[2] - volumeGas_L2_chem.bulk.xi[2]) - volumeGas_L2_chem.chemicalReactions.m_flow_reaction[1] * volumeGas_L2_chem.bulk.xi[2]) / volumeGas_L2_chem.chemicalReactions.mass 9/32 (1): volumeGas_L2_chem.chemicalReactions.m_flow_aux + volumeGas_L2_chem.outlet.m_flow + volumeGas_L2_chem.chemicalReactions.m_flow_reaction[1] = volumeGas_L2_chem.drhodt * volumeGas_L2_chem.geo.volume 10/33 (1): der(volumeGas_L2_chem.bulk.xi[9]) = (volumeGas_L2_chem.chemicalReactions.m_flow_aux * (volumeGas_L2_chem.chemicalReactions.xi_aux[9] - volumeGas_L2_chem.bulk.xi[9]) + volumeGas_L2_chem.outlet.m_flow * (volumeGas_L2_chem.flueGasOutlet.xi[9] - volumeGas_L2_chem.bulk.xi[9]) - volumeGas_L2_chem.chemicalReactions.m_flow_reaction[1] * volumeGas_L2_chem.bulk.xi[9]) / volumeGas_L2_chem.chemicalReactions.mass 11/34 (1): der(volumeGas_L2_chem.bulk.xi[8]) = (volumeGas_L2_chem.chemicalReactions.m_flow_aux * (volumeGas_L2_chem.chemicalReactions.xi_aux[8] - volumeGas_L2_chem.bulk.xi[8]) + volumeGas_L2_chem.outlet.m_flow * (volumeGas_L2_chem.flueGasOutlet.xi[8] - volumeGas_L2_chem.bulk.xi[8]) - volumeGas_L2_chem.chemicalReactions.m_flow_reaction[1] * volumeGas_L2_chem.bulk.xi[8]) / volumeGas_L2_chem.chemicalReactions.mass 12/35 (1): der(volumeGas_L2_chem.bulk.xi[7]) = (volumeGas_L2_chem.chemicalReactions.m_flow_aux * (volumeGas_L2_chem.chemicalReactions.xi_aux[7] - volumeGas_L2_chem.bulk.xi[7]) + volumeGas_L2_chem.outlet.m_flow * (volumeGas_L2_chem.flueGasOutlet.xi[7] - volumeGas_L2_chem.bulk.xi[7]) - volumeGas_L2_chem.chemicalReactions.m_flow_reaction[1] * volumeGas_L2_chem.bulk.xi[7]) / volumeGas_L2_chem.chemicalReactions.mass 13/36 (1): der(volumeGas_L2_chem.bulk.xi[6]) = (volumeGas_L2_chem.chemicalReactions.m_flow_aux * (volumeGas_L2_chem.chemicalReactions.xi_aux[6] - volumeGas_L2_chem.bulk.xi[6]) + volumeGas_L2_chem.outlet.m_flow * (volumeGas_L2_chem.flueGasOutlet.xi[6] - volumeGas_L2_chem.bulk.xi[6]) - volumeGas_L2_chem.chemicalReactions.m_flow_reaction[1] * volumeGas_L2_chem.bulk.xi[6]) / volumeGas_L2_chem.chemicalReactions.mass 14/37 (1): der(volumeGas_L2_chem.bulk.xi[5]) = (volumeGas_L2_chem.chemicalReactions.m_flow_aux * (volumeGas_L2_chem.chemicalReactions.xi_aux[5] - volumeGas_L2_chem.bulk.xi[5]) + volumeGas_L2_chem.outlet.m_flow * (volumeGas_L2_chem.flueGasOutlet.xi[5] - volumeGas_L2_chem.bulk.xi[5]) + volumeGas_L2_chem.chemicalReactions.m_flow_reaction[1] * (1e-5 - volumeGas_L2_chem.bulk.xi[5])) / volumeGas_L2_chem.chemicalReactions.mass 15/38 (1): der(volumeGas_L2_chem.bulk.xi[4]) = (volumeGas_L2_chem.chemicalReactions.m_flow_aux * (volumeGas_L2_chem.chemicalReactions.xi_aux[4] - volumeGas_L2_chem.bulk.xi[4]) + volumeGas_L2_chem.outlet.m_flow * (volumeGas_L2_chem.flueGasOutlet.xi[4] - volumeGas_L2_chem.bulk.xi[4]) - volumeGas_L2_chem.chemicalReactions.m_flow_reaction[1] * volumeGas_L2_chem.bulk.xi[4]) / volumeGas_L2_chem.chemicalReactions.mass 16/39 (1): der(volumeGas_L2_chem.bulk.xi[3]) = (volumeGas_L2_chem.chemicalReactions.m_flow_aux * (volumeGas_L2_chem.chemicalReactions.xi_aux[3] - volumeGas_L2_chem.bulk.xi[3]) + volumeGas_L2_chem.outlet.m_flow * (volumeGas_L2_chem.flueGasOutlet.xi[3] - volumeGas_L2_chem.bulk.xi[3]) - volumeGas_L2_chem.chemicalReactions.m_flow_reaction[1] * volumeGas_L2_chem.bulk.xi[3]) / volumeGas_L2_chem.chemicalReactions.mass 17/40 (1): der(volumeGas_L2_chem.bulk.xi[1]) = (volumeGas_L2_chem.chemicalReactions.m_flow_aux * (volumeGas_L2_chem.chemicalReactions.xi_aux[1] - volumeGas_L2_chem.bulk.xi[1]) + volumeGas_L2_chem.outlet.m_flow * (volumeGas_L2_chem.flueGasOutlet.xi[1] - volumeGas_L2_chem.bulk.xi[1]) + volumeGas_L2_chem.chemicalReactions.m_flow_reaction[1] * (0.99999 - volumeGas_L2_chem.bulk.xi[1])) / volumeGas_L2_chem.chemicalReactions.mass 18/41 (1): volumeGas_L2_chem.chemicalReactions.m_flow_reaction[1] = if volumeGas_L2_chem.chemicalReactions.m_flow_aux > 0.0 and volumeGas_L2_chem.outlet.m_flow <= 0.0 then volumeGas_L2_chem.chemicalReactions.separationRate * (-volumeGas_L2_chem.chemicalReactions.xi_aux[1]) * volumeGas_L2_chem.chemicalReactions.m_flow_aux else if volumeGas_L2_chem.chemicalReactions.m_flow_aux > 0.0 then volumeGas_L2_chem.chemicalReactions.separationRate * ((-volumeGas_L2_chem.flueGasOutlet.xi[1]) * volumeGas_L2_chem.outlet.m_flow - volumeGas_L2_chem.chemicalReactions.xi_aux[1] * volumeGas_L2_chem.chemicalReactions.m_flow_aux) else if volumeGas_L2_chem.chemicalReactions.m_flow_aux <= 0.0 and volumeGas_L2_chem.outlet.m_flow <= 0.0 then 1e-20 else volumeGas_L2_chem.chemicalReactions.separationRate * (-volumeGas_L2_chem.flueGasOutlet.xi[1]) * volumeGas_L2_chem.outlet.m_flow 19/42 (1): volumeGas_L2_chem.chemicalReactions.separationRate = 1.0 - $cse2 20/43 (1): $cse2 = exp((-volumeGas_L2_chem.chemicalReactions.w_m) * volumeGas_L2_chem.chemicalReactions.A_filter / volumeGas_L2_chem.chemicalReactions.V_flow) 21/44 (1): volumeGas_L2_chem.flueGasOutlet.xi[9] = if noEvent(volumeGas_L2_chem.outlet.m_flow > 0.0) then boundaryGas_pTxi.xi_const[9] else volumeGas_L2_chem.bulk.xi[9] 22/45 (1): volumeGas_L2_chem.flueGasOutlet.xi[8] = if noEvent(volumeGas_L2_chem.outlet.m_flow > 0.0) then boundaryGas_pTxi.xi_const[8] else volumeGas_L2_chem.bulk.xi[8] 23/46 (1): volumeGas_L2_chem.flueGasOutlet.xi[7] = if noEvent(volumeGas_L2_chem.outlet.m_flow > 0.0) then boundaryGas_pTxi.xi_const[7] else volumeGas_L2_chem.bulk.xi[7] 24/47 (1): volumeGas_L2_chem.flueGasOutlet.xi[6] = if noEvent(volumeGas_L2_chem.outlet.m_flow > 0.0) then boundaryGas_pTxi.xi_const[6] else volumeGas_L2_chem.bulk.xi[6] 25/48 (1): volumeGas_L2_chem.flueGasOutlet.xi[5] = if noEvent(volumeGas_L2_chem.outlet.m_flow > 0.0) then boundaryGas_pTxi.xi_const[5] else volumeGas_L2_chem.bulk.xi[5] 26/49 (1): volumeGas_L2_chem.flueGasOutlet.xi[4] = if noEvent(volumeGas_L2_chem.outlet.m_flow > 0.0) then boundaryGas_pTxi.xi_const[4] else volumeGas_L2_chem.bulk.xi[4] 27/50 (1): volumeGas_L2_chem.flueGasOutlet.xi[3] = if noEvent(volumeGas_L2_chem.outlet.m_flow > 0.0) then boundaryGas_pTxi.xi_const[3] else volumeGas_L2_chem.bulk.xi[3] 28/51 (1): volumeGas_L2_chem.flueGasOutlet.xi[2] = if noEvent(volumeGas_L2_chem.outlet.m_flow > 0.0) then boundaryGas_pTxi.xi_const[2] else volumeGas_L2_chem.bulk.xi[2] 29/52 (1): volumeGas_L2_chem.flueGasOutlet.xi[1] = if noEvent(volumeGas_L2_chem.outlet.m_flow > 0.0) then boundaryGas_pTxi.xi_const[1] else volumeGas_L2_chem.bulk.xi[1] Variables: 1: volumeGas_L2_chem.flueGasOutlet.xi[1]:VARIABLE(min = 0.0 max = 1.0 unit = "1" nominal = 1.0 ) "Mass fraction" type: Real [9] 2: volumeGas_L2_chem.flueGasOutlet.xi[2]:VARIABLE(min = 0.0 max = 1.0 unit = "1" nominal = 1.0 ) "Mass fraction" type: Real [9] 3: volumeGas_L2_chem.flueGasOutlet.xi[3]:VARIABLE(min = 0.0 max = 1.0 unit = "1" nominal = 1.0 ) "Mass fraction" type: Real [9] 4: volumeGas_L2_chem.flueGasOutlet.xi[4]:VARIABLE(min = 0.0 max = 1.0 unit = "1" nominal = 1.0 ) "Mass fraction" type: Real [9] 5: volumeGas_L2_chem.flueGasOutlet.xi[5]:VARIABLE(min = 0.0 max = 1.0 unit = "1" nominal = 1.0 ) "Mass fraction" type: Real [9] 6: volumeGas_L2_chem.flueGasOutlet.xi[6]:VARIABLE(min = 0.0 max = 1.0 unit = "1" nominal = 1.0 ) "Mass fraction" type: Real [9] 7: volumeGas_L2_chem.flueGasOutlet.xi[7]:VARIABLE(min = 0.0 max = 1.0 unit = "1" nominal = 1.0 ) "Mass fraction" type: Real [9] 8: volumeGas_L2_chem.flueGasOutlet.xi[8]:VARIABLE(min = 0.0 max = 1.0 unit = "1" nominal = 1.0 ) "Mass fraction" type: Real [9] 9: volumeGas_L2_chem.flueGasOutlet.xi[9]:VARIABLE(min = 0.0 max = 1.0 unit = "1" nominal = 1.0 ) "Mass fraction" type: Real [9] 10: volumeGas_L2_chem.chemicalReactions.V_flow:VARIABLE(unit = "m3/s" nominal = 1.0 ) "Volume flow rate of flue Gas entering the E-Filter" type: Real 11: $cse2:VARIABLE(protected = true ) type: Real unreplaceable 12: volumeGas_L2_chem.chemicalReactions.separationRate:VARIABLE() "Separation rate" type: Real 13: volumeGas_L2_chem.bulk.xi[1]:STATE(1)(min = 0.0 max = 1.0 start = volumeGas_L2_chem.xi_start[1] unit = "1" fixed = true nominal = 1.0 stateSelect=StateSelect.prefer ) "Mass fraction" type: Real [9] 14: volumeGas_L2_chem.bulk.xi[3]:STATE(1)(min = 0.0 max = 1.0 start = volumeGas_L2_chem.xi_start[3] unit = "1" fixed = true nominal = 1.0 stateSelect=StateSelect.prefer ) "Mass fraction" type: Real [9] 15: volumeGas_L2_chem.bulk.xi[4]:STATE(1)(min = 0.0 max = 1.0 start = volumeGas_L2_chem.xi_start[4] unit = "1" fixed = true nominal = 1.0 stateSelect=StateSelect.prefer ) "Mass fraction" type: Real [9] 16: volumeGas_L2_chem.bulk.xi[5]:STATE(1)(min = 0.0 max = 1.0 start = volumeGas_L2_chem.xi_start[5] unit = "1" fixed = true nominal = 1.0 stateSelect=StateSelect.prefer ) "Mass fraction" type: Real [9] 17: volumeGas_L2_chem.bulk.xi[6]:STATE(1)(min = 0.0 max = 1.0 start = volumeGas_L2_chem.xi_start[6] unit = "1" fixed = true nominal = 1.0 stateSelect=StateSelect.prefer ) "Mass fraction" type: Real [9] 18: volumeGas_L2_chem.bulk.xi[7]:STATE(1)(min = 0.0 max = 1.0 start = volumeGas_L2_chem.xi_start[7] unit = "1" fixed = true nominal = 1.0 stateSelect=StateSelect.prefer ) "Mass fraction" type: Real [9] 19: volumeGas_L2_chem.bulk.xi[8]:STATE(1)(min = 0.0 max = 1.0 start = volumeGas_L2_chem.xi_start[8] unit = "1" fixed = true nominal = 1.0 stateSelect=StateSelect.prefer ) "Mass fraction" type: Real [9] 20: volumeGas_L2_chem.bulk.xi[9]:STATE(1)(min = 0.0 max = 1.0 start = volumeGas_L2_chem.xi_start[9] unit = "1" fixed = true nominal = 1.0 stateSelect=StateSelect.prefer ) "Mass fraction" type: Real [9] 21: volumeGas_L2_chem.drhodt:VARIABLE(protected = true ) "Density derivative" type: Real 22: volumeGas_L2_chem.chemicalReactions.m_flow_reaction[1]:VARIABLE(unit = "kg/s" nominal = 1.0 ) type: Real [1] 23: volumeGas_L2_chem.bulk.xi[2]:STATE(1)(min = 0.0 max = 1.0 start = volumeGas_L2_chem.xi_start[2] unit = "1" fixed = true nominal = 1.0 stateSelect=StateSelect.prefer ) "Mass fraction" type: Real [9] 24: volumeGas_L2_chem.bulk.h:STATE(1)(start = volumeGas_L2_chem.h_start unit = "J/kg" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer ) "Specific enthalpy" type: Real 25: volumeGas_L2_chem.flueGasOutlet.h:VARIABLE(unit = "J/kg" nominal = 1000.0 ) "Specific enthalpy" type: Real 26: volumeGas_L2_chem.flueGasOutlet.p_i[5]:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 ) "Partial pressure" type: Real [10] 27: volumeGas_L2_chem.flueGasOutlet.kappa:VARIABLE(unit = "1/Pa" ) "Isothermal compressibility" type: Real 28: volumeGas_L2_chem.flueGasOutlet.drhodp_hxi:VARIABLE(unit = "s2/m2" ) "Derivative of density wrt pressure at specific enthalpy and mass fraction" type: Real 29: volumeGas_L2_chem.flueGasOutlet.p_i[1]:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 ) "Partial pressure" type: Real [10] 30: volumeGas_L2_chem.flueGasOutlet.drhodxi_ph[4]:VARIABLE(unit = "kg/(m3)" ) "Derivative of density wrt mass fraction of water at constant pressure and specific enthalpy" type: Real [9] 31: volumeGas_L2_chem.flueGasOutlet.p_i[8]:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 ) "Partial pressure" type: Real [10] 32: volumeGas_L2_chem.flueGasOutlet.xi_gas:VARIABLE(min = 0.0 max = 1.0 unit = "1" ) "Mass fraction of gasoues condensing component" type: Real 33: volumeGas_L2_chem.flueGasOutlet.p_i[3]:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 ) "Partial pressure" type: Real [10] 34: volumeGas_L2_chem.flueGasOutlet.p_i[7]:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 ) "Partial pressure" type: Real [10] 35: volumeGas_L2_chem.flueGasOutlet.drhodxi_ph[7]:VARIABLE(unit = "kg/(m3)" ) "Derivative of density wrt mass fraction of water at constant pressure and specific enthalpy" type: Real [9] 36: volumeGas_L2_chem.flueGasOutlet.p_i[6]:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 ) "Partial pressure" type: Real [10] 37: volumeGas_L2_chem.flueGasOutlet.p_i[9]:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 ) "Partial pressure" type: Real [10] 38: volumeGas_L2_chem.flueGasOutlet.drhodxi_ph[1]:VARIABLE(unit = "kg/(m3)" ) "Derivative of density wrt mass fraction of water at constant pressure and specific enthalpy" type: Real [9] 39: volumeGas_L2_chem.flueGasOutlet.p_i[4]:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 ) "Partial pressure" type: Real [10] 40: volumeGas_L2_chem.flueGasOutlet.drhodxi_ph[6]:VARIABLE(unit = "kg/(m3)" ) "Derivative of density wrt mass fraction of water at constant pressure and specific enthalpy" type: Real [9] 41: volumeGas_L2_chem.flueGasOutlet.drhodxi_ph[2]:VARIABLE(unit = "kg/(m3)" ) "Derivative of density wrt mass fraction of water at constant pressure and specific enthalpy" type: Real [9] 42: volumeGas_L2_chem.flueGasOutlet.drhodxi_ph[3]:VARIABLE(unit = "kg/(m3)" ) "Derivative of density wrt mass fraction of water at constant pressure and specific enthalpy" type: Real [9] 43: volumeGas_L2_chem.flueGasOutlet.drhodxi_ph[8]:VARIABLE(unit = "kg/(m3)" ) "Derivative of density wrt mass fraction of water at constant pressure and specific enthalpy" type: Real [9] 44: volumeGas_L2_chem.flueGasOutlet.d:VARIABLE(min = 0.0 unit = "kg/m3" ) "Density" type: Real 45: volumeGas_L2_chem.flueGasOutlet.drhodxi_ph[5]:VARIABLE(unit = "kg/(m3)" ) "Derivative of density wrt mass fraction of water at constant pressure and specific enthalpy" type: Real [9] 46: volumeGas_L2_chem.flueGasOutlet.p_i[2]:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 ) "Partial pressure" type: Real [10] 47: volumeGas_L2_chem.flueGasOutlet.drhodh_pxi:VARIABLE(unit = "kg.s2/m5" ) "Derivative of density wrt specific enthalpy at constant pressure and mass fraction" type: Real 48: volumeGas_L2_chem.flueGasOutlet.drhodxi_ph[9]:VARIABLE(unit = "kg/(m3)" ) "Derivative of density wrt mass fraction of water at constant pressure and specific enthalpy" type: Real [9] 49: volumeGas_L2_chem.flueGasOutlet.p_i[10]:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 ) "Partial pressure" type: Real [10] 50: volumeGas_L2_chem.flueGasOutlet.T:VARIABLE(min = 0.0 start = 288.15 unit = "K" nominal = 300.0 ) "Temperature" type: Real 51: volumeGas_L2_chem.outlet.m_flow:VARIABLE(flow=true max = 1e60 unit = "kg/s" nominal = 1.0 ) "Mass flow rate from the connection point into the component" type: Real 52: volumeGas_L2_chem.iCom.V_flow_out:VARIABLE(unit = "m3/s" nominal = 1.0 protected = true ) "Outlet volume flow" type: Real [/var/lib/jenkins1/ws/OpenModelicaLibraryTestingWork/OpenModelica/OMCompiler/Compiler/BackEnd/BackendDAEUtil.mo:9805:5-9806:77:writable] Error: Internal error BackendDAEUtil.traverseEqSystemStrongComponents failed with function: omc_DAEMode_traverserStrongComponents Notification: Performance of postOpt createDAEmodeBDAE (simulation): time 0.00861/0.9125, allocations: 4.11 MB / 0.9035 GB, free: 13.97 MB / 0.7013 GB Error: post-optimization module createDAEmodeBDAE (simulation) failed. Error: Internal error SimCode DAEmode: The model ClaRa.Basics.ControlVolumes.GasVolumes.Check.TestFlueGasCell_chem could not be translated