Running: ./testmodel.py --libraries=/home/hudson/saved_omc/libraries/.openmodelica/libraries --ompython_omhome=/usr ClaRa_dev_ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.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.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning,tolerance=1e-06,outputFormat="mat",numberOfIntervals=5000,variableFilter="Time|deNOx.bulk.h|deNOx.heat.Q_flow|deNOx.heattransfer.heat.Q_flow|deNOx.outlet.T_outflow|deNOx.outlet.m_flow|deNOx.summary.outlet.m_flow|deNOx.summary.outline.Q_flow_tot|deNOx.summary.outline.m_flow_reaction.1.|deSO_ideal_L1_1.bulk.h|deSO_ideal_L1_1.heat.Q_flow|deSO_ideal_L1_1.heattransfer.heat.Q_flow|deSO_ideal_L1_1.outlet.T_outflow|deSO_ideal_L1_1.outlet.m_flow|deSO_ideal_L1_1.summary.outlet.m_flow|deSO_ideal_L1_1.summary.outline.Q_flow_tot|deSO_ideal_L1_1.summary.outline.m_flow_reaction.1.|deSO_ideal_L1_1.summary.outline.m_flow_reaction.2.|deSO_ideal_L1_1.summary.outline.m_flow_reaction.3.|deSO_ideal_L1_1.summary.outline.m_flow_reaction.4.|deSO_ideal_L1_1.summary.outline.m_flow_reaction.5.|deSO_ideal_L1_1.summary.outline.m_flow_reaction.6.|deSO_ideal_L1_1.summary.outline.m_flow_reaction.7.|e_Filter_dynamic.bulk.h|e_Filter_dynamic.heat.Q_flow|e_Filter_dynamic.heattransfer.heat.Q_flow|e_Filter_dynamic.outlet.T_outflow|e_Filter_dynamic.outlet.m_flow|e_Filter_dynamic.summary.outlet.m_flow|e_Filter_dynamic.summary.outline.Q_flow_tot|e_Filter_dynamic.summary.outline.m_flow_reaction.1.|e_Filter_dynamic1.bulk.h|e_Filter_dynamic1.heat.Q_flow|e_Filter_dynamic1.heattransfer.heat.Q_flow|e_Filter_dynamic1.outlet.T_outflow|e_Filter_dynamic1.outlet.m_flow|e_Filter_dynamic1.summary.outlet.m_flow|e_Filter_dynamic1.summary.outline.Q_flow_tot|e_Filter_dynamic1.summary.outline.m_flow_reaction.1.|e_Filter_dynamic2.bulk.h|e_Filter_dynamic2.heat.Q_flow|e_Filter_dynamic2.heattransfer.heat.Q_flow|e_Filter_dynamic2.outlet.T_outflow|e_Filter_dynamic2.outlet.m_flow|e_Filter_dynamic2.summary.outlet.m_flow|e_Filter_dynamic2.summary.outline.Q_flow_tot|e_Filter_dynamic2.summary.outline.m_flow_reaction.1.|pipeFlowGas_L4_Simple.heatTransfer.heat.1..Q_flow|pipeFlowGas_L4_Simple.heatTransfer.heat.2..Q_flow|pipeFlowGas_L4_Simple.heatTransfer.heat.3..Q_flow|pipeFlowGas_L4_Simple.heat.1..Q_flow|pipeFlowGas_L4_Simple.heat.2..Q_flow|pipeFlowGas_L4_Simple.heat.3..Q_flow|pipeFlowGas_L4_Simple.outlet.T_outflow|pipeFlowGas_L4_Simple.outlet.m_flow|pipeFlowGas_L4_Simple.summary.outlet.m_flow|pipeFlowGas_L4_Simple.summary.outline.Q_flow_tot|pipeFlowGas_L4_Simple.summary.outline.m_flow.1.|pipeFlowGas_L4_Simple.summary.outline.m_flow.2.|pipeFlowGas_L4_Simple.summary.outline.m_flow.3.|pipeFlowGas_L4_Simple.summary.outline.m_flow.4.|scalar2VectorHeatPort2.heatScalar.Q_flow|scalar2VectorHeatPort2.heatVector.1..Q_flow|scalar2VectorHeatPort2.heatVector.2..Q_flow|scalar2VectorHeatPort2.heatVector.3..Q_flow",fileNamePrefix="ClaRa_dev_ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning")
translateModel(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning,tolerance=1e-06,outputFormat="mat",numberOfIntervals=5000,variableFilter="Time|deNOx.bulk.h|deNOx.heat.Q_flow|deNOx.heattransfer.heat.Q_flow|deNOx.outlet.T_outflow|deNOx.outlet.m_flow|deNOx.summary.outlet.m_flow|deNOx.summary.outline.Q_flow_tot|deNOx.summary.outline.m_flow_reaction.1.|deSO_ideal_L1_1.bulk.h|deSO_ideal_L1_1.heat.Q_flow|deSO_ideal_L1_1.heattransfer.heat.Q_flow|deSO_ideal_L1_1.outlet.T_outflow|deSO_ideal_L1_1.outlet.m_flow|deSO_ideal_L1_1.summary.outlet.m_flow|deSO_ideal_L1_1.summary.outline.Q_flow_tot|deSO_ideal_L1_1.summary.outline.m_flow_reaction.1.|deSO_ideal_L1_1.summary.outline.m_flow_reaction.2.|deSO_ideal_L1_1.summary.outline.m_flow_reaction.3.|deSO_ideal_L1_1.summary.outline.m_flow_reaction.4.|deSO_ideal_L1_1.summary.outline.m_flow_reaction.5.|deSO_ideal_L1_1.summary.outline.m_flow_reaction.6.|deSO_ideal_L1_1.summary.outline.m_flow_reaction.7.|e_Filter_dynamic.bulk.h|e_Filter_dynamic.heat.Q_flow|e_Filter_dynamic.heattransfer.heat.Q_flow|e_Filter_dynamic.outlet.T_outflow|e_Filter_dynamic.outlet.m_flow|e_Filter_dynamic.summary.outlet.m_flow|e_Filter_dynamic.summary.outline.Q_flow_tot|e_Filter_dynamic.summary.outline.m_flow_reaction.1.|e_Filter_dynamic1.bulk.h|e_Filter_dynamic1.heat.Q_flow|e_Filter_dynamic1.heattransfer.heat.Q_flow|e_Filter_dynamic1.outlet.T_outflow|e_Filter_dynamic1.outlet.m_flow|e_Filter_dynamic1.summary.outlet.m_flow|e_Filter_dynamic1.summary.outline.Q_flow_tot|e_Filter_dynamic1.summary.outline.m_flow_reaction.1.|e_Filter_dynamic2.bulk.h|e_Filter_dynamic2.heat.Q_flow|e_Filter_dynamic2.heattransfer.heat.Q_flow|e_Filter_dynamic2.outlet.T_outflow|e_Filter_dynamic2.outlet.m_flow|e_Filter_dynamic2.summary.outlet.m_flow|e_Filter_dynamic2.summary.outline.Q_flow_tot|e_Filter_dynamic2.summary.outline.m_flow_reaction.1.|pipeFlowGas_L4_Simple.heatTransfer.heat.1..Q_flow|pipeFlowGas_L4_Simple.heatTransfer.heat.2..Q_flow|pipeFlowGas_L4_Simple.heatTransfer.heat.3..Q_flow|pipeFlowGas_L4_Simple.heat.1..Q_flow|pipeFlowGas_L4_Simple.heat.2..Q_flow|pipeFlowGas_L4_Simple.heat.3..Q_flow|pipeFlowGas_L4_Simple.outlet.T_outflow|pipeFlowGas_L4_Simple.outlet.m_flow|pipeFlowGas_L4_Simple.summary.outlet.m_flow|pipeFlowGas_L4_Simple.summary.outline.Q_flow_tot|pipeFlowGas_L4_Simple.summary.outline.m_flow.1.|pipeFlowGas_L4_Simple.summary.outline.m_flow.2.|pipeFlowGas_L4_Simple.summary.outline.m_flow.3.|pipeFlowGas_L4_Simple.summary.outline.m_flow.4.|scalar2VectorHeatPort2.heatScalar.Q_flow|scalar2VectorHeatPort2.heatVector.1..Q_flow|scalar2VectorHeatPort2.heatVector.2..Q_flow|scalar2VectorHeatPort2.heatVector.3..Q_flow",fileNamePrefix="ClaRa_dev_ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning")
Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/SMArtIInt 0.2.2-main/package.mo): time 0.009234/0.009234, allocations: 1.439 MB / 17.75 MB, free: 5.348 MB / 14.72 MB
Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.8.1-main/package.mo): time 0.1219/0.1219, allocations: 22.38 MB / 41.17 MB, free: 7.781 MB / 34.91 MB
Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/ModelicaServices 4.0.0+maint.om/package.mo): time 0.00122/0.00122, allocations: 112 kB / 48.66 MB, free: 268 kB / 34.91 MB
Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/Complex 4.0.0+maint.om/package.mo): time 0.001617/0.001617, allocations: 200.1 kB / 56.26 MB, free: 9.469 MB / 46.55 MB
Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/Modelica 4.0.0+maint.om/package.mo): time 1.355/1.355, allocations: 222.9 MB / 286.6 MB, free: 13.96 MB / 222.1 MB
Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/ClaRa 1.8.2-main/package.mo): time 0.8678/0.8678, allocations: 127.8 MB / 471.3 MB, free: 0.582 MB / 366.1 MB
Notification: Performance of FrontEnd - loaded program: time 0.002532/0.002532, allocations: 135.8 kB / 0.636 GB, free: 13.18 MB / 478.1 MB
Notification: Performance of FrontEnd - Absyn->SCode: time 0.3768/0.3793, allocations: 82.35 MB / 0.7164 GB, free: 9.738 MB / 0.5138 GB
Notification: Performance of NFInst.instantiate(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning): time 0.03299/0.4124, allocations: 33.96 MB / 0.7496 GB, free: 14.02 MB / 0.545 GB
Notification: Performance of NFInst.instExpressions: time 0.0352/0.4476, allocations: 21.29 MB / 0.7703 GB, free: 8.66 MB / 0.5607 GB
Notification: Performance of NFInst.updateImplicitVariability: time 0.006492/0.4541, allocations: 127.6 kB / 0.7705 GB, free: 8.535 MB / 0.5607 GB
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/ClaRa 1.8.2-main/Basics/Interfaces/CycleSumModel.mo:3:3-3:52: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 0.009433/0.4636, allocations: 3.805 MB / 0.7742 GB, free: 4.719 MB / 0.5607 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'.
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.8.1-main/GasFunctions.mo:238:23-242:17:writable] Warning: Pure function 'TILMedia.GasFunctions.density_pTxi' contains a call to impure function 'TILMedia.Internals.GasFunctions.density_pTxi'.
Notification: Performance of NFTyping.typeBindings: time 0.01342/0.477, allocations: 5.161 MB / 0.7792 GB, free: 15.53 MB / 0.5763 GB
Notification: Performance of NFTyping.typeClassSections: time 0.0132/0.4902, allocations: 5.262 MB / 0.7844 GB, free: 10.26 MB / 0.5763 GB
Notification: Performance of NFFlatten.flatten: time 0.02369/0.5139, allocations: 18.15 MB / 0.8021 GB, free: 8.07 MB / 0.5919 GB
Notification: Performance of NFFlatten.resolveConnections: time 0.02065/0.5346, allocations: 15.89 MB / 0.8176 GB, free: 8.055 MB / 0.6075 GB
Notification: Performance of NFEvalConstants.evaluate: time 0.01589/0.5505, allocations: 9.424 MB / 0.8268 GB, free: 14.61 MB / 0.6232 GB
Notification: Performance of NFSimplifyModel.simplify: time 0.01997/0.5706, allocations: 15.83 MB / 0.8423 GB, free: 14.74 MB / 0.6388 GB
Notification: Performance of NFPackage.collectConstants: time 0.01003/0.5806, allocations: 3.891 MB / 0.8461 GB, free: 10.85 MB / 0.6388 GB
Notification: Performance of NFFlatten.collectFunctions: time 0.01535/0.596, allocations: 6.263 MB / 0.8522 GB, free: 4.586 MB / 0.6388 GB
Notification: Performance of NFScalarize.scalarize: time 0.01892/0.615, allocations: 16.6 MB / 0.8684 GB, free: 3.945 MB / 0.6544 GB
Notification: Performance of NFVerifyModel.verify: time 0.0291/0.6441, allocations: 18.24 MB / 0.8862 GB, free: 1.621 MB / 0.67 GB
Notification: Performance of NFConvertDAE.convert: time 0.06081/0.7049, allocations: 57.39 MB / 0.9423 GB, free: 8.078 MB / 0.7325 GB
Notification: Performance of FrontEnd - DAE generated: time 6.022e-06/0.705, allocations: 0 / 0.9423 GB, free: 8.078 MB / 0.7325 GB
Notification: Performance of FrontEnd: time 1.974e-06/0.705, allocations: 4 kB / 0.9423 GB, free: 8.074 MB / 0.7325 GB
Notification: Performance of Transformations before backend: time 0.00109/0.7061, allocations: 0 / 0.9423 GB, free: 8.074 MB / 0.7325 GB
Notification: Model statistics after passing the front-end and creating the data structures used by the back-end:
 * Number of equations: 3722
 * Number of variables: 3722
Notification: Performance of Generate backend data structure: time 0.726/1.432, allocations: 39.17 MB / 0.9805 GB, free: 170.6 MB / 0.7483 GB
Notification: Performance of prepare preOptimizeDAE: time 4.676e-05/1.432, allocations: 8.531 kB / 0.9805 GB, free: 170.6 MB / 0.7483 GB
Notification: Performance of preOpt normalInlineFunction (simulation): time 0.01754/1.45, allocations: 3.251 MB / 0.9837 GB, free: 169 MB / 0.7483 GB
Notification: Performance of preOpt evaluateParameters (simulation): time 0.07241/1.522, allocations: 41.86 MB / 1.025 GB, free: 138.4 MB / 0.7483 GB
Notification: Performance of preOpt simplifyIfEquations (simulation): time 0.0006823/1.523, allocations: 0.7886 MB / 1.025 GB, free: 137.6 MB / 0.7483 GB
Notification: Performance of preOpt expandDerOperator (simulation): time 0.005449/1.528, allocations: 0.9226 MB / 1.026 GB, free: 136.7 MB / 0.7483 GB
Notification: Performance of preOpt clockPartitioning (simulation): time 0.05646/1.585, allocations: 39.54 MB / 1.065 GB, free: 93.57 MB / 0.7483 GB
Notification: Performance of preOpt findStateOrder (simulation): time 0.0002028/1.585, allocations: 15.81 kB / 1.065 GB, free: 93.56 MB / 0.7483 GB
Notification: Performance of preOpt replaceEdgeChange (simulation): time 0.004952/1.59, allocations: 0.5604 MB / 1.065 GB, free: 93.02 MB / 0.7483 GB
Notification: Performance of preOpt inlineArrayEqn (simulation): time 0.001053/1.591, allocations: 1.317 MB / 1.067 GB, free: 91.7 MB / 0.7483 GB
Notification: Performance of preOpt removeEqualRHS (simulation): time 0.06538/1.656, allocations: 46.98 MB / 1.113 GB, free: 44.68 MB / 0.7483 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 0.1799/1.836, allocations: 100.8 MB / 1.211 GB, free: 7.793 MB / 0.8108 GB
Notification: Performance of preOpt comSubExp (simulation): time 0.04258/1.879, allocations: 27.39 MB / 1.238 GB, free: 12.38 MB / 0.842 GB
Notification: Performance of preOpt resolveLoops (simulation): time 0.0332/1.912, allocations: 21.75 MB / 1.259 GB, free: 6.602 MB / 0.8577 GB
Notification: Performance of preOpt evalFunc (simulation): time 0.00308/1.915, allocations: 368.5 kB / 1.259 GB, free: 6.242 MB / 0.8577 GB
Notification: Performance of preOpt encapsulateWhenConditions (simulation): time 0.0002398/1.916, allocations: 174.5 kB / 1.26 GB, free: 6.062 MB / 0.8577 GB
Notification: Performance of pre-optimization done (n=2030): time 3.813e-05/1.916, allocations: 0 / 1.26 GB, free: 6.062 MB / 0.8577 GB
Notification: Performance of matching and sorting (n=2030): time 0.481/2.397, allocations: 70.03 MB / 1.328 GB, free: 288.8 MB / 0.8889 GB
Notification: Performance of inlineWhenForInitialization (initialization): time 0.0002624/2.397, allocations: 1.216 MB / 1.329 GB, free: 287.4 MB / 0.8889 GB
Notification: Performance of selectInitializationVariablesDAE (initialization): time 0.04309/2.44, allocations: 24.16 MB / 1.353 GB, free: 277 MB / 0.8889 GB
Notification: Performance of collectPreVariables (initialization): time 0.004189/2.444, allocations: 230.3 kB / 1.353 GB, free: 276.8 MB / 0.8889 GB
Notification: Performance of collectInitialEqns (initialization): time 0.01224/2.457, allocations: 10.8 MB / 1.364 GB, free: 268.7 MB / 0.8889 GB
Notification: Performance of collectInitialBindings (initialization): time 0.008356/2.465, allocations: 6.649 MB / 1.37 GB, free: 264.2 MB / 0.8889 GB
Notification: Performance of simplifyInitialFunctions (initialization): time 0.01615/2.481, allocations: 3.093 MB / 1.373 GB, free: 261.1 MB / 0.8889 GB
Notification: Performance of setup shared object (initialization): time 4.085e-05/2.481, allocations: 301.1 kB / 1.373 GB, free: 260.8 MB / 0.8889 GB
Notification: Performance of preBalanceInitialSystem (initialization): time 0.02718/2.508, allocations: 19.38 MB / 1.392 GB, free: 241.4 MB / 0.8889 GB
Notification: Performance of partitionIndependentBlocks (initialization): time 0.02983/2.538, allocations: 21.87 MB / 1.414 GB, free: 218.8 MB / 0.8889 GB
Notification: Performance of analyzeInitialSystem (initialization): time 0.6032/3.141, allocations: 194.1 MB / 1.603 GB, free: 24.21 MB / 0.8889 GB
Notification: Performance of solveInitialSystemEqSystem (initialization): time 4.761e-05/3.142, allocations: 15.94 kB / 1.603 GB, free: 24.2 MB / 0.8889 GB
Notification: Performance of matching and sorting (n=2358) (initialization): time 0.4345/3.576, allocations: 50.5 MB / 1.652 GB, free: 291.9 MB / 0.9045 GB
Notification: Performance of prepare postOptimizeDAE: time 4.919e-05/3.576, allocations: 25.34 kB / 1.652 GB, free: 291.9 MB / 0.9045 GB
Notification: Performance of postOpt simplifyComplexFunction (initialization): time 0.000519/3.577, allocations: 186.6 kB / 1.653 GB, free: 291.9 MB / 0.9045 GB
Notification: Performance of postOpt tearingSystem (initialization): time 0.01554/3.592, allocations: 6.613 MB / 1.659 GB, free: 291.7 MB / 0.9045 GB
Notification: Performance of postOpt solveSimpleEquations (initialization): time 0.0422/3.634, allocations: 3.752 MB / 1.663 GB, free: 291.7 MB / 0.9045 GB
Notification: Performance of postOpt calculateStrongComponentJacobians (initialization): time 0.01505/3.65, allocations: 16.94 MB / 1.679 GB, free: 282.8 MB / 0.9045 GB
Notification: Performance of postOpt simplifyAllExpressions (initialization): time 0.01741/3.667, allocations: 1.55 MB / 1.681 GB, free: 282.6 MB / 0.9045 GB
Notification: Performance of postOpt collapseArrayExpressions (initialization): time 0.004117/3.671, allocations: 0.5984 MB / 1.681 GB, free: 282.5 MB / 0.9045 GB
Warning: Assuming fixed start value for the following 56 variables:
         deSO_ideal_L1_1.bulk.h:VARIABLE(start = deSO_ideal_L1_1.h_start unit = "J/kg" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer )  "Specific enthalpy" type: Real
         deSO_ideal_L1_1.bulk.xi[1]:VARIABLE(min = 0.0 max = 1.0 start = deSO_ideal_L1_1.xi_start[1] unit = "1" fixed = true nominal = 1.0 stateSelect=StateSelect.prefer )  "Mass fraction" type: Real [9]
         deSO_ideal_L1_1.bulk.xi[2]:VARIABLE(min = 0.0 max = 1.0 start = deSO_ideal_L1_1.xi_start[2] unit = "1" fixed = true nominal = 1.0 stateSelect=StateSelect.prefer )  "Mass fraction" type: Real [9]
         deSO_ideal_L1_1.bulk.xi[3]:VARIABLE(min = 0.0 max = 1.0 start = deSO_ideal_L1_1.xi_start[3] unit = "1" fixed = true nominal = 1.0 stateSelect=StateSelect.prefer )  "Mass fraction" type: Real [9]
         deSO_ideal_L1_1.bulk.xi[4]:VARIABLE(min = 0.0 max = 1.0 start = deSO_ideal_L1_1.xi_start[4] unit = "1" fixed = true nominal = 1.0 stateSelect=StateSelect.prefer )  "Mass fraction" type: Real [9]
         deSO_ideal_L1_1.bulk.xi[5]:VARIABLE(min = 0.0 max = 1.0 start = deSO_ideal_L1_1.xi_start[5] unit = "1" fixed = true nominal = 1.0 stateSelect=StateSelect.prefer )  "Mass fraction" type: Real [9]
         deSO_ideal_L1_1.bulk.xi[6]:VARIABLE(min = 0.0 max = 1.0 start = deSO_ideal_L1_1.xi_start[6] unit = "1" fixed = true nominal = 1.0 stateSelect=StateSelect.prefer )  "Mass fraction" type: Real [9]
         deSO_ideal_L1_1.bulk.xi[7]:VARIABLE(min = 0.0 max = 1.0 start = deSO_ideal_L1_1.xi_start[7] unit = "1" fixed = true nominal = 1.0 stateSelect=StateSelect.prefer )  "Mass fraction" type: Real [9]
         deSO_ideal_L1_1.bulk.xi[8]:VARIABLE(min = 0.0 max = 1.0 start = deSO_ideal_L1_1.xi_start[8] unit = "1" fixed = true nominal = 1.0 stateSelect=StateSelect.prefer )  "Mass fraction" type: Real [9]
         deSO_ideal_L1_1.bulk.xi[9]:VARIABLE(min = 0.0 max = 1.0 start = deSO_ideal_L1_1.xi_start[9] unit = "1" fixed = true nominal = 1.0 stateSelect=StateSelect.prefer )  "Mass fraction" type: Real [9]
         deNOx.bulk.h:VARIABLE(start = deNOx.h_start unit = "J/kg" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer )  "Specific enthalpy" type: Real
         deNOx.bulk.xi[1]:VARIABLE(min = 0.0 max = 1.0 start = 9.910802775024783e-4 unit = "1" fixed = true nominal = 1.0 stateSelect=StateSelect.prefer )  "Mass fraction" type: Real [9]
         deNOx.bulk.xi[2]:VARIABLE(min = 0.0 max = 1.0 start = 9.910802775024783e-4 unit = "1" fixed = true nominal = 1.0 stateSelect=StateSelect.prefer )  "Mass fraction" type: Real [9]
         deNOx.bulk.xi[3]:VARIABLE(min = 0.0 max = 1.0 start = 9.910802775024783e-4 unit = "1" fixed = true nominal = 1.0 stateSelect=StateSelect.prefer )  "Mass fraction" type: Real [9]
         deNOx.bulk.xi[4]:VARIABLE(min = 0.0 max = 1.0 start = 9.910802775024783e-4 unit = "1" fixed = true nominal = 1.0 stateSelect=StateSelect.prefer )  "Mass fraction" type: Real [9]
         deNOx.bulk.xi[5]:VARIABLE(min = 0.0 max = 1.0 start = 0.9910802775024783 unit = "1" fixed = true nominal = 1.0 stateSelect=StateSelect.prefer )  "Mass fraction" type: Real [9]
         deNOx.bulk.xi[6]:VARIABLE(min = 0.0 max = 1.0 start = 9.910802775024783e-4 unit = "1" fixed = true nominal = 1.0 stateSelect=StateSelect.prefer )  "Mass fraction" type: Real [9]
         deNOx.bulk.xi[7]:VARIABLE(min = 0.0 max = 1.0 start = 9.910802775024783e-4 unit = "1" fixed = true nominal = 1.0 stateSelect=StateSelect.prefer )  "Mass fraction" type: Real [9]
         deNOx.bulk.xi[8]:VARIABLE(min = 0.0 max = 1.0 start = 9.910802775024783e-4 unit = "1" fixed = true nominal = 1.0 stateSelect=StateSelect.prefer )  "Mass fraction" type: Real [9]
         deNOx.bulk.xi[9]:VARIABLE(min = 0.0 max = 1.0 start = 9.910802775024783e-4 unit = "1" fixed = true nominal = 1.0 stateSelect=StateSelect.prefer )  "Mass fraction" type: Real [9]
         e_Filter_dynamic.bulk.h:VARIABLE(start = e_Filter_dynamic.h_start unit = "J/kg" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer )  "Specific enthalpy" type: Real
         e_Filter_dynamic.bulk.xi[1]:VARIABLE(min = 0.0 max = 1.0 start = e_Filter_dynamic.xi_start[1] unit = "1" fixed = true nominal = 1.0 stateSelect=StateSelect.prefer )  "Mass fraction" type: Real [9]
         e_Filter_dynamic.bulk.xi[2]:VARIABLE(min = 0.0 max = 1.0 start = e_Filter_dynamic.xi_start[2] unit = "1" fixed = true nominal = 1.0 stateSelect=StateSelect.prefer )  "Mass fraction" type: Real [9]
         e_Filter_dynamic.bulk.xi[3]:VARIABLE(min = 0.0 max = 1.0 start = e_Filter_dynamic.xi_start[3] unit = "1" fixed = true nominal = 1.0 stateSelect=StateSelect.prefer )  "Mass fraction" type: Real [9]
         e_Filter_dynamic.bulk.xi[4]:VARIABLE(min = 0.0 max = 1.0 start = e_Filter_dynamic.xi_start[4] unit = "1" fixed = true nominal = 1.0 stateSelect=StateSelect.prefer )  "Mass fraction" type: Real [9]
         e_Filter_dynamic.bulk.xi[5]:VARIABLE(min = 0.0 max = 1.0 start = e_Filter_dynamic.xi_start[5] unit = "1" fixed = true nominal = 1.0 stateSelect=StateSelect.prefer )  "Mass fraction" type: Real [9]
         e_Filter_dynamic.bulk.xi[6]:VARIABLE(min = 0.0 max = 1.0 start = e_Filter_dynamic.xi_start[6] unit = "1" fixed = true nominal = 1.0 stateSelect=StateSelect.prefer )  "Mass fraction" type: Real [9]
         e_Filter_dynamic.bulk.xi[7]:VARIABLE(min = 0.0 max = 1.0 start = e_Filter_dynamic.xi_start[7] unit = "1" fixed = true nominal = 1.0 stateSelect=StateSelect.prefer )  "Mass fraction" type: Real [9]
         e_Filter_dynamic.bulk.xi[8]:VARIABLE(min = 0.0 max = 1.0 start = e_Filter_dynamic.xi_start[8] unit = "1" fixed = true nominal = 1.0 stateSelect=StateSelect.prefer )  "Mass fraction" type: Real [9]
         e_Filter_dynamic.bulk.xi[9]:VARIABLE(min = 0.0 max = 1.0 start = e_Filter_dynamic.xi_start[9] unit = "1" fixed = true nominal = 1.0 stateSelect=StateSelect.prefer )  "Mass fraction" type: Real [9]
         e_Filter_dynamic1.bulk.h:VARIABLE(start = e_Filter_dynamic1.h_start unit = "J/kg" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer )  "Specific enthalpy" type: Real
         e_Filter_dynamic1.bulk.xi[1]:VARIABLE(min = 0.0 max = 1.0 start = 9.910802775024783e-4 unit = "1" fixed = true nominal = 1.0 stateSelect=StateSelect.prefer )  "Mass fraction" type: Real [9]
         e_Filter_dynamic1.bulk.xi[2]:VARIABLE(min = 0.0 max = 1.0 start = 9.910802775024783e-4 unit = "1" fixed = true nominal = 1.0 stateSelect=StateSelect.prefer )  "Mass fraction" type: Real [9]
         e_Filter_dynamic1.bulk.xi[3]:VARIABLE(min = 0.0 max = 1.0 start = 9.910802775024783e-4 unit = "1" fixed = true nominal = 1.0 stateSelect=StateSelect.prefer )  "Mass fraction" type: Real [9]
         e_Filter_dynamic1.bulk.xi[4]:VARIABLE(min = 0.0 max = 1.0 start = 9.910802775024783e-4 unit = "1" fixed = true nominal = 1.0 stateSelect=StateSelect.prefer )  "Mass fraction" type: Real [9]
         e_Filter_dynamic1.bulk.xi[5]:VARIABLE(min = 0.0 max = 1.0 start = 0.9910802775024783 unit = "1" fixed = true nominal = 1.0 stateSelect=StateSelect.prefer )  "Mass fraction" type: Real [9]
         e_Filter_dynamic1.bulk.xi[6]:VARIABLE(min = 0.0 max = 1.0 start = 9.910802775024783e-4 unit = "1" fixed = true nominal = 1.0 stateSelect=StateSelect.prefer )  "Mass fraction" type: Real [9]
         e_Filter_dynamic1.bulk.xi[7]:VARIABLE(min = 0.0 max = 1.0 start = 9.910802775024783e-4 unit = "1" fixed = true nominal = 1.0 stateSelect=StateSelect.prefer )  "Mass fraction" type: Real [9]
         e_Filter_dynamic1.bulk.xi[8]:VARIABLE(min = 0.0 max = 1.0 start = 9.910802775024783e-4 unit = "1" fixed = true nominal = 1.0 stateSelect=StateSelect.prefer )  "Mass fraction" type: Real [9]
         e_Filter_dynamic1.bulk.xi[9]:VARIABLE(min = 0.0 max = 1.0 start = 9.910802775024783e-4 unit = "1" fixed = true nominal = 1.0 stateSelect=StateSelect.prefer )  "Mass fraction" type: Real [9]
         e_Filter_dynamic2.bulk.h:VARIABLE(start = e_Filter_dynamic2.h_start unit = "J/kg" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer )  "Specific enthalpy" type: Real
         e_Filter_dynamic2.bulk.xi[1]:VARIABLE(min = 0.0 max = 1.0 start = e_Filter_dynamic2.xi_start[1] unit = "1" fixed = true nominal = 1.0 stateSelect=StateSelect.prefer )  "Mass fraction" type: Real [9]
         e_Filter_dynamic2.bulk.xi[2]:VARIABLE(min = 0.0 max = 1.0 start = e_Filter_dynamic2.xi_start[2] unit = "1" fixed = true nominal = 1.0 stateSelect=StateSelect.prefer )  "Mass fraction" type: Real [9]
         e_Filter_dynamic2.bulk.xi[3]:VARIABLE(min = 0.0 max = 1.0 start = e_Filter_dynamic2.xi_start[3] unit = "1" fixed = true nominal = 1.0 stateSelect=StateSelect.prefer )  "Mass fraction" type: Real [9]
         e_Filter_dynamic2.bulk.xi[4]:VARIABLE(min = 0.0 max = 1.0 start = e_Filter_dynamic2.xi_start[4] unit = "1" fixed = true nominal = 1.0 stateSelect=StateSelect.prefer )  "Mass fraction" type: Real [9]
         e_Filter_dynamic2.bulk.xi[5]:VARIABLE(min = 0.0 max = 1.0 start = e_Filter_dynamic2.xi_start[5] unit = "1" fixed = true nominal = 1.0 stateSelect=StateSelect.prefer )  "Mass fraction" type: Real [9]
         e_Filter_dynamic2.bulk.xi[6]:VARIABLE(min = 0.0 max = 1.0 start = e_Filter_dynamic2.xi_start[6] unit = "1" fixed = true nominal = 1.0 stateSelect=StateSelect.prefer )  "Mass fraction" type: Real [9]
         e_Filter_dynamic2.bulk.xi[7]:VARIABLE(min = 0.0 max = 1.0 start = e_Filter_dynamic2.xi_start[7] unit = "1" fixed = true nominal = 1.0 stateSelect=StateSelect.prefer )  "Mass fraction" type: Real [9]
         e_Filter_dynamic2.bulk.xi[8]:VARIABLE(min = 0.0 max = 1.0 start = e_Filter_dynamic2.xi_start[8] unit = "1" fixed = true nominal = 1.0 stateSelect=StateSelect.prefer )  "Mass fraction" type: Real [9]
         e_Filter_dynamic2.bulk.xi[9]:VARIABLE(min = 0.0 max = 1.0 start = e_Filter_dynamic2.xi_start[9] unit = "1" fixed = true nominal = 1.0 stateSelect=StateSelect.prefer )  "Mass fraction" type: Real [9]
         pipeFlowGas_L4_Simple.h[1]:VARIABLE(start = pipeFlowGas_L4_Simple.h_start[1] unit = "J/kg" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer )  "Cell enthalpy" type: Real [3]
         pipeFlowGas_L4_Simple.h[2]:VARIABLE(start = pipeFlowGas_L4_Simple.h_start[2] unit = "J/kg" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer )  "Cell enthalpy" type: Real [3]
         pipeFlowGas_L4_Simple.h[3]:VARIABLE(start = pipeFlowGas_L4_Simple.h_start[3] unit = "J/kg" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer )  "Cell enthalpy" type: Real [3]
         pipeFlowGas_L4_Simple.p[1]:VARIABLE(min = 0.0 start = pipeFlowGas_L4_Simple.p_start[1] unit = "Pa" fixed = true nominal = 1e5 protected = true )  "Cell pressure" type: Real [3]
         pipeFlowGas_L4_Simple.p[2]:VARIABLE(min = 0.0 start = pipeFlowGas_L4_Simple.p_start[2] unit = "Pa" fixed = true nominal = 1e5 protected = true )  "Cell pressure" type: Real [3]
         pipeFlowGas_L4_Simple.p[3]:VARIABLE(min = 0.0 start = pipeFlowGas_L4_Simple.p_start[3] unit = "Pa" fixed = true nominal = 1e5 protected = true )  "Cell pressure" type: Real [3]
Notification: Performance of preBalanceInitialSystem (initialization_lambda0): time 0.03893/3.71, allocations: 27.11 MB / 1.708 GB, free: 269.3 MB / 0.9045 GB
Notification: Performance of partitionIndependentBlocks (initialization_lambda0): time 0.02801/3.738, allocations: 21.7 MB / 1.729 GB, free: 251.5 MB / 0.9045 GB
Notification: Performance of analyzeInitialSystem (initialization_lambda0): time 0.5872/4.325, allocations: 193.4 MB / 1.918 GB, free: 58.01 MB / 0.9045 GB
Notification: Performance of solveInitialSystemEqSystem (initialization_lambda0): time 7.431e-05/4.326, allocations: 15.94 kB / 1.918 GB, free: 57.99 MB / 0.9045 GB
Notification: Performance of matching and sorting (n=2358) (initialization_lambda0): time 0.09254/4.418, allocations: 50.15 MB / 1.967 GB, free: 9.035 MB / 0.9045 GB
Notification: Performance of prepare postOptimizeDAE: time 5.406e-05/4.418, allocations: 24 kB / 1.967 GB, free: 9.012 MB / 0.9045 GB
Notification: Performance of postOpt simplifyComplexFunction (initialization): time 0.0005491/4.419, allocations: 191.9 kB / 1.967 GB, free: 8.824 MB / 0.9045 GB
Notification: Performance of postOpt tearingSystem (initialization): time 0.0156/4.434, allocations: 6.618 MB / 1.974 GB, free: 2.176 MB / 0.9045 GB
Notification: Performance of postOpt solveSimpleEquations (initialization): time 0.4381/4.872, allocations: 3.714 MB / 1.977 GB, free: 296.8 MB / 0.9045 GB
Notification: Performance of postOpt calculateStrongComponentJacobians (initialization): time 0.01637/4.889, allocations: 16.34 MB / 1.993 GB, free: 288.7 MB / 0.9045 GB
Notification: Performance of postOpt simplifyAllExpressions (initialization): time 0.01966/4.909, allocations: 1.373 MB / 1.995 GB, free: 288.7 MB / 0.9045 GB
Notification: Performance of postOpt collapseArrayExpressions (initialization): time 0.00533/4.914, allocations: 0.5868 MB / 1.995 GB, free: 288.7 MB / 0.9045 GB
Warning: Assuming fixed start value for the following 56 variables:
         deSO_ideal_L1_1.bulk.h:VARIABLE(start = deSO_ideal_L1_1.h_start unit = "J/kg" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer )  "Specific enthalpy" type: Real
         deSO_ideal_L1_1.bulk.xi[1]:VARIABLE(min = 0.0 max = 1.0 start = deSO_ideal_L1_1.xi_start[1] unit = "1" fixed = true nominal = 1.0 stateSelect=StateSelect.prefer )  "Mass fraction" type: Real [9]
         deSO_ideal_L1_1.bulk.xi[2]:VARIABLE(min = 0.0 max = 1.0 start = deSO_ideal_L1_1.xi_start[2] unit = "1" fixed = true nominal = 1.0 stateSelect=StateSelect.prefer )  "Mass fraction" type: Real [9]
         deSO_ideal_L1_1.bulk.xi[3]:VARIABLE(min = 0.0 max = 1.0 start = deSO_ideal_L1_1.xi_start[3] unit = "1" fixed = true nominal = 1.0 stateSelect=StateSelect.prefer )  "Mass fraction" type: Real [9]
         deSO_ideal_L1_1.bulk.xi[4]:VARIABLE(min = 0.0 max = 1.0 start = deSO_ideal_L1_1.xi_start[4] unit = "1" fixed = true nominal = 1.0 stateSelect=StateSelect.prefer )  "Mass fraction" type: Real [9]
         deSO_ideal_L1_1.bulk.xi[5]:VARIABLE(min = 0.0 max = 1.0 start = deSO_ideal_L1_1.xi_start[5] unit = "1" fixed = true nominal = 1.0 stateSelect=StateSelect.prefer )  "Mass fraction" type: Real [9]
         deSO_ideal_L1_1.bulk.xi[6]:VARIABLE(min = 0.0 max = 1.0 start = deSO_ideal_L1_1.xi_start[6] unit = "1" fixed = true nominal = 1.0 stateSelect=StateSelect.prefer )  "Mass fraction" type: Real [9]
         deSO_ideal_L1_1.bulk.xi[7]:VARIABLE(min = 0.0 max = 1.0 start = deSO_ideal_L1_1.xi_start[7] unit = "1" fixed = true nominal = 1.0 stateSelect=StateSelect.prefer )  "Mass fraction" type: Real [9]
         deSO_ideal_L1_1.bulk.xi[8]:VARIABLE(min = 0.0 max = 1.0 start = deSO_ideal_L1_1.xi_start[8] unit = "1" fixed = true nominal = 1.0 stateSelect=StateSelect.prefer )  "Mass fraction" type: Real [9]
         deSO_ideal_L1_1.bulk.xi[9]:VARIABLE(min = 0.0 max = 1.0 start = deSO_ideal_L1_1.xi_start[9] unit = "1" fixed = true nominal = 1.0 stateSelect=StateSelect.prefer )  "Mass fraction" type: Real [9]
         deNOx.bulk.h:VARIABLE(start = deNOx.h_start unit = "J/kg" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer )  "Specific enthalpy" type: Real
         deNOx.bulk.xi[1]:VARIABLE(min = 0.0 max = 1.0 start = 9.910802775024783e-4 unit = "1" fixed = true nominal = 1.0 stateSelect=StateSelect.prefer )  "Mass fraction" type: Real [9]
         deNOx.bulk.xi[2]:VARIABLE(min = 0.0 max = 1.0 start = 9.910802775024783e-4 unit = "1" fixed = true nominal = 1.0 stateSelect=StateSelect.prefer )  "Mass fraction" type: Real [9]
         deNOx.bulk.xi[3]:VARIABLE(min = 0.0 max = 1.0 start = 9.910802775024783e-4 unit = "1" fixed = true nominal = 1.0 stateSelect=StateSelect.prefer )  "Mass fraction" type: Real [9]
         deNOx.bulk.xi[4]:VARIABLE(min = 0.0 max = 1.0 start = 9.910802775024783e-4 unit = "1" fixed = true nominal = 1.0 stateSelect=StateSelect.prefer )  "Mass fraction" type: Real [9]
         deNOx.bulk.xi[5]:VARIABLE(min = 0.0 max = 1.0 start = 0.9910802775024783 unit = "1" fixed = true nominal = 1.0 stateSelect=StateSelect.prefer )  "Mass fraction" type: Real [9]
         deNOx.bulk.xi[6]:VARIABLE(min = 0.0 max = 1.0 start = 9.910802775024783e-4 unit = "1" fixed = true nominal = 1.0 stateSelect=StateSelect.prefer )  "Mass fraction" type: Real [9]
         deNOx.bulk.xi[7]:VARIABLE(min = 0.0 max = 1.0 start = 9.910802775024783e-4 unit = "1" fixed = true nominal = 1.0 stateSelect=StateSelect.prefer )  "Mass fraction" type: Real [9]
         deNOx.bulk.xi[8]:VARIABLE(min = 0.0 max = 1.0 start = 9.910802775024783e-4 unit = "1" fixed = true nominal = 1.0 stateSelect=StateSelect.prefer )  "Mass fraction" type: Real [9]
         deNOx.bulk.xi[9]:VARIABLE(min = 0.0 max = 1.0 start = 9.910802775024783e-4 unit = "1" fixed = true nominal = 1.0 stateSelect=StateSelect.prefer )  "Mass fraction" type: Real [9]
         e_Filter_dynamic.bulk.h:VARIABLE(start = e_Filter_dynamic.h_start unit = "J/kg" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer )  "Specific enthalpy" type: Real
         e_Filter_dynamic.bulk.xi[1]:VARIABLE(min = 0.0 max = 1.0 start = e_Filter_dynamic.xi_start[1] unit = "1" fixed = true nominal = 1.0 stateSelect=StateSelect.prefer )  "Mass fraction" type: Real [9]
         e_Filter_dynamic.bulk.xi[2]:VARIABLE(min = 0.0 max = 1.0 start = e_Filter_dynamic.xi_start[2] unit = "1" fixed = true nominal = 1.0 stateSelect=StateSelect.prefer )  "Mass fraction" type: Real [9]
         e_Filter_dynamic.bulk.xi[3]:VARIABLE(min = 0.0 max = 1.0 start = e_Filter_dynamic.xi_start[3] unit = "1" fixed = true nominal = 1.0 stateSelect=StateSelect.prefer )  "Mass fraction" type: Real [9]
         e_Filter_dynamic.bulk.xi[4]:VARIABLE(min = 0.0 max = 1.0 start = e_Filter_dynamic.xi_start[4] unit = "1" fixed = true nominal = 1.0 stateSelect=StateSelect.prefer )  "Mass fraction" type: Real [9]
         e_Filter_dynamic.bulk.xi[5]:VARIABLE(min = 0.0 max = 1.0 start = e_Filter_dynamic.xi_start[5] unit = "1" fixed = true nominal = 1.0 stateSelect=StateSelect.prefer )  "Mass fraction" type: Real [9]
         e_Filter_dynamic.bulk.xi[6]:VARIABLE(min = 0.0 max = 1.0 start = e_Filter_dynamic.xi_start[6] unit = "1" fixed = true nominal = 1.0 stateSelect=StateSelect.prefer )  "Mass fraction" type: Real [9]
         e_Filter_dynamic.bulk.xi[7]:VARIABLE(min = 0.0 max = 1.0 start = e_Filter_dynamic.xi_start[7] unit = "1" fixed = true nominal = 1.0 stateSelect=StateSelect.prefer )  "Mass fraction" type: Real [9]
         e_Filter_dynamic.bulk.xi[8]:VARIABLE(min = 0.0 max = 1.0 start = e_Filter_dynamic.xi_start[8] unit = "1" fixed = true nominal = 1.0 stateSelect=StateSelect.prefer )  "Mass fraction" type: Real [9]
         e_Filter_dynamic.bulk.xi[9]:VARIABLE(min = 0.0 max = 1.0 start = e_Filter_dynamic.xi_start[9] unit = "1" fixed = true nominal = 1.0 stateSelect=StateSelect.prefer )  "Mass fraction" type: Real [9]
         e_Filter_dynamic1.bulk.h:VARIABLE(start = e_Filter_dynamic1.h_start unit = "J/kg" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer )  "Specific enthalpy" type: Real
         e_Filter_dynamic1.bulk.xi[1]:VARIABLE(min = 0.0 max = 1.0 start = 9.910802775024783e-4 unit = "1" fixed = true nominal = 1.0 stateSelect=StateSelect.prefer )  "Mass fraction" type: Real [9]
         e_Filter_dynamic1.bulk.xi[2]:VARIABLE(min = 0.0 max = 1.0 start = 9.910802775024783e-4 unit = "1" fixed = true nominal = 1.0 stateSelect=StateSelect.prefer )  "Mass fraction" type: Real [9]
         e_Filter_dynamic1.bulk.xi[3]:VARIABLE(min = 0.0 max = 1.0 start = 9.910802775024783e-4 unit = "1" fixed = true nominal = 1.0 stateSelect=StateSelect.prefer )  "Mass fraction" type: Real [9]
         e_Filter_dynamic1.bulk.xi[4]:VARIABLE(min = 0.0 max = 1.0 start = 9.910802775024783e-4 unit = "1" fixed = true nominal = 1.0 stateSelect=StateSelect.prefer )  "Mass fraction" type: Real [9]
         e_Filter_dynamic1.bulk.xi[5]:VARIABLE(min = 0.0 max = 1.0 start = 0.9910802775024783 unit = "1" fixed = true nominal = 1.0 stateSelect=StateSelect.prefer )  "Mass fraction" type: Real [9]
         e_Filter_dynamic1.bulk.xi[6]:VARIABLE(min = 0.0 max = 1.0 start = 9.910802775024783e-4 unit = "1" fixed = true nominal = 1.0 stateSelect=StateSelect.prefer )  "Mass fraction" type: Real [9]
         e_Filter_dynamic1.bulk.xi[7]:VARIABLE(min = 0.0 max = 1.0 start = 9.910802775024783e-4 unit = "1" fixed = true nominal = 1.0 stateSelect=StateSelect.prefer )  "Mass fraction" type: Real [9]
         e_Filter_dynamic1.bulk.xi[8]:VARIABLE(min = 0.0 max = 1.0 start = 9.910802775024783e-4 unit = "1" fixed = true nominal = 1.0 stateSelect=StateSelect.prefer )  "Mass fraction" type: Real [9]
         e_Filter_dynamic1.bulk.xi[9]:VARIABLE(min = 0.0 max = 1.0 start = 9.910802775024783e-4 unit = "1" fixed = true nominal = 1.0 stateSelect=StateSelect.prefer )  "Mass fraction" type: Real [9]
         e_Filter_dynamic2.bulk.h:VARIABLE(start = e_Filter_dynamic2.h_start unit = "J/kg" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer )  "Specific enthalpy" type: Real
         e_Filter_dynamic2.bulk.xi[1]:VARIABLE(min = 0.0 max = 1.0 start = e_Filter_dynamic2.xi_start[1] unit = "1" fixed = true nominal = 1.0 stateSelect=StateSelect.prefer )  "Mass fraction" type: Real [9]
         e_Filter_dynamic2.bulk.xi[2]:VARIABLE(min = 0.0 max = 1.0 start = e_Filter_dynamic2.xi_start[2] unit = "1" fixed = true nominal = 1.0 stateSelect=StateSelect.prefer )  "Mass fraction" type: Real [9]
         e_Filter_dynamic2.bulk.xi[3]:VARIABLE(min = 0.0 max = 1.0 start = e_Filter_dynamic2.xi_start[3] unit = "1" fixed = true nominal = 1.0 stateSelect=StateSelect.prefer )  "Mass fraction" type: Real [9]
         e_Filter_dynamic2.bulk.xi[4]:VARIABLE(min = 0.0 max = 1.0 start = e_Filter_dynamic2.xi_start[4] unit = "1" fixed = true nominal = 1.0 stateSelect=StateSelect.prefer )  "Mass fraction" type: Real [9]
         e_Filter_dynamic2.bulk.xi[5]:VARIABLE(min = 0.0 max = 1.0 start = e_Filter_dynamic2.xi_start[5] unit = "1" fixed = true nominal = 1.0 stateSelect=StateSelect.prefer )  "Mass fraction" type: Real [9]
         e_Filter_dynamic2.bulk.xi[6]:VARIABLE(min = 0.0 max = 1.0 start = e_Filter_dynamic2.xi_start[6] unit = "1" fixed = true nominal = 1.0 stateSelect=StateSelect.prefer )  "Mass fraction" type: Real [9]
         e_Filter_dynamic2.bulk.xi[7]:VARIABLE(min = 0.0 max = 1.0 start = e_Filter_dynamic2.xi_start[7] unit = "1" fixed = true nominal = 1.0 stateSelect=StateSelect.prefer )  "Mass fraction" type: Real [9]
         e_Filter_dynamic2.bulk.xi[8]:VARIABLE(min = 0.0 max = 1.0 start = e_Filter_dynamic2.xi_start[8] unit = "1" fixed = true nominal = 1.0 stateSelect=StateSelect.prefer )  "Mass fraction" type: Real [9]
         e_Filter_dynamic2.bulk.xi[9]:VARIABLE(min = 0.0 max = 1.0 start = e_Filter_dynamic2.xi_start[9] unit = "1" fixed = true nominal = 1.0 stateSelect=StateSelect.prefer )  "Mass fraction" type: Real [9]
         pipeFlowGas_L4_Simple.h[1]:VARIABLE(start = pipeFlowGas_L4_Simple.h_start[1] unit = "J/kg" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer )  "Cell enthalpy" type: Real [3]
         pipeFlowGas_L4_Simple.h[2]:VARIABLE(start = pipeFlowGas_L4_Simple.h_start[2] unit = "J/kg" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer )  "Cell enthalpy" type: Real [3]
         pipeFlowGas_L4_Simple.h[3]:VARIABLE(start = pipeFlowGas_L4_Simple.h_start[3] unit = "J/kg" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer )  "Cell enthalpy" type: Real [3]
         pipeFlowGas_L4_Simple.p[1]:VARIABLE(min = 0.0 start = pipeFlowGas_L4_Simple.p_start[1] unit = "Pa" fixed = true nominal = 1e5 protected = true )  "Cell pressure" type: Real [3]
         pipeFlowGas_L4_Simple.p[2]:VARIABLE(min = 0.0 start = pipeFlowGas_L4_Simple.p_start[2] unit = "Pa" fixed = true nominal = 1e5 protected = true )  "Cell pressure" type: Real [3]
         pipeFlowGas_L4_Simple.p[3]:VARIABLE(min = 0.0 start = pipeFlowGas_L4_Simple.p_start[3] unit = "Pa" fixed = true nominal = 1e5 protected = true )  "Cell pressure" type: Real [3]
Notification: Model statistics after passing the back-end for initialization:
 * Number of independent subsystems: 197
 * 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 (1394):
 * Single equations (assignments): 1313
 * Array equations: 0
 * Algorithm blocks: 0
 * Record equations: 71
 * When equations: 0
 * If-equations: 0
 * Equation systems (not torn): 1
 * Torn equation systems: 9
 * 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): 4 systems
   {(1,1,100.0%), (1,1,100.0%), (1,1,100.0%), (1,3,100.0%)}
 * Non-linear torn systems (#iteration vars, #inner vars): 5 systems
   {(2,29), (1,27), (1,28), (1,23), (1,22)}
Notification: Performance of prepare postOptimizeDAE: time 0.008283/4.922, allocations: 1.176 MB / 1.996 GB, free: 288.3 MB / 0.9045 GB
Notification: Performance of postOpt lateInlineFunction (simulation): time 0.007154/4.929, allocations: 2.517 MB / 1.999 GB, free: 288.3 MB / 0.9045 GB
Notification: Performance of postOpt wrapFunctionCalls (simulation): time 0.09693/5.026, allocations: 50.18 MB / 2.048 GB, free: 270.4 MB / 0.9045 GB
Notification: Performance of postOpt simplifysemiLinear (simulation): time 0.07459/5.101, allocations: 44.14 MB / 2.091 GB, free: 226.3 MB / 0.9045 GB
Notification: Performance of postOpt simplifyComplexFunction (simulation): time 0.000557/5.101, allocations: 147.8 kB / 2.091 GB, free: 226.1 MB / 0.9045 GB
Notification: Performance of postOpt removeConstants (simulation): time 0.02018/5.122, allocations: 6.702 MB / 2.098 GB, free: 220.8 MB / 0.9045 GB
Notification: Performance of postOpt simplifyTimeIndepFuncCalls (simulation): time 0.00882/5.131, allocations: 315.9 kB / 2.098 GB, free: 220.5 MB / 0.9045 GB
Notification: Performance of postOpt simplifyAllExpressions (simulation): time 0.01733/5.148, allocations: 460.4 kB / 2.098 GB, free: 220.1 MB / 0.9045 GB
Notification: Performance of postOpt findZeroCrossings (simulation): time 0.006165/5.154, allocations: 0.8556 MB / 2.099 GB, free: 219.2 MB / 0.9045 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): (e_Filter_dynamic2.flueGasOutlet.d, e_Filter_dynamic2.flueGasOutlet.kappa, e_Filter_dynamic2.flueGasOutlet.drhodp_hxi, e_Filter_dynamic2.flueGasOutlet.drhodh_pxi, e_Filter_dynamic2.flueGasOutlet.drhodxi_ph, e_Filter_dynamic2.flueGasOutlet.p_i, e_Filter_dynamic2.flueGasOutlet.xi_gas) = TILMedia.Internals.GasObjectFunctions.additionalProperties_pTxi(idealGasPressureSink3.p_const, e_Filter_dynamic2.flueGasOutlet.T, e_Filter_dynamic2.flueGasOutlet.xi, e_Filter_dynamic2.flueGasOutlet.gasPointer)

Variables:
1: e_Filter_dynamic2.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]
2: e_Filter_dynamic2.flueGasOutlet.p_i[2]:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 )  "Partial pressure" type: Real [10]
3: e_Filter_dynamic2.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]
4: e_Filter_dynamic2.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]
5: e_Filter_dynamic2.flueGasOutlet.p_i[5]:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 )  "Partial pressure" type: Real [10]
6: e_Filter_dynamic2.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]
7: e_Filter_dynamic2.flueGasOutlet.p_i[10]:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 )  "Partial pressure" type: Real [10]
8: e_Filter_dynamic2.flueGasOutlet.p_i[1]:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 )  "Partial pressure" type: Real [10]
9: e_Filter_dynamic2.flueGasOutlet.drhodh_pxi:VARIABLE(unit = "kg.s2/m5" )  "Derivative of density wrt specific enthalpy at constant pressure and mass fraction" type: Real
10: e_Filter_dynamic2.flueGasOutlet.p_i[7]:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 )  "Partial pressure" type: Real [10]
11: e_Filter_dynamic2.flueGasOutlet.d:VARIABLE(min = 0.0 unit = "kg/m3" )  "Density" type: Real
12: e_Filter_dynamic2.flueGasOutlet.p_i[3]:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 )  "Partial pressure" type: Real [10]
13: e_Filter_dynamic2.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]
14: e_Filter_dynamic2.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]
15: e_Filter_dynamic2.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]
16: e_Filter_dynamic2.flueGasOutlet.xi_gas:VARIABLE(min = 0.0 max = 1.0 unit = "1" )  "Mass fraction of gasoues condensing component" type: Real
17: e_Filter_dynamic2.flueGasOutlet.p_i[6]:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 )  "Partial pressure" type: Real [10]
18: e_Filter_dynamic2.flueGasOutlet.p_i[4]:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 )  "Partial pressure" type: Real [10]
19: e_Filter_dynamic2.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]
20: e_Filter_dynamic2.flueGasOutlet.p_i[9]:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 )  "Partial pressure" type: Real [10]
21: e_Filter_dynamic2.flueGasOutlet.p_i[8]:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 )  "Partial pressure" type: Real [10]
22: e_Filter_dynamic2.flueGasOutlet.kappa:VARIABLE(unit = "1/Pa" )  "Isothermal compressibility" type: Real
23: e_Filter_dynamic2.flueGasOutlet.drhodp_hxi:VARIABLE(unit = "s2/m2" )  "Derivative of density wrt pressure at specific enthalpy and mass fraction" type: Real
24: e_Filter_dynamic2.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]
[/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): e_Filter_dynamic2.chemicalReactions.V_flow = if pipeFlowGas_L4_Simple.heatTransfer.m_flow[4] > 0.0 and e_Filter_dynamic2.outlet.m_flow <= 0.0 then e_Filter_dynamic2.iCom.V_flow_in else if pipeFlowGas_L4_Simple.heatTransfer.m_flow[4] > 0.0 then e_Filter_dynamic2.iCom.V_flow_in + e_Filter_dynamic2.iCom.V_flow_out else if pipeFlowGas_L4_Simple.heatTransfer.m_flow[4] <= 0.0 and e_Filter_dynamic2.outlet.m_flow <= 0.0 then 1e-20 else e_Filter_dynamic2.iCom.V_flow_out
2/2 (1): e_Filter_dynamic2.iCom.V_flow_out = abs(e_Filter_dynamic2.outlet.m_flow / e_Filter_dynamic2.flueGasOutlet.d)
3/3 (1): e_Filter_dynamic2.flueGasOutlet.T = if noEvent(e_Filter_dynamic2.outlet.m_flow > 0.0) then idealGasPressureSink3.T_const else e_Filter_dynamic2.bulk.T
4/4 (24): (e_Filter_dynamic2.flueGasOutlet.d, e_Filter_dynamic2.flueGasOutlet.kappa, e_Filter_dynamic2.flueGasOutlet.drhodp_hxi, e_Filter_dynamic2.flueGasOutlet.drhodh_pxi, e_Filter_dynamic2.flueGasOutlet.drhodxi_ph, e_Filter_dynamic2.flueGasOutlet.p_i, e_Filter_dynamic2.flueGasOutlet.xi_gas) = TILMedia.Internals.GasObjectFunctions.additionalProperties_pTxi(idealGasPressureSink3.p_const, e_Filter_dynamic2.flueGasOutlet.T, e_Filter_dynamic2.flueGasOutlet.xi, e_Filter_dynamic2.flueGasOutlet.gasPointer)
5/28 (1): e_Filter_dynamic2.flueGasOutlet.h = TILMedia.Internals.GasObjectFunctions.specificEnthalpy_pTxi(idealGasPressureSink3.p_const, e_Filter_dynamic2.flueGasOutlet.T, e_Filter_dynamic2.flueGasOutlet.xi, e_Filter_dynamic2.flueGasOutlet.gasPointer)
6/29 (1): der(e_Filter_dynamic2.bulk.h) = (pipeFlowGas_L4_Simple.heatTransfer.m_flow[4] * (e_Filter_dynamic2.chemicalReactions.h_aux - e_Filter_dynamic2.bulk.h) + e_Filter_dynamic2.outlet.m_flow * (e_Filter_dynamic2.flueGasOutlet.h - e_Filter_dynamic2.bulk.h) + e_Filter_dynamic2.chemicalReactions.m_flow_reaction[1] * (e_Filter_dynamic2.chemicalReactions.h_reaction[1] - e_Filter_dynamic2.bulk.h)) / e_Filter_dynamic2.chemicalReactions.mass
7/30 (1): pipeFlowGas_L4_Simple.heatTransfer.m_flow[4] + e_Filter_dynamic2.outlet.m_flow + e_Filter_dynamic2.chemicalReactions.m_flow_reaction[1] = e_Filter_dynamic2.drhodt * e_Filter_dynamic2.geo.volume
8/31 (1): e_Filter_dynamic2.drhodt = e_Filter_dynamic2.bulk.drhodh_pxi * der(e_Filter_dynamic2.bulk.h) + e_Filter_dynamic2.bulk.drhodxi_ph[1] * der(e_Filter_dynamic2.bulk.xi[1]) + e_Filter_dynamic2.bulk.drhodxi_ph[2] * der(e_Filter_dynamic2.bulk.xi[2]) + e_Filter_dynamic2.bulk.drhodxi_ph[3] * der(e_Filter_dynamic2.bulk.xi[3]) + e_Filter_dynamic2.bulk.drhodxi_ph[4] * der(e_Filter_dynamic2.bulk.xi[4]) + e_Filter_dynamic2.bulk.drhodxi_ph[5] * der(e_Filter_dynamic2.bulk.xi[5]) + e_Filter_dynamic2.bulk.drhodxi_ph[6] * der(e_Filter_dynamic2.bulk.xi[6]) + e_Filter_dynamic2.bulk.drhodxi_ph[7] * der(e_Filter_dynamic2.bulk.xi[7]) + e_Filter_dynamic2.bulk.drhodxi_ph[8] * der(e_Filter_dynamic2.bulk.xi[8]) + e_Filter_dynamic2.bulk.drhodxi_ph[9] * der(e_Filter_dynamic2.bulk.xi[9])
9/32 (1): der(e_Filter_dynamic2.bulk.xi[9]) = (pipeFlowGas_L4_Simple.heatTransfer.m_flow[4] * (e_Filter_dynamic2.chemicalReactions.xi_aux[9] - e_Filter_dynamic2.bulk.xi[9]) + e_Filter_dynamic2.outlet.m_flow * (e_Filter_dynamic2.flueGasOutlet.xi[9] - e_Filter_dynamic2.bulk.xi[9]) - e_Filter_dynamic2.chemicalReactions.m_flow_reaction[1] * e_Filter_dynamic2.bulk.xi[9]) / e_Filter_dynamic2.chemicalReactions.mass
10/33 (1): der(e_Filter_dynamic2.bulk.xi[8]) = (pipeFlowGas_L4_Simple.heatTransfer.m_flow[4] * (e_Filter_dynamic2.chemicalReactions.xi_aux[8] - e_Filter_dynamic2.bulk.xi[8]) + e_Filter_dynamic2.outlet.m_flow * (e_Filter_dynamic2.flueGasOutlet.xi[8] - e_Filter_dynamic2.bulk.xi[8]) - e_Filter_dynamic2.chemicalReactions.m_flow_reaction[1] * e_Filter_dynamic2.bulk.xi[8]) / e_Filter_dynamic2.chemicalReactions.mass
11/34 (1): der(e_Filter_dynamic2.bulk.xi[7]) = (pipeFlowGas_L4_Simple.heatTransfer.m_flow[4] * (e_Filter_dynamic2.chemicalReactions.xi_aux[7] - e_Filter_dynamic2.bulk.xi[7]) + e_Filter_dynamic2.outlet.m_flow * (e_Filter_dynamic2.flueGasOutlet.xi[7] - e_Filter_dynamic2.bulk.xi[7]) - e_Filter_dynamic2.chemicalReactions.m_flow_reaction[1] * e_Filter_dynamic2.bulk.xi[7]) / e_Filter_dynamic2.chemicalReactions.mass
12/35 (1): der(e_Filter_dynamic2.bulk.xi[6]) = (pipeFlowGas_L4_Simple.heatTransfer.m_flow[4] * (e_Filter_dynamic2.chemicalReactions.xi_aux[6] - e_Filter_dynamic2.bulk.xi[6]) + e_Filter_dynamic2.outlet.m_flow * (e_Filter_dynamic2.flueGasOutlet.xi[6] - e_Filter_dynamic2.bulk.xi[6]) - e_Filter_dynamic2.chemicalReactions.m_flow_reaction[1] * e_Filter_dynamic2.bulk.xi[6]) / e_Filter_dynamic2.chemicalReactions.mass
13/36 (1): der(e_Filter_dynamic2.bulk.xi[5]) = (pipeFlowGas_L4_Simple.heatTransfer.m_flow[4] * (e_Filter_dynamic2.chemicalReactions.xi_aux[5] - e_Filter_dynamic2.bulk.xi[5]) + e_Filter_dynamic2.outlet.m_flow * (e_Filter_dynamic2.flueGasOutlet.xi[5] - e_Filter_dynamic2.bulk.xi[5]) + e_Filter_dynamic2.chemicalReactions.m_flow_reaction[1] * (1e-5 - e_Filter_dynamic2.bulk.xi[5])) / e_Filter_dynamic2.chemicalReactions.mass
14/37 (1): der(e_Filter_dynamic2.bulk.xi[4]) = (pipeFlowGas_L4_Simple.heatTransfer.m_flow[4] * (e_Filter_dynamic2.chemicalReactions.xi_aux[4] - e_Filter_dynamic2.bulk.xi[4]) + e_Filter_dynamic2.outlet.m_flow * (e_Filter_dynamic2.flueGasOutlet.xi[4] - e_Filter_dynamic2.bulk.xi[4]) - e_Filter_dynamic2.chemicalReactions.m_flow_reaction[1] * e_Filter_dynamic2.bulk.xi[4]) / e_Filter_dynamic2.chemicalReactions.mass
15/38 (1): der(e_Filter_dynamic2.bulk.xi[3]) = (pipeFlowGas_L4_Simple.heatTransfer.m_flow[4] * (e_Filter_dynamic2.chemicalReactions.xi_aux[3] - e_Filter_dynamic2.bulk.xi[3]) + e_Filter_dynamic2.outlet.m_flow * (e_Filter_dynamic2.flueGasOutlet.xi[3] - e_Filter_dynamic2.bulk.xi[3]) - e_Filter_dynamic2.chemicalReactions.m_flow_reaction[1] * e_Filter_dynamic2.bulk.xi[3]) / e_Filter_dynamic2.chemicalReactions.mass
16/39 (1): der(e_Filter_dynamic2.bulk.xi[2]) = (pipeFlowGas_L4_Simple.heatTransfer.m_flow[4] * (e_Filter_dynamic2.chemicalReactions.xi_aux[2] - e_Filter_dynamic2.bulk.xi[2]) + e_Filter_dynamic2.outlet.m_flow * (e_Filter_dynamic2.flueGasOutlet.xi[2] - e_Filter_dynamic2.bulk.xi[2]) - e_Filter_dynamic2.chemicalReactions.m_flow_reaction[1] * e_Filter_dynamic2.bulk.xi[2]) / e_Filter_dynamic2.chemicalReactions.mass
17/40 (1): der(e_Filter_dynamic2.bulk.xi[1]) = (pipeFlowGas_L4_Simple.heatTransfer.m_flow[4] * (e_Filter_dynamic2.chemicalReactions.xi_aux[1] - e_Filter_dynamic2.bulk.xi[1]) + e_Filter_dynamic2.outlet.m_flow * (e_Filter_dynamic2.flueGasOutlet.xi[1] - e_Filter_dynamic2.bulk.xi[1]) + e_Filter_dynamic2.chemicalReactions.m_flow_reaction[1] * (0.99999 - e_Filter_dynamic2.bulk.xi[1])) / e_Filter_dynamic2.chemicalReactions.mass
18/41 (1): e_Filter_dynamic2.chemicalReactions.m_flow_reaction[1] = if pipeFlowGas_L4_Simple.heatTransfer.m_flow[4] > 0.0 and e_Filter_dynamic2.outlet.m_flow <= 0.0 then e_Filter_dynamic2.chemicalReactions.separationRate * (-e_Filter_dynamic2.chemicalReactions.xi_aux[1]) * pipeFlowGas_L4_Simple.heatTransfer.m_flow[4] else if pipeFlowGas_L4_Simple.heatTransfer.m_flow[4] > 0.0 then e_Filter_dynamic2.chemicalReactions.separationRate * ((-e_Filter_dynamic2.flueGasOutlet.xi[1]) * e_Filter_dynamic2.outlet.m_flow - e_Filter_dynamic2.chemicalReactions.xi_aux[1] * pipeFlowGas_L4_Simple.heatTransfer.m_flow[4]) else if pipeFlowGas_L4_Simple.heatTransfer.m_flow[4] <= 0.0 and e_Filter_dynamic2.outlet.m_flow <= 0.0 then 1e-20 else e_Filter_dynamic2.chemicalReactions.separationRate * (-e_Filter_dynamic2.flueGasOutlet.xi[1]) * e_Filter_dynamic2.outlet.m_flow
19/42 (1): e_Filter_dynamic2.chemicalReactions.separationRate = 1.0 - $cse4
20/43 (1): $cse4 = exp((-e_Filter_dynamic2.chemicalReactions.w_m) * e_Filter_dynamic2.chemicalReactions.A_filter / e_Filter_dynamic2.chemicalReactions.V_flow)
21/44 (1): e_Filter_dynamic2.flueGasOutlet.xi[9] = if noEvent(e_Filter_dynamic2.outlet.m_flow > 0.0) then idealGasPressureSink3.xi_const[9] else e_Filter_dynamic2.bulk.xi[9]
22/45 (1): e_Filter_dynamic2.flueGasOutlet.xi[8] = if noEvent(e_Filter_dynamic2.outlet.m_flow > 0.0) then idealGasPressureSink3.xi_const[8] else e_Filter_dynamic2.bulk.xi[8]
23/46 (1): e_Filter_dynamic2.flueGasOutlet.xi[7] = if noEvent(e_Filter_dynamic2.outlet.m_flow > 0.0) then idealGasPressureSink3.xi_const[7] else e_Filter_dynamic2.bulk.xi[7]
24/47 (1): e_Filter_dynamic2.flueGasOutlet.xi[6] = if noEvent(e_Filter_dynamic2.outlet.m_flow > 0.0) then idealGasPressureSink3.xi_const[6] else e_Filter_dynamic2.bulk.xi[6]
25/48 (1): e_Filter_dynamic2.flueGasOutlet.xi[5] = if noEvent(e_Filter_dynamic2.outlet.m_flow > 0.0) then idealGasPressureSink3.xi_const[5] else e_Filter_dynamic2.bulk.xi[5]
26/49 (1): e_Filter_dynamic2.flueGasOutlet.xi[4] = if noEvent(e_Filter_dynamic2.outlet.m_flow > 0.0) then idealGasPressureSink3.xi_const[4] else e_Filter_dynamic2.bulk.xi[4]
27/50 (1): e_Filter_dynamic2.flueGasOutlet.xi[3] = if noEvent(e_Filter_dynamic2.outlet.m_flow > 0.0) then idealGasPressureSink3.xi_const[3] else e_Filter_dynamic2.bulk.xi[3]
28/51 (1): e_Filter_dynamic2.flueGasOutlet.xi[2] = if noEvent(e_Filter_dynamic2.outlet.m_flow > 0.0) then idealGasPressureSink3.xi_const[2] else e_Filter_dynamic2.bulk.xi[2]
29/52 (1): e_Filter_dynamic2.flueGasOutlet.xi[1] = if noEvent(e_Filter_dynamic2.outlet.m_flow > 0.0) then idealGasPressureSink3.xi_const[1] else e_Filter_dynamic2.bulk.xi[1]

Variables:
1: e_Filter_dynamic2.flueGasOutlet.xi[1]:VARIABLE(min = 0.0 max = 1.0 unit = "1" nominal = 1.0 )  "Mass fraction" type: Real [9]
2: e_Filter_dynamic2.flueGasOutlet.xi[2]:VARIABLE(min = 0.0 max = 1.0 unit = "1" nominal = 1.0 )  "Mass fraction" type: Real [9]
3: e_Filter_dynamic2.flueGasOutlet.xi[3]:VARIABLE(min = 0.0 max = 1.0 unit = "1" nominal = 1.0 )  "Mass fraction" type: Real [9]
4: e_Filter_dynamic2.flueGasOutlet.xi[4]:VARIABLE(min = 0.0 max = 1.0 unit = "1" nominal = 1.0 )  "Mass fraction" type: Real [9]
5: e_Filter_dynamic2.flueGasOutlet.xi[5]:VARIABLE(min = 0.0 max = 1.0 unit = "1" nominal = 1.0 )  "Mass fraction" type: Real [9]
6: e_Filter_dynamic2.flueGasOutlet.xi[6]:VARIABLE(min = 0.0 max = 1.0 unit = "1" nominal = 1.0 )  "Mass fraction" type: Real [9]
7: e_Filter_dynamic2.flueGasOutlet.xi[7]:VARIABLE(min = 0.0 max = 1.0 unit = "1" nominal = 1.0 )  "Mass fraction" type: Real [9]
8: e_Filter_dynamic2.flueGasOutlet.xi[8]:VARIABLE(min = 0.0 max = 1.0 unit = "1" nominal = 1.0 )  "Mass fraction" type: Real [9]
9: e_Filter_dynamic2.flueGasOutlet.xi[9]:VARIABLE(min = 0.0 max = 1.0 unit = "1" nominal = 1.0 )  "Mass fraction" type: Real [9]
10: e_Filter_dynamic2.chemicalReactions.V_flow:VARIABLE(unit = "m3/s" nominal = 1.0 )  "Volume flow rate of flue Gas entering the E-Filter" type: Real
11: $cse4:VARIABLE(protected = true )  type: Real unreplaceable
12: e_Filter_dynamic2.chemicalReactions.separationRate:VARIABLE()  "Separation rate" type: Real
13: e_Filter_dynamic2.bulk.xi[1]:STATE(1)(min = 0.0 max = 1.0 start = e_Filter_dynamic2.xi_start[1] unit = "1" fixed = true nominal = 1.0 stateSelect=StateSelect.prefer )  "Mass fraction" type: Real [9]
14: e_Filter_dynamic2.bulk.xi[2]:STATE(1)(min = 0.0 max = 1.0 start = e_Filter_dynamic2.xi_start[2] unit = "1" fixed = true nominal = 1.0 stateSelect=StateSelect.prefer )  "Mass fraction" type: Real [9]
15: e_Filter_dynamic2.bulk.xi[3]:STATE(1)(min = 0.0 max = 1.0 start = e_Filter_dynamic2.xi_start[3] unit = "1" fixed = true nominal = 1.0 stateSelect=StateSelect.prefer )  "Mass fraction" type: Real [9]
16: e_Filter_dynamic2.bulk.xi[4]:STATE(1)(min = 0.0 max = 1.0 start = e_Filter_dynamic2.xi_start[4] unit = "1" fixed = true nominal = 1.0 stateSelect=StateSelect.prefer )  "Mass fraction" type: Real [9]
17: e_Filter_dynamic2.bulk.xi[5]:STATE(1)(min = 0.0 max = 1.0 start = e_Filter_dynamic2.xi_start[5] unit = "1" fixed = true nominal = 1.0 stateSelect=StateSelect.prefer )  "Mass fraction" type: Real [9]
18: e_Filter_dynamic2.bulk.xi[6]:STATE(1)(min = 0.0 max = 1.0 start = e_Filter_dynamic2.xi_start[6] unit = "1" fixed = true nominal = 1.0 stateSelect=StateSelect.prefer )  "Mass fraction" type: Real [9]
19: e_Filter_dynamic2.bulk.xi[7]:STATE(1)(min = 0.0 max = 1.0 start = e_Filter_dynamic2.xi_start[7] unit = "1" fixed = true nominal = 1.0 stateSelect=StateSelect.prefer )  "Mass fraction" type: Real [9]
20: e_Filter_dynamic2.bulk.xi[8]:STATE(1)(min = 0.0 max = 1.0 start = e_Filter_dynamic2.xi_start[8] unit = "1" fixed = true nominal = 1.0 stateSelect=StateSelect.prefer )  "Mass fraction" type: Real [9]
21: e_Filter_dynamic2.bulk.xi[9]:STATE(1)(min = 0.0 max = 1.0 start = e_Filter_dynamic2.xi_start[9] unit = "1" fixed = true nominal = 1.0 stateSelect=StateSelect.prefer )  "Mass fraction" type: Real [9]
22: e_Filter_dynamic2.bulk.h:STATE(1)(start = e_Filter_dynamic2.h_start unit = "J/kg" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer )  "Specific enthalpy" type: Real
23: e_Filter_dynamic2.drhodt:VARIABLE(protected = true )  "Density derivative" type: Real
24: e_Filter_dynamic2.chemicalReactions.m_flow_reaction[1]:VARIABLE(unit = "kg/s" nominal = 1.0 )  type: Real [1]
25: e_Filter_dynamic2.flueGasOutlet.h:VARIABLE(unit = "J/kg" nominal = 1000.0 )  "Specific enthalpy" type: Real
26: e_Filter_dynamic2.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]
27: e_Filter_dynamic2.flueGasOutlet.p_i[2]:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 )  "Partial pressure" type: Real [10]
28: e_Filter_dynamic2.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]
29: e_Filter_dynamic2.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]
30: e_Filter_dynamic2.flueGasOutlet.p_i[5]:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 )  "Partial pressure" type: Real [10]
31: e_Filter_dynamic2.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]
32: e_Filter_dynamic2.flueGasOutlet.p_i[10]:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 )  "Partial pressure" type: Real [10]
33: e_Filter_dynamic2.flueGasOutlet.p_i[1]:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 )  "Partial pressure" type: Real [10]
34: e_Filter_dynamic2.flueGasOutlet.drhodh_pxi:VARIABLE(unit = "kg.s2/m5" )  "Derivative of density wrt specific enthalpy at constant pressure and mass fraction" type: Real
35: e_Filter_dynamic2.flueGasOutlet.p_i[7]:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 )  "Partial pressure" type: Real [10]
36: e_Filter_dynamic2.flueGasOutlet.d:VARIABLE(min = 0.0 unit = "kg/m3" )  "Density" type: Real
37: e_Filter_dynamic2.flueGasOutlet.p_i[3]:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 )  "Partial pressure" type: Real [10]
38: e_Filter_dynamic2.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]
39: e_Filter_dynamic2.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]
40: e_Filter_dynamic2.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]
41: e_Filter_dynamic2.flueGasOutlet.xi_gas:VARIABLE(min = 0.0 max = 1.0 unit = "1" )  "Mass fraction of gasoues condensing component" type: Real
42: e_Filter_dynamic2.flueGasOutlet.p_i[6]:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 )  "Partial pressure" type: Real [10]
43: e_Filter_dynamic2.flueGasOutlet.p_i[4]:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 )  "Partial pressure" type: Real [10]
44: e_Filter_dynamic2.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]
45: e_Filter_dynamic2.flueGasOutlet.p_i[9]:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 )  "Partial pressure" type: Real [10]
46: e_Filter_dynamic2.flueGasOutlet.p_i[8]:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 )  "Partial pressure" type: Real [10]
47: e_Filter_dynamic2.flueGasOutlet.kappa:VARIABLE(unit = "1/Pa" )  "Isothermal compressibility" type: Real
48: e_Filter_dynamic2.flueGasOutlet.drhodp_hxi:VARIABLE(unit = "s2/m2" )  "Derivative of density wrt pressure at specific enthalpy and mass fraction" type: Real
49: e_Filter_dynamic2.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]
50: e_Filter_dynamic2.flueGasOutlet.T:VARIABLE(min = 0.0 start = 288.15 unit = "K" nominal = 300.0 )  "Temperature" type: Real
51: e_Filter_dynamic2.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: e_Filter_dynamic2.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 <failed> postOpt createDAEmodeBDAE (simulation): time 0.02159/5.176, allocations: 5.709 MB / 2.105 GB, free: 213 MB / 0.9045 GB
Error: post-optimization module createDAEmodeBDAE (simulation) failed.
Error: Internal error SimCode DAEmode: The model ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning could not be translated