Running: ./testmodel.py --libraries=/home/hudson/saved_omc/libraries/.openmodelica/libraries --ompython_omhome=/usr ClaRa_dev_ClaRa.Components.Mills.HardCoalMills.Check.combineMillandFurnace.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.Mills.HardCoalMills.Check.combineMillandFurnace,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|NonlinearSystems.simulation.2..Calls|NonlinearSystems.simulation.2..Iterations|NonlinearSystems.simulation.2..Jacobians|NonlinearSystems.simulation.2..Residues|PTarget1.duration|PTarget1.height|PTarget1.offset|PTarget1.startTime|PTarget1.y|Time|coalFlowSource.T_const|coalFlowSource.contributeToCycleSummary|coalFlowSource.energyType|coalFlowSource.fuelModel.C_LHV.1.|coalFlowSource.fuelModel.C_LHV.2.|coalFlowSource.fuelModel.C_LHV.3.|coalFlowSource.fuelModel.C_LHV.4.|coalFlowSource.fuelModel.C_LHV.5.|coalFlowSource.fuelModel.C_LHV.6.|coalFlowSource.fuelModel.C_LHV.7.|coalFlowSource.fuelModel.C_cp.1.|coalFlowSource.fuelModel.C_cp.2.|coalFlowSource.fuelModel.C_cp.3.|coalFlowSource.fuelModel.C_cp.4.|coalFlowSource.fuelModel.C_cp.5.|coalFlowSource.fuelModel.C_cp.6.|coalFlowSource.fuelModel.C_cp.7.|coalFlowSource.fuelModel.C_rho.1.|coalFlowSource.fuelModel.C_rho.2.|coalFlowSource.fuelModel.C_rho.3.|coalFlowSource.fuelModel.C_rho.4.|coalFlowSource.fuelModel.C_rho.5.|coalFlowSource.fuelModel.C_rho.6.|coalFlowSource.fuelModel.C_rho.7.|coalFlowSource.fuelModel.N_c|coalFlowSource.fuelModel.N_e|coalFlowSource.fuelModel.T_ref|coalFlowSource.fuelModel.ashIndex|coalFlowSource.fuelModel.defaultComposition.1.|coalFlowSource.fuelModel.defaultComposition.2.|coalFlowSource.fuelModel.defaultComposition.3.|coalFlowSource.fuelModel.defaultComposition.4.|coalFlowSource.fuelModel.defaultComposition.5.|coalFlowSource.fuelModel.defaultComposition.6.|coalFlowSource.fuelModel.waterIndex|coalFlowSource.fuel_a.T_outflow|coalFlowSource.fuel_a.fuelModel.C_LHV.1.|coalFlowSource.fuel_a.fuelModel.C_LHV.2.|coalFlowSource.fuel_a.fuelModel.C_LHV.3.|coalFlowSource.fuel_a.fuelModel.C_LHV.4.|coalFlowSource.fuel_a.fuelModel.C_LHV.5.|coalFlowSource.fuel_a.fuelModel.C_LHV.6.|coalFlowSource.fuel_a.fuelModel.C_LHV.7.|coalFlowSource.fuel_a.fuelModel.C_cp.1.|coalFlowSource.fuel_a.fuelModel.C_cp.2.|coalFlowSource.fuel_a.fuelModel.C_cp.3.|coalFlowSource.fuel_a.fuelModel.C_cp.4.|coalFlowSource.fuel_a.fuelModel.C_cp.5.|coalFlowSource.fuel_a.fuelModel.C_cp.6.|coalFlowSource.fuel_a.fuelModel.C_cp.7.|coalFlowSource.fuel_a.fuelModel.C_rho.1.|coalFlowSource.fuel_a.fuelModel.C_rho.2.|coalFlowSource.fuel_a.fuelModel.C_rho.3.|coalFlowSource.fuel_a.fuelModel.C_rho.4.|coalFlowSource.fuel_a.fuelModel.C_rho.5.|coalFlowSource.fuel_a.fuelModel.C_rho.6.|coalFlowSource.fuel_a.fuelModel.C_rho.7.|coalFlowSource.fuel_a.fuelModel.N_c|coalFlowSource.fuel_a.fuelModel.N_e|coalFlowSource.fuel_a.fuelModel.T_ref|coalFlowSource.fuel_a.fuelModel.ashIndex|coalFlowSource.fuel_a.fuelModel.defaultComposition.1.|coalFlowSource.fuel_a.fuelModel.defaultComposition.2.|coalFlowSource.fuel_a.fuelModel.defaultComposition.3.|coalFlowSource.fuel_a.fuelModel.defaultComposition.4.|coalFlowSource.fuel_a.fuelModel.defaultComposition.5.|coalFlowSource.fuel_a.fuelModel.defaultComposition.6.|coalFlowSource.fuel_a.fuelModel.waterIndex|coalFlowSource.fuel_a.m_flow|coalFlowSource.fuel_a.p|coalFlowSource.fuel_a.xi_outflow.1.|coalFlowSource.fuel_a.xi_outflow.2.|coalFlowSource.fuel_a.xi_outflow.3.|coalFlowSource.fuel_a.xi_outflow.4.|coalFlowSource.fuel_a.xi_outflow.5.|coalFlowSource.fuel_a.xi_outflow.6.|coalFlowSource.m_flow|coalFlowSource.m_flow_const|coalFlowSource.variable_T|coalFlowSource.variable_m_flow|coalFlowSource.variable_xi|coalFlowSource.xi_const.1.|coalFlowSource.xi_const.2.|coalFlowSource.xi_const.3.|coalFlowSource.xi_const.4.|coalFlowSource.xi_const.5.|coalFlowSource.xi_const.6.|coalGas_join_burner4.flueGas_inlet.T_outflow|coalGas_join_burner4.flueGas_inlet.m_flow|coalGas_join_burner4.flueGas_inlet.p|coalGas_join_burner4.flueGas_inlet.xi_outflow.1.|coalGas_join_burner4.flueGas_inlet.xi_outflow.2.|coalGas_join_burner4.flueGas_inlet.xi_outflow.3.|coalGas_join_burner4.flueGas_inlet.xi_outflow.4.|coalGas_join_burner4.flueGas_inlet.xi_outflow.5.|coalGas_join_burner4.flueGas_inlet.xi_outflow.6.|coalGas_join_burner4.flueGas_inlet.xi_outflow.7.|coalGas_join_burner4.flueGas_inlet.xi_outflow.8.|coalGas_join_burner4.flueGas_inlet.xi_outflow.9.|coalGas_join_burner4.fuelFlueGas_outlet.flueGas.T_outflow|coalGas_join_burner4.fuelFlueGas_outlet.flueGas.m_flow|coalGas_join_burner4.fuelFlueGas_outlet.flueGas.p|coalGas_join_burner4.fuelFlueGas_outlet.flueGas.xi_outflow.1.|coalGas_join_burner4.fuelFlueGas_outlet.flueGas.xi_outflow.2.|coalGas_join_burner4.fuelFlueGas_outlet.flueGas.xi_outflow.3.|coalGas_join_burner4.fuelFlueGas_outlet.flueGas.xi_outflow.4.|coalGas_join_burner4.fuelFlueGas_outlet.flueGas.xi_outflow.5.|coalGas_join_burner4.fuelFlueGas_outlet.flueGas.xi_outflow.6.|coalGas_join_burner4.fuelFlueGas_outlet.flueGas.xi_outflow.7.|coalGas_join_burner4.fuelFlueGas_outlet.flueGas.xi_outflow.8.|coalGas_join_burner4.fuelFlueGas_outlet.flueGas.xi_outflow.9.|coalGas_join_burner4.fuelFlueGas_outlet.fuel.T_outflow|coalGas_join_burner4.fuelFlueGas_outlet.fuel.fuelModel.C_LHV.1.|coalGas_join_burner4.fuelFlueGas_outlet.fuel.fuelModel.C_LHV.2.|coalGas_join_burner4.fuelFlueGas_outlet.fuel.fuelModel.C_LHV.3.|coalGas_join_burner4.fuelFlueGas_outlet.fuel.fuelModel.C_LHV.4.|coalGas_join_burner4.fuelFlueGas_outlet.fuel.fuelModel.C_LHV.5.|coalGas_join_burner4.fuelFlueGas_outlet.fuel.fuelModel.C_LHV.6.|coalGas_join_burner4.fuelFlueGas_outlet.fuel.fuelModel.C_LHV.7.|coalGas_join_burner4.fuelFlueGas_outlet.fuel.fuelModel.C_cp.1.|coalGas_join_burner4.fuelFlueGas_outlet.fuel.fuelModel.C_cp.2.|coalGas_join_burner4.fuelFlueGas_outlet.fuel.fuelModel.C_cp.3.|coalGas_join_burner4.fuelFlueGas_outlet.fuel.fuelModel.C_cp.4.|coalGas_join_burner4.fuelFlueGas_outlet.fuel.fuelModel.C_cp.5.|coalGas_join_burner4.fuelFlueGas_outlet.fuel.fuelModel.C_cp.6.|coalGas_join_burner4.fuelFlueGas_outlet.fuel.fuelModel.C_cp.7.|coalGas_join_burner4.fuelFlueGas_outlet.fuel.fuelModel.C_rho.1.|coalGas_join_burner4.fuelFlueGas_outlet.fuel.fuelModel.C_rho.2.|coalGas_join_burner4.fuelFlueGas_outlet.fuel.fuelModel.C_rho.3.|coalGas_join_burner4.fuelFlueGas_outlet.fuel.fuelModel.C_rho.4.|coalGas_join_burner4.fuelFlueGas_outlet.fuel.fuelModel.C_rho.5.|coalGas_join_burner4.fuelFlueGas_outlet.fuel.fuelModel.C_rho.6.|coalGas_join_burner4.fuelFlueGas_outlet.fuel.fuelModel.C_rho.7.|coalGas_join_burner4.fuelFlueGas_outlet.fuel.fuelModel.N_c|coalGas_join_burner4.fuelFlueGas_outlet.fuel.fuelModel.N_e|coalGas_join_burner4.fuelFlueGas_outlet.fuel.fuelModel.T_ref|coalGas_join_burner4.fuelFlueGas_outlet.fuel.fuelModel.ashIndex|coalGas_join_burner4.fuelFlueGas_outlet.fuel.fuelModel.defaultComposition.1.|coalGas_join_burner4.fuelFlueGas_outlet.fuel.fuelModel.defaultComposition.2.|coalGas_join_burner4.fuelFlueGas_outlet.fuel.fuelModel.defaultComposition.3.|coalGas_join_burner4.fuelFlueGas_outlet.fuel.fuelModel.defaultComposition.4.|coalGas_join_burner4.fuelFlueGas_outlet.fuel.fuelModel.defaultComposition.5.|coalGas_join_burner4.fuelFlueGas_outlet.fuel.fuelModel.defaultComposition.6.|coalGas_join_burner4.fuelFlueGas_outlet.fuel.fuelModel.waterIndex|coalGas_join_burner4.fuelFlueGas_outlet.fuel.m_flow|coalGas_join_burner4.fuelFlueGas_outlet.fuel.p|coalGas_join_burner4.fuelFlueGas_outlet.fuel.xi_outflow.1.|coalGas_join_burner4.fuelFlueGas_outlet.fuel.xi_outflow.2.|coalGas_join_burner4.fuelFlueGas_outlet.fuel.xi_outflow.3.|coalGas_join_burner4.fuelFlueGas_outlet.fuel.xi_outflow.4.|coalGas_join_burner4.fuelFlueGas_outlet.fuel.xi_outflow.5.|coalGas_join_burner4.fuelFlueGas_outlet.fuel.xi_outflow.6.|coalGas_join_burner4.fuelFlueGas_outlet.fuelModel.C_LHV.1.|coalGas_join_burner4.fuelFlueGas_outlet.fuelModel.C_LHV.2.|coalGas_join_burner4.fuelFlueGas_outlet.fuelModel.C_LHV.3.|coalGas_join_burner4.fuelFlueGas_outlet.fuelModel.C_LHV.4.|coalGas_join_burner4.fuelFlueGas_outlet.fuelModel.C_LHV.5.|coalGas_join_burner4.fuelFlueGas_outlet.fuelModel.C_LHV.6.|coalGas_join_burner4.fuelFlueGas_outlet.fuelModel.C_LHV.7.|coalGas_join_burner4.fuelFlueGas_outlet.fuelModel.C_cp.1.|coalGas_join_burner4.fuelFlueGas_outlet.fuelModel.C_cp.2.|coalGas_join_burner4.fuelFlueGas_outlet.fuelModel.C_cp.3.|coalGas_join_burner4.fuelFlueGas_outlet.fuelModel.C_cp.4.|coalGas_join_burner4.fuelFlueGas_outlet.fuelModel.C_cp.5.|coalGas_join_burner4.fuelFlueGas_outlet.fuelModel.C_cp.6.|coalGas_join_burner4.fuelFlueGas_outlet.fuelModel.C_cp.7.|coalGas_join_burner4.fuelFlueGas_outlet.fuelModel.C_rho.1.|coalGas_join_burner4.fuelFlueGas_outlet.fuelModel.C_rho.2.|coalGas_join_burner4.fuelFlueGas_outlet.fuelModel.C_rho.3.|coalGas_join_burner4.fuelFlueGas_outlet.fuelModel.C_rho.4.|coalGas_join_burner4.fuelFlueGas_outlet.fuelModel.C_rho.5.|coalGas_join_burner4.fuelFlueGas_outlet.fuelModel.C_rho.6.|coalGas_join_burner4.fuelFlueGas_outlet.fuelModel.C_rho.7.|coalGas_join_burner4.fuelFlueGas_outlet.fuelModel.N_c|coalGas_join_burner4.fuelFlueGas_outlet.fuelModel.N_e|coalGas_join_burner4.fuelFlueGas_outlet.fuelModel.T_ref|coalGas_join_burner4.fuelFlueGas_outlet.fuelModel.ashIndex|coalGas_join_burner4.fuelFlueGas_outlet.fuelModel.defaultComposition.1.|coalGas_join_burner4.fuelFlueGas_outlet.fuelModel.defaultComposition.2.|coalGas_join_burner4.fuelFlueGas_outlet.fuelModel.defaultComposition.3.|coalGas_join_burner4.fuelFlueGas_outlet.fuelModel.defaultComposition.4.|coalGas_join_burner4.fuelFlueGas_outlet.fuelModel.defaultComposition.5.|coalGas_join_burner4.fuelFlueGas_outlet.fuelModel.defaultComposition.6.|coalGas_join_burner4.fuelFlueGas_outlet.fuelModel.waterIndex|coalGas_join_burner4.fuelModel.C_LHV.1.|coalGas_join_burner4.fuelModel.C_LHV.2.|coalGas_join_burner4.fuelModel.C_LHV.3.|coalGas_join_burner4.fuelModel.C_LHV.4.|coalGas_join_burner4.fuelModel.C_LHV.5.|coalGas_join_burner4.fuelModel.C_LHV.6.|coalGas_join_burner4.fuelModel.C_LHV.7.|coalGas_join_burner4.fuelModel.C_cp.1.|coalGas_join_burner4.fuelModel.C_cp.2.|coalGas_join_burner4.fuelModel.C_cp.3.|coalGas_join_burner4.fuelModel.C_cp.4.|coalGas_join_burner4.fuelModel.C_cp.5.|coalGas_join_burner4.fuelModel.C_cp.6.|coalGas_join_burner4.fuelModel.C_cp.7.|coalGas_join_burner4.fuelModel.C_rho.1.|coalGas_join_burner4.fuelModel.C_rho.2.|coalGas_join_burner4.fuelModel.C_rho.3.|coalGas_join_burner4.fuelModel.C_rho.4.|coalGas_join_burner4.fuelModel.C_rho.5.|coalGas_join_burner4.fuelModel.C_rho.6.|coalGas_join_burner4.fuelModel.C_rho.7.|coalGas_join_burner4.fuelModel.N_c|coalGas_join_burner4.fuelModel.N_e|coalGas_join_burner4.fuelModel.T_ref|coalGas_join_burner4.fuelModel.ashIndex|coalGas_join_burner4.fuelModel.defaultComposition.1.|coalGas_join_burner4.fuelModel.defaultComposition.2.|coalGas_join_burner4.fuelModel.defaultComposition.3.|coalGas_join_burner4.fuelModel.defaultComposition.4.|coalGas_join_burner4.fuelModel.defaultComposition.5.|coalGas_join_burner4.fuelModel.defaultComposition.6.|coalGas_join_burner4.fuelModel.waterIndex|coalGas_join_burner4.fuel_inlet.T_outflow|coalGas_join_burner4.fuel_inlet.fuelModel.C_LHV.1.|coalGas_join_burner4.fuel_inlet.fuelModel.C_LHV.2.|coalGas_join_burner4.fuel_inlet.fuelModel.C_LHV.3.|coalGas_join_burner4.fuel_inlet.fuelModel.C_LHV.4.|coalGas_join_burner4.fuel_inlet.fuelModel.C_LHV.5.|coalGas_join_burner4.fuel_inlet.fuelModel.C_LHV.6.|coalGas_join_burner4.fuel_inlet.fuelModel.C_LHV.7.|coalGas_join_burner4.fuel_inlet.fuelModel.C_cp.1.|coalGas_join_burner4.fuel_inlet.fuelModel.C_cp.2.|coalGas_join_burner4.fuel_inlet.fuelModel.C_cp.3.|coalGas_join_burner4.fuel_inlet.fuelModel.C_cp.4.|coalGas_join_burner4.fuel_inlet.fuelModel.C_cp.5.|coalGas_join_burner4.fuel_inlet.fuelModel.C_cp.6.|coalGas_join_burner4.fuel_inlet.fuelModel.C_cp.7.|coalGas_join_burner4.fuel_inlet.fuelModel.C_rho.1.|coalGas_join_burner4.fuel_inlet.fuelModel.C_rho.2.|coalGas_join_burner4.fuel_inlet.fuelModel.C_rho.3.|coalGas_join_burner4.fuel_inlet.fuelModel.C_rho.4.|coalGas_join_burner4.fuel_inlet.fuelModel.C_rho.5.|coalGas_join_burner4.fuel_inlet.fuelModel.C_rho.6.|coalGas_join_burner4.fuel_inlet.fuelModel.C_rho.7.|coalGas_join_burner4.fuel_inlet.fuelModel.N_c|coalGas_join_burner4.fuel_inlet.fuelModel.N_e|coalGas_join_burner4.fuel_inlet.fuelModel.T_ref|coalGas_join_burner4.fuel_inlet.fuelModel.ashIndex|coalGas_join_burner4.fuel_inlet.fuelModel.defaultComposition.1.|coalGas_join_burner4.fuel_inlet.fuelModel.defaultComposition.2.|coalGas_join_burner4.fuel_inlet.fuelModel.defaultComposition.3.|coalGas_join_burner4.fuel_inlet.fuelModel.defaultComposition.4.|coalGas_join_burner4.fuel_inlet.fuelModel.defaultComposition.5.|coalGas_join_burner4.fuel_inlet.fuelModel.defaultComposition.6.|coalGas_join_burner4.fuel_inlet.fuelModel.waterIndex|coalGas_join_burner4.fuel_inlet.m_flow|coalGas_join_burner4.fuel_inlet.p|coalGas_join_burner4.fuel_inlet.xi_outflow.1.|coalGas_join_burner4.fuel_inlet.xi_outflow.2.|coalGas_join_burner4.fuel_inlet.xi_outflow.3.|coalGas_join_burner4.fuel_inlet.xi_outflow.4.|coalGas_join_burner4.fuel_inlet.xi_outflow.5.|coalGas_join_burner4.fuel_inlet.xi_outflow.6.|coalSink.T_const|coalSink.contributeToCycleSummary|coalSink.energyType|coalSink.p_const|coalSink.slagType.cp|coalSink.slag_inlet.T_outflow|coalSink.slag_inlet.m_flow|coalSink.slag_inlet.p|coalSink.slag_inlet.slagType.cp|coalSink.variable_T|coalSink.variable_p|combustionChamber.Q_flow_boiler|combustionChamber.T_flueGas_out|combustionChamber.T_slag_bottom|combustionChamber.contributeToCycleSummary|combustionChamber.flueGas_outlet.T_outflow|combustionChamber.flueGas_outlet.m_flow|combustionChamber.flueGas_outlet.p|combustionChamber.flueGas_outlet.xi_outflow.1.|combustionChamber.flueGas_outlet.xi_outflow.2.|combustionChamber.flueGas_outlet.xi_outflow.3.|combustionChamber.flueGas_outlet.xi_outflow.4.|combustionChamber.flueGas_outlet.xi_outflow.5.|combustionChamber.flueGas_outlet.xi_outflow.6.|combustionChamber.flueGas_outlet.xi_outflow.7.|combustionChamber.flueGas_outlet.xi_outflow.8.|combustionChamber.flueGas_outlet.xi_outflow.9.|combustionChamber.fuelModel.C_LHV.1.|combustionChamber.fuelModel.C_LHV.2.|combustionChamber.fuelModel.C_LHV.3.|combustionChamber.fuelModel.C_LHV.4.|combustionChamber.fuelModel.C_LHV.5.|combustionChamber.fuelModel.C_LHV.6.|combustionChamber.fuelModel.C_LHV.7.|combustionChamber.fuelModel.C_cp.1.|combustionChamber.fuelModel.C_cp.2.|combustionChamber.fuelModel.C_cp.3.|combustionChamber.fuelModel.C_cp.4.|combustionChamber.fuelModel.C_cp.5.|combustionChamber.fuelModel.C_cp.6.|combustionChamber.fuelModel.C_cp.7.|combustionChamber.fuelModel.C_rho.1.|combustionChamber.fuelModel.C_rho.2.|combustionChamber.fuelModel.C_rho.3.|combustionChamber.fuelModel.C_rho.4.|combustionChamber.fuelModel.C_rho.5.|combustionChamber.fuelModel.C_rho.6.|combustionChamber.fuelModel.C_rho.7.|combustionChamber.fuelModel.N_c|combustionChamber.fuelModel.N_e|combustionChamber.fuelModel.T_ref|combustionChamber.fuelModel.ashIndex|combustionChamber.fuelModel.defaultComposition.1.|combustionChamber.fuelModel.defaultComposition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Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/SMArtIInt 0.2.2-main/package.mo): time 0.007504/0.007504, allocations: 1.435 MB / 17.74 MB, free: 5.262 MB / 14.72 MB
Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.8.1-main/package.mo): time 0.1148/0.1148, allocations: 22.38 MB / 41.16 MB, free: 7.758 MB / 34.91 MB
Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/ModelicaServices 4.0.0+maint.om/package.mo): time 0.001147/0.001147, allocations: 104 kB / 48.65 MB, free: 244 kB / 34.91 MB
Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/Complex 4.0.0+maint.om/package.mo): time 0.001433/0.001433, allocations: 194.6 kB / 56.24 MB, free: 9.453 MB / 46.55 MB
Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/Modelica 4.0.0+maint.om/package.mo): time 1.358/1.358, allocations: 222.9 MB / 286.6 MB, free: 13.91 MB / 222.1 MB
Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/ClaRa 1.8.2-main/package.mo): time 0.9016/0.9016, allocations: 127.8 MB / 471.2 MB, free: 0.5625 MB / 366.1 MB
Notification: Performance of FrontEnd - loaded program: time 0.002207/0.002207, allocations: 119.8 kB / 0.6361 GB, free: 13.03 MB / 478.1 MB
Notification: Performance of FrontEnd - Absyn->SCode: time 0.4552/0.4574, allocations: 82.34 MB / 0.7165 GB, free: 9.73 MB / 0.5138 GB
Notification: Performance of NFInst.instantiate(ClaRa.Components.Mills.HardCoalMills.Check.combineMillandFurnace): time 0.01467/0.4721, allocations: 13.23 MB / 0.7294 GB, free: 15.26 MB / 0.5294 GB
Notification: Performance of NFInst.instExpressions: time 0.02056/0.4928, allocations: 12.37 MB / 0.7415 GB, free: 5.25 MB / 0.5294 GB
Notification: Performance of NFInst.updateImplicitVariability: time 0.003068/0.4959, allocations: 42.81 kB / 0.7416 GB, free: 5.242 MB / 0.5294 GB
Notification: Performance of NFTyping.typeComponents: time 0.004337/0.5003, allocations: 1.378 MB / 0.7429 GB, free: 4.332 MB / 0.5294 GB
Notification: Performance of NFTyping.typeBindings: time 0.005104/0.5054, allocations: 1.54 MB / 0.7444 GB, free: 3.125 MB / 0.5294 GB
Notification: Performance of NFTyping.typeClassSections: time 0.005588/0.511, allocations: 1.984 MB / 0.7463 GB, free: 1.25 MB / 0.5294 GB
Notification: Performance of NFFlatten.flatten: time 0.008046/0.5191, allocations: 4.817 MB / 0.7511 GB, free: 12.43 MB / 0.545 GB
Notification: Performance of NFFlatten.resolveConnections: time 0.007096/0.5262, allocations: 5.228 MB / 0.7562 GB, free: 7.102 MB / 0.545 GB
Notification: Performance of NFEvalConstants.evaluate: time 0.005664/0.5319, allocations: 2.926 MB / 0.759 GB, free: 4.168 MB / 0.545 GB
Notification: Performance of NFSimplifyModel.simplify: time 0.00595/0.5379, allocations: 3.851 MB / 0.7628 GB, free: 316 kB / 0.545 GB
Notification: Performance of NFPackage.collectConstants: time 0.002531/0.5404, allocations: 0.8829 MB / 0.7636 GB, free: 15.42 MB / 0.5607 GB
Notification: Performance of NFFlatten.collectFunctions: time 0.006663/0.5471, allocations: 3.046 MB / 0.7666 GB, free: 12.38 MB / 0.5607 GB
Notification: Performance of NFScalarize.scalarize: time 0.005408/0.5525, allocations: 4.119 MB / 0.7706 GB, free: 8.246 MB / 0.5607 GB
Notification: Performance of NFVerifyModel.verify: time 0.01078/0.5633, allocations: 4.604 MB / 0.7751 GB, free: 3.621 MB / 0.5607 GB
Notification: Performance of NFConvertDAE.convert: time 0.02397/0.5873, allocations: 14.7 MB / 0.7895 GB, free: 4.867 MB / 0.5763 GB
Notification: Performance of FrontEnd - DAE generated: time 7.444e-06/0.5874, allocations: 0 / 0.7895 GB, free: 4.867 MB / 0.5763 GB
Notification: Performance of FrontEnd: time 2.004e-06/0.5874, allocations: 0 / 0.7895 GB, free: 4.867 MB / 0.5763 GB
Notification: Performance of Transformations before backend: time 0.0004325/0.5878, allocations: 0 / 0.7895 GB, free: 4.867 MB / 0.5763 GB
Notification: Model statistics after passing the front-end and creating the data structures used by the back-end:
 * Number of equations: 821
 * Number of variables: 821
Notification: Performance of Generate backend data structure: time 0.02822/0.6161, allocations: 10.39 MB / 0.7996 GB, free: 10.36 MB / 0.5919 GB
Notification: Performance of prepare preOptimizeDAE: time 5.183e-05/0.6161, allocations: 12.03 kB / 0.7997 GB, free: 10.35 MB / 0.5919 GB
Notification: Performance of preOpt normalInlineFunction (simulation): time 0.004589/0.6207, allocations: 0.9483 MB / 0.8006 GB, free: 9.398 MB / 0.5919 GB
Notification: Performance of preOpt evaluateParameters (simulation): time 0.02011/0.6409, allocations: 9.429 MB / 0.8098 GB, free: 15.9 MB / 0.6075 GB
Notification: Performance of preOpt simplifyIfEquations (simulation): time 0.0002868/0.6412, allocations: 206.9 kB / 0.81 GB, free: 15.69 MB / 0.6075 GB
Notification: Performance of preOpt expandDerOperator (simulation): time 0.001349/0.6426, allocations: 232.4 kB / 0.8102 GB, free: 15.46 MB / 0.6075 GB
Notification: Performance of preOpt clockPartitioning (simulation): time 0.01704/0.6596, allocations: 11.13 MB / 0.8211 GB, free: 3.199 MB / 0.6075 GB
Notification: Performance of preOpt findStateOrder (simulation): time 0.000101/0.6598, allocations: 3.938 kB / 0.8211 GB, free: 3.195 MB / 0.6075 GB
Notification: Performance of preOpt replaceEdgeChange (simulation): time 0.0013/0.6611, allocations: 164 kB / 0.8212 GB, free: 3.035 MB / 0.6075 GB
Notification: Performance of preOpt inlineArrayEqn (simulation): time 0.0002166/0.6613, allocations: 184.7 kB / 0.8214 GB, free: 2.852 MB / 0.6075 GB
Notification: Performance of preOpt removeEqualRHS (simulation): time 0.01994/0.6813, allocations: 14.33 MB / 0.8354 GB, free: 4.496 MB / 0.6232 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 0.04524/0.7265, allocations: 25.1 MB / 0.8599 GB, free: 11.13 MB / 0.6544 GB
Notification: Performance of preOpt comSubExp (simulation): time 0.009093/0.7357, allocations: 6.819 MB / 0.8666 GB, free: 4.277 MB / 0.6544 GB
Notification: Performance of preOpt resolveLoops (simulation): time 0.006525/0.7422, allocations: 5.125 MB / 0.8716 GB, free: 15.14 MB / 0.67 GB
Notification: Performance of preOpt evalFunc (simulation): time 0.0007283/0.743, allocations: 157.8 kB / 0.8717 GB, free: 14.99 MB / 0.67 GB
Notification: Performance of preOpt encapsulateWhenConditions (simulation): time 9.813e-05/0.7431, allocations: 77.06 kB / 0.8718 GB, free: 14.91 MB / 0.67 GB
Notification: Performance of pre-optimization done (n=404): time 5.781e-06/0.7431, allocations: 0 / 0.8718 GB, free: 14.91 MB / 0.67 GB
Notification: Performance of matching and sorting (n=404): time 0.02748/0.7706, allocations: 16.32 MB / 0.8877 GB, free: 14.51 MB / 0.6857 GB
Notification: Performance of inlineWhenForInitialization (initialization): time 0.0009646/0.7716, allocations: 1.886 MB / 0.8896 GB, free: 12.17 MB / 0.6857 GB
Notification: Performance of selectInitializationVariablesDAE (initialization): time 0.02274/0.7944, allocations: 10.25 MB / 0.8996 GB, free: 1.934 MB / 0.6857 GB
Notification: Performance of collectPreVariables (initialization): time 0.001159/0.7956, allocations: 85.7 kB / 0.8997 GB, free: 1.844 MB / 0.6857 GB
Notification: Performance of collectInitialEqns (initialization): time 0.003922/0.7995, allocations: 2.631 MB / 0.9022 GB, free: 15.2 MB / 0.7013 GB
Notification: Performance of collectInitialBindings (initialization): time 0.002252/0.8018, allocations: 1.386 MB / 0.9036 GB, free: 13.8 MB / 0.7013 GB
Notification: Performance of simplifyInitialFunctions (initialization): time 0.004934/0.8068, allocations: 1.004 MB / 0.9046 GB, free: 12.79 MB / 0.7013 GB
Notification: Performance of setup shared object (initialization): time 0.0001117/0.8069, allocations: 301.1 kB / 0.9049 GB, free: 12.5 MB / 0.7013 GB
Notification: Performance of preBalanceInitialSystem (initialization): time 0.007889/0.8148, allocations: 5.792 MB / 0.9105 GB, free: 6.699 MB / 0.7013 GB
Notification: Performance of partitionIndependentBlocks (initialization): time 0.009549/0.8244, allocations: 7.136 MB / 0.9175 GB, free: 15.11 MB / 0.7169 GB
Notification: Performance of analyzeInitialSystem (initialization): time 0.1299/0.9544, allocations: 42.04 MB / 0.9585 GB, free: 4.758 MB / 0.7482 GB
Notification: Performance of solveInitialSystemEqSystem (initialization): time 3.149e-05/0.9544, allocations: 4 kB / 0.9586 GB, free: 4.754 MB / 0.7482 GB
Notification: Performance of matching and sorting (n=507) (initialization): time 0.4401/1.395, allocations: 13.75 MB / 0.972 GB, free: 217.5 MB / 0.7482 GB
Notification: Performance of prepare postOptimizeDAE: time 3.225e-05/1.395, allocations: 11.78 kB / 0.972 GB, free: 217.5 MB / 0.7482 GB
Notification: Performance of postOpt simplifyComplexFunction (initialization): time 0.0001083/1.395, allocations: 45.59 kB / 0.972 GB, free: 217.5 MB / 0.7482 GB
Notification: Performance of postOpt tearingSystem (initialization): time 0.002354/1.397, allocations: 1.381 MB / 0.9734 GB, free: 217.3 MB / 0.7482 GB
Notification: Performance of postOpt solveSimpleEquations (initialization): time 0.007427/1.404, allocations: 0.7682 MB / 0.9741 GB, free: 217.2 MB / 0.7482 GB
Notification: Performance of postOpt calculateStrongComponentJacobians (initialization): time 0.001436/1.406, allocations: 1.821 MB / 0.9759 GB, free: 215.9 MB / 0.7482 GB
Notification: Performance of postOpt simplifyAllExpressions (initialization): time 0.005244/1.411, allocations: 432.7 kB / 0.9763 GB, free: 215.9 MB / 0.7482 GB
Notification: Performance of postOpt collapseArrayExpressions (initialization): time 0.0007625/1.412, allocations: 189 kB / 0.9765 GB, free: 215.8 MB / 0.7482 GB
Warning: Assuming fixed start value for the following 4 variables:
         mills1.mass_rct:VARIABLE(min = 0.0 start = mills1.mass_rct_start unit = "kg" fixed = true nominal = 1.0 protected = true )  "Mass of raw coal on the table" type: Real
         mills1.mass_pct:VARIABLE(min = 0.0 start = mills1.mass_pct_start unit = "kg" fixed = true nominal = 1.0 protected = true )  "Mass of pulverized coal on the table" type: Real
         mills1.mass_pca:VARIABLE(min = 0.0 start = mills1.mass_pca_start unit = "kg" fixed = true nominal = 1.0 protected = true )  "Mass of pulverized coal carried by primary air" type: Real
         mills1.T_out:VARIABLE(min = 0.0 start = mills1.T_out_start unit = "K" fixed = true nominal = 300.0 protected = true )  "Classifier Temperature (outlet temperature)" type: Real
Notification: Model statistics after passing the back-end for initialization:
 * Number of independent subsystems: 76
 * 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 (332):
 * Single equations (assignments): 319
 * Array equations: 0
 * Algorithm blocks: 0
 * Record equations: 11
 * When equations: 0
 * If-equations: 0
 * Equation systems (not torn): 0
 * Torn equation systems: 2
 * 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): 2 systems
   {(2,20), (1,2)}
Notification: Performance of prepare postOptimizeDAE: time 0.003822/1.416, allocations: 2.19 MB / 0.9786 GB, free: 214.8 MB / 0.7482 GB
Notification: Performance of postOpt lateInlineFunction (simulation): time 0.001541/1.417, allocations: 0.7848 MB / 0.9794 GB, free: 214.8 MB / 0.7482 GB
Notification: Performance of postOpt wrapFunctionCalls (simulation): time 0.01365/1.431, allocations: 11.65 MB / 0.9908 GB, free: 209.9 MB / 0.7482 GB
Notification: Performance of postOpt simplifysemiLinear (simulation): time 2.572e-05/1.431, allocations: 19.2 kB / 0.9908 GB, free: 209.9 MB / 0.7482 GB
Notification: Performance of postOpt simplifyComplexFunction (simulation): time 6.517e-05/1.431, allocations: 31.3 kB / 0.9908 GB, free: 209.9 MB / 0.7482 GB
Notification: Performance of postOpt removeConstants (simulation): time 0.01561/1.447, allocations: 12.55 MB / 1.003 GB, free: 198.1 MB / 0.7482 GB
Notification: Performance of postOpt simplifyTimeIndepFuncCalls (simulation): time 0.00182/1.449, allocations: 59.98 kB / 1.003 GB, free: 198 MB / 0.7482 GB
Notification: Performance of postOpt simplifyAllExpressions (simulation): time 0.003275/1.452, allocations: 104.1 kB / 1.003 GB, free: 197.9 MB / 0.7482 GB
Notification: Performance of postOpt findZeroCrossings (simulation): time 0.0006686/1.453, allocations: 241.6 kB / 1.003 GB, free: 197.7 MB / 0.7482 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): (mills1.gasIn.d, mills1.gasIn.kappa, mills1.gasIn.drhodp_hxi, mills1.gasIn.drhodh_pxi, mills1.gasIn.drhodxi_ph, mills1.gasIn.p_i, mills1.gasIn.xi_gas) = TILMedia.Internals.GasObjectFunctions.additionalProperties_pTxi(mills1.coalIn.p, fluelGasFlowSource1.T_const, {fluelGasFlowSource1.xi_const[1], fluelGasFlowSource1.xi_const[2], fluelGasFlowSource1.xi_const[3], fluelGasFlowSource1.xi_const[4], fluelGasFlowSource1.xi_const[5], fluelGasFlowSource1.xi_const[6], fluelGasFlowSource1.xi_const[7], fluelGasFlowSource1.xi_const[8], fluelGasFlowSource1.xi_const[9]}, mills1.gasIn.gasPointer)

Variables:
1: mills1.gasIn.p_i[6]:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 )  "Partial pressure" type: Real [10]
2: mills1.gasIn.drhodxi_ph[6]:VARIABLE(unit = "kg/(m3)" )  "Derivative of density wrt mass fraction of water at constant pressure and specific enthalpy" type: Real [9]
3: mills1.gasIn.drhodxi_ph[7]:VARIABLE(unit = "kg/(m3)" )  "Derivative of density wrt mass fraction of water at constant pressure and specific enthalpy" type: Real [9]
4: mills1.gasIn.drhodxi_ph[2]:VARIABLE(unit = "kg/(m3)" )  "Derivative of density wrt mass fraction of water at constant pressure and specific enthalpy" type: Real [9]
5: mills1.gasIn.p_i[9]:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 )  "Partial pressure" type: Real [10]
6: mills1.gasIn.p_i[7]:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 )  "Partial pressure" type: Real [10]
7: mills1.gasIn.drhodxi_ph[9]:VARIABLE(unit = "kg/(m3)" )  "Derivative of density wrt mass fraction of water at constant pressure and specific enthalpy" type: Real [9]
8: mills1.gasIn.p_i[5]:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 )  "Partial pressure" type: Real [10]
9: mills1.gasIn.drhodxi_ph[4]:VARIABLE(unit = "kg/(m3)" )  "Derivative of density wrt mass fraction of water at constant pressure and specific enthalpy" type: Real [9]
10: mills1.gasIn.drhodp_hxi:VARIABLE(unit = "s2/m2" )  "Derivative of density wrt pressure at specific enthalpy and mass fraction" type: Real
11: mills1.gasIn.p_i[2]:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 )  "Partial pressure" type: Real [10]
12: mills1.gasIn.drhodh_pxi:VARIABLE(unit = "kg.s2/m5" )  "Derivative of density wrt specific enthalpy at constant pressure and mass fraction" type: Real
13: mills1.gasIn.p_i[4]:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 )  "Partial pressure" type: Real [10]
14: mills1.gasIn.drhodxi_ph[5]:VARIABLE(unit = "kg/(m3)" )  "Derivative of density wrt mass fraction of water at constant pressure and specific enthalpy" type: Real [9]
15: mills1.gasIn.p_i[10]:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 )  "Partial pressure" type: Real [10]
16: mills1.coalIn.p:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 )  "Pressure" type: Real
17: mills1.gasIn.drhodxi_ph[1]:VARIABLE(unit = "kg/(m3)" )  "Derivative of density wrt mass fraction of water at constant pressure and specific enthalpy" type: Real [9]
18: mills1.gasIn.kappa:VARIABLE(unit = "1/Pa" )  "Isothermal compressibility" type: Real
19: mills1.gasIn.p_i[1]:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 )  "Partial pressure" type: Real [10]
20: mills1.gasIn.p_i[3]:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 )  "Partial pressure" type: Real [10]
21: mills1.gasIn.drhodxi_ph[3]:VARIABLE(unit = "kg/(m3)" )  "Derivative of density wrt mass fraction of water at constant pressure and specific enthalpy" type: Real [9]
22: mills1.gasIn.xi_gas:VARIABLE(min = 0.0 max = 1.0 unit = "1" )  "Mass fraction of gasoues condensing component" type: Real
23: mills1.gasIn.drhodxi_ph[8]:VARIABLE(unit = "kg/(m3)" )  "Derivative of density wrt mass fraction of water at constant pressure and specific enthalpy" type: Real [9]
24: mills1.gasIn.p_i[8]: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): mills1.Delta_p_pa = mills1.millKoeff.K_12 * abs(mills1.m_flow_air_in) * mills1.m_flow_air_in / $cse1
2/2 (1): $cse1 = max(mills1.gasIn.d, 1e-4)
3/3 (24): (mills1.gasIn.d, mills1.gasIn.kappa, mills1.gasIn.drhodp_hxi, mills1.gasIn.drhodh_pxi, mills1.gasIn.drhodxi_ph, mills1.gasIn.p_i, mills1.gasIn.xi_gas) = TILMedia.Internals.GasObjectFunctions.additionalProperties_pTxi(mills1.coalIn.p, fluelGasFlowSource1.T_const, {fluelGasFlowSource1.xi_const[1], fluelGasFlowSource1.xi_const[2], fluelGasFlowSource1.xi_const[3], fluelGasFlowSource1.xi_const[4], fluelGasFlowSource1.xi_const[5], fluelGasFlowSource1.xi_const[6], fluelGasFlowSource1.xi_const[7], fluelGasFlowSource1.xi_const[8], fluelGasFlowSource1.xi_const[9]}, mills1.gasIn.gasPointer)
4/27 (1): mills1.coalIn.p = flueGasPressureSink.p_const + mills1.Delta_p_pa

Variables:
1: mills1.Delta_p_pa:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 protected = true )  "Primary air difference pressure" type: Real
2: mills1.gasIn.p_i[6]:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 )  "Partial pressure" type: Real [10]
3: mills1.gasIn.drhodxi_ph[6]:VARIABLE(unit = "kg/(m3)" )  "Derivative of density wrt mass fraction of water at constant pressure and specific enthalpy" type: Real [9]
4: mills1.gasIn.drhodxi_ph[7]:VARIABLE(unit = "kg/(m3)" )  "Derivative of density wrt mass fraction of water at constant pressure and specific enthalpy" type: Real [9]
5: mills1.gasIn.drhodxi_ph[2]:VARIABLE(unit = "kg/(m3)" )  "Derivative of density wrt mass fraction of water at constant pressure and specific enthalpy" type: Real [9]
6: mills1.gasIn.p_i[9]:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 )  "Partial pressure" type: Real [10]
7: mills1.gasIn.p_i[7]:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 )  "Partial pressure" type: Real [10]
8: mills1.gasIn.drhodxi_ph[9]:VARIABLE(unit = "kg/(m3)" )  "Derivative of density wrt mass fraction of water at constant pressure and specific enthalpy" type: Real [9]
9: mills1.gasIn.p_i[5]:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 )  "Partial pressure" type: Real [10]
10: mills1.gasIn.drhodxi_ph[4]:VARIABLE(unit = "kg/(m3)" )  "Derivative of density wrt mass fraction of water at constant pressure and specific enthalpy" type: Real [9]
11: mills1.gasIn.drhodp_hxi:VARIABLE(unit = "s2/m2" )  "Derivative of density wrt pressure at specific enthalpy and mass fraction" type: Real
12: mills1.gasIn.p_i[2]:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 )  "Partial pressure" type: Real [10]
13: mills1.gasIn.drhodh_pxi:VARIABLE(unit = "kg.s2/m5" )  "Derivative of density wrt specific enthalpy at constant pressure and mass fraction" type: Real
14: mills1.gasIn.p_i[4]:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 )  "Partial pressure" type: Real [10]
15: mills1.gasIn.drhodxi_ph[5]:VARIABLE(unit = "kg/(m3)" )  "Derivative of density wrt mass fraction of water at constant pressure and specific enthalpy" type: Real [9]
16: mills1.gasIn.p_i[10]:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 )  "Partial pressure" type: Real [10]
17: mills1.coalIn.p:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 )  "Pressure" type: Real
18: mills1.gasIn.drhodxi_ph[1]:VARIABLE(unit = "kg/(m3)" )  "Derivative of density wrt mass fraction of water at constant pressure and specific enthalpy" type: Real [9]
19: mills1.gasIn.kappa:VARIABLE(unit = "1/Pa" )  "Isothermal compressibility" type: Real
20: mills1.gasIn.p_i[1]:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 )  "Partial pressure" type: Real [10]
21: mills1.gasIn.p_i[3]:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 )  "Partial pressure" type: Real [10]
22: mills1.gasIn.drhodxi_ph[3]:VARIABLE(unit = "kg/(m3)" )  "Derivative of density wrt mass fraction of water at constant pressure and specific enthalpy" type: Real [9]
23: mills1.gasIn.xi_gas:VARIABLE(min = 0.0 max = 1.0 unit = "1" )  "Mass fraction of gasoues condensing component" type: Real
24: mills1.gasIn.drhodxi_ph[8]:VARIABLE(unit = "kg/(m3)" )  "Derivative of density wrt mass fraction of water at constant pressure and specific enthalpy" type: Real [9]
25: mills1.gasIn.p_i[8]:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 )  "Partial pressure" type: Real [10]
26: mills1.gasIn.d:VARIABLE(min = 0.0 unit = "kg/m3" )  "Density" type: Real
27: $cse1:VARIABLE(protected = true )  type: Real unreplaceable
[/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 0.001087/1.454, allocations: 0.8831 MB / 1.004 GB, free: 196.8 MB / 0.7482 GB
Error: post-optimization module createDAEmodeBDAE (simulation) failed.
Error: Internal error SimCode DAEmode: The model ClaRa.Components.Mills.HardCoalMills.Check.combineMillandFurnace could not be translated