Running: ./testmodel.py --libraries=/home/hudson/saved_omc/libraries/.openmodelica/libraries --ompython_omhome=/usr ClaRa_dev_ClaRa.Components.Mills.HardCoalMills.Check.SimpleMillTester.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.SimpleMillTester,tolerance=1e-06,outputFormat="mat",numberOfIntervals=5000,variableFilter="CPUtime|EventCounter|NonlinearSystems.initialization.1..Calls|NonlinearSystems.initialization.1..Iterations|NonlinearSystems.initialization.1..Jacobians|NonlinearSystems.initialization.1..Residues|NonlinearSystems.initialization.2..Calls|NonlinearSystems.initialization.2..Iterations|NonlinearSystems.initialization.2..Jacobians|NonlinearSystems.initialization.2..Residues|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|boundaryGas_pTxi.T_const|boundaryGas_pTxi.contributeToCycleSummary|boundaryGas_pTxi.energyType|boundaryGas_pTxi.eyeOut.T|boundaryGas_pTxi.eyeOut.h|boundaryGas_pTxi.eyeOut.m_flow|boundaryGas_pTxi.eyeOut.p|boundaryGas_pTxi.eyeOut.s|boundaryGas_pTxi.eyeOut.xi.1.|boundaryGas_pTxi.eyeOut.xi.2.|boundaryGas_pTxi.eyeOut.xi.3.|boundaryGas_pTxi.eyeOut.xi.4.|boundaryGas_pTxi.eyeOut.xi.5.|boundaryGas_pTxi.eyeOut.xi.6.|boundaryGas_pTxi.eyeOut.xi.7.|boundaryGas_pTxi.eyeOut.xi.8.|boundaryGas_pTxi.eyeOut.xi.9.|boundaryGas_pTxi.eye_int.1..T|boundaryGas_pTxi.eye_int.1..h|boundaryGas_pTxi.eye_int.1..m_flow|boundaryGas_pTxi.eye_int.1..p|boundaryGas_pTxi.eye_int.1..s|boundaryGas_pTxi.eye_int.1..xi.1.|boundaryGas_pTxi.eye_int.1..xi.2.|boundaryGas_pTxi.eye_int.1..xi.3.|boundaryGas_pTxi.eye_int.1..xi.4.|boundaryGas_pTxi.eye_int.1..xi.5.|boundaryGas_pTxi.eye_int.1..xi.6.|boundaryGas_pTxi.eye_int.1..xi.7.|boundaryGas_pTxi.eye_int.1..xi.8.|boundaryGas_pTxi.eye_int.1..xi.9.|boundaryGas_pTxi.gas_a.T_outflow|boundaryGas_pTxi.gas_a.m_flow|boundaryGas_pTxi.gas_a.p|boundaryGas_pTxi.gas_a.xi_outflow.1.|boundaryGas_pTxi.gas_a.xi_outflow.2.|boundaryGas_pTxi.gas_a.xi_outflow.3.|boundaryGas_pTxi.gas_a.xi_outflow.4.|boundaryGas_pTxi.gas_a.xi_outflow.5.|boundaryGas_pTxi.gas_a.xi_outflow.6.|boundaryGas_pTxi.gas_a.xi_outflow.7.|boundaryGas_pTxi.gas_a.xi_outflow.8.|boundaryGas_pTxi.gas_a.xi_outflow.9.|boundaryGas_pTxi.p_const|boundaryGas_pTxi.variable_T|boundaryGas_pTxi.variable_p|boundaryGas_pTxi.variable_xi|boundaryGas_pTxi.xi_const.1.|boundaryGas_pTxi.xi_const.2.|boundaryGas_pTxi.xi_const.3.|boundaryGas_pTxi.xi_const.4.|boundaryGas_pTxi.xi_const.5.|boundaryGas_pTxi.xi_const.6.|boundaryGas_pTxi.xi_const.7.|boundaryGas_pTxi.xi_const.8.|boundaryGas_pTxi.xi_const.9.|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_cp.1.|coalFlowSource.fuelModel.C_cp.2.|coalFlowSource.fuelModel.C_cp.3.|coalFlowSource.fuelModel.C_rho.1.|coalFlowSource.fuelModel.C_rho.2.|coalFlowSource.fuelModel.C_rho.3.|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.waterIndex|coalFlowSource.fuelModel.xi_e_waf.1,1.|coalFlowSource.fuelModel.xi_e_waf.1,2.|coalFlowSource.fuelModel.xi_e_waf.1,3.|coalFlowSource.fuelModel.xi_e_waf.1,4.|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_cp.1.|coalFlowSource.fuel_a.fuelModel.C_cp.2.|coalFlowSource.fuel_a.fuelModel.C_cp.3.|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.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.waterIndex|coalFlowSource.fuel_a.fuelModel.xi_e_waf.1,1.|coalFlowSource.fuel_a.fuelModel.xi_e_waf.1,2.|coalFlowSource.fuel_a.fuelModel.xi_e_waf.1,3.|coalFlowSource.fuel_a.fuelModel.xi_e_waf.1,4.|coalFlowSource.fuel_a.m_flow|coalFlowSource.fuel_a.p|coalFlowSource.fuel_a.xi_outflow.1.|coalFlowSource.fuel_a.xi_outflow.2.|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.|fluelGasFlowSource1.T_const|fluelGasFlowSource1.contributeToCycleSummary|fluelGasFlowSource1.energyType|fluelGasFlowSource1.eyeOut.T|fluelGasFlowSource1.eyeOut.h|fluelGasFlowSource1.eyeOut.m_flow|fluelGasFlowSource1.eyeOut.p|fluelGasFlowSource1.eyeOut.s|fluelGasFlowSource1.eyeOut.xi.1.|fluelGasFlowSource1.eyeOut.xi.2.|fluelGasFlowSource1.eyeOut.xi.3.|fluelGasFlowSource1.eyeOut.xi.4.|fluelGasFlowSource1.eyeOut.xi.5.|fluelGasFlowSource1.eyeOut.xi.6.|fluelGasFlowSource1.eyeOut.xi.7.|fluelGasFlowSource1.eyeOut.xi.8.|fluelGasFlowSource1.eyeOut.xi.9.|fluelGasFlowSource1.eye_int.1..T|fluelGasFlowSource1.eye_int.1..h|fluelGasFlowSource1.eye_int.1..m_flow|fluelGasFlowSource1.eye_int.1..p|fluelGasFlowSource1.eye_int.1..s|fluelGasFlowSource1.eye_int.1..xi.1.|fluelGasFlowSource1.eye_int.1..xi.2.|fluelGasFlowSource1.eye_int.1..xi.3.|fluelGasFlowSource1.eye_int.1..xi.4.|fluelGasFlowSource1.eye_int.1..xi.5.|fluelGasFlowSource1.eye_int.1..xi.6.|fluelGasFlowSource1.eye_int.1..xi.7.|fluelGasFlowSource1.eye_int.1..xi.8.|fluelGasFlowSource1.eye_int.1..xi.9.|fluelGasFlowSource1.gas_a.T_outflow|fluelGasFlowSource1.gas_a.m_flow|fluelGasFlowSource1.gas_a.p|fluelGasFlowSource1.gas_a.xi_outflow.1.|fluelGasFlowSource1.gas_a.xi_outflow.2.|fluelGasFlowSource1.gas_a.xi_outflow.3.|fluelGasFlowSource1.gas_a.xi_outflow.4.|fluelGasFlowSource1.gas_a.xi_outflow.5.|fluelGasFlowSource1.gas_a.xi_outflow.6.|fluelGasFlowSource1.gas_a.xi_outflow.7.|fluelGasFlowSource1.gas_a.xi_outflow.8.|fluelGasFlowSource1.gas_a.xi_outflow.9.|fluelGasFlowSource1.m_flow|fluelGasFlowSource1.m_flow_const|fluelGasFlowSource1.variable_T|fluelGasFlowSource1.variable_m_flow|fluelGasFlowSource1.variable_xi|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.|fuelBoundary_pTxi.T_const|fuelBoundary_pTxi.contributeToCycleSummary|fuelBoundary_pTxi.energyType|fuelBoundary_pTxi.fuelModel.C_LHV.1.|fuelBoundary_pTxi.fuelModel.C_LHV.2.|fuelBoundary_pTxi.fuelModel.C_LHV.3.|fuelBoundary_pTxi.fuelModel.C_cp.1.|fuelBoundary_pTxi.fuelModel.C_cp.2.|fuelBoundary_pTxi.fuelModel.C_cp.3.|fuelBoundary_pTxi.fuelModel.C_rho.1.|fuelBoundary_pTxi.fuelModel.C_rho.2.|fuelBoundary_pTxi.fuelModel.C_rho.3.|fuelBoundary_pTxi.fuelModel.N_c|fuelBoundary_pTxi.fuelModel.N_e|fuelBoundary_pTxi.fuelModel.T_ref|fuelBoundary_pTxi.fuelModel.ashIndex|fuelBoundary_pTxi.fuelModel.defaultComposition.1.|fuelBoundary_pTxi.fuelModel.defaultComposition.2.|fuelBoundary_pTxi.fuelModel.waterIndex|fuelBoundary_pTxi.fuelModel.xi_e_waf.1,1.|fuelBoundary_pTxi.fuelModel.xi_e_waf.1,2.|fuelBoundary_pTxi.fuelModel.xi_e_waf.1,3.|fuelBoundary_pTxi.fuelModel.xi_e_waf.1,4.|fuelBoundary_pTxi.fuel_a.T_outflow|fuelBoundary_pTxi.fuel_a.fuelModel.C_LHV.1.|fuelBoundary_pTxi.fuel_a.fuelModel.C_LHV.2.|fuelBoundary_pTxi.fuel_a.fuelModel.C_LHV.3.|fuelBoundary_pTxi.fuel_a.fuelModel.C_cp.1.|fuelBoundary_pTxi.fuel_a.fuelModel.C_cp.2.|fuelBoundary_pTxi.fuel_a.fuelModel.C_cp.3.|fuelBoundary_pTxi.fuel_a.fuelModel.C_rho.1.|fuelBoundary_pTxi.fuel_a.fuelModel.C_rho.2.|fuelBoundary_pTxi.fuel_a.fuelModel.C_rho.3.|fuelBoundary_pTxi.fuel_a.fuelModel.N_c|fuelBoundary_pTxi.fuel_a.fuelModel.N_e|fuelBoundary_pTxi.fuel_a.fuelModel.T_ref|fuelBoundary_pTxi.fuel_a.fuelModel.ashIndex|fuelBoundary_pTxi.fuel_a.fuelModel.defaultComposition.1.|fuelBoundary_pTxi.fuel_a.fuelModel.defaultComposition.2.|fuelBoundary_pTxi.fuel_a.fuelModel.waterIndex|fuelBoundary_pTxi.fuel_a.fuelModel.xi_e_waf.1,1.|fuelBoundary_pTxi.fuel_a.fuelModel.xi_e_waf.1,2.|fuelBoundary_pTxi.fuel_a.fuelModel.xi_e_waf.1,3.|fuelBoundary_pTxi.fuel_a.fuelModel.xi_e_waf.1,4.|fuelBoundary_pTxi.fuel_a.m_flow|fuelBoundary_pTxi.fuel_a.p|fuelBoundary_pTxi.fuel_a.xi_outflow.1.|fuelBoundary_pTxi.fuel_a.xi_outflow.2.|fuelBoundary_pTxi.p_const|fuelBoundary_pTxi.variable_T|fuelBoundary_pTxi.variable_p|fuelBoundary_pTxi.variable_xi|fuelBoundary_pTxi.xi_const.1.|fuelBoundary_pTxi.xi_const.2.|gain2.k|gain2.u|gain2.y|join.flueGas_inlet.T_outflow|join.flueGas_inlet.m_flow|join.flueGas_inlet.p|join.flueGas_inlet.xi_outflow.1.|join.flueGas_inlet.xi_outflow.2.|join.flueGas_inlet.xi_outflow.3.|join.flueGas_inlet.xi_outflow.4.|join.flueGas_inlet.xi_outflow.5.|join.flueGas_inlet.xi_outflow.6.|join.flueGas_inlet.xi_outflow.7.|join.flueGas_inlet.xi_outflow.8.|join.flueGas_inlet.xi_outflow.9.|join.fuelFlueGas_outlet.flueGas.T_outflow|join.fuelFlueGas_outlet.flueGas.m_flow|join.fuelFlueGas_outlet.flueGas.p|join.fuelFlueGas_outlet.flueGas.xi_outflow.1.|join.fuelFlueGas_outlet.flueGas.xi_outflow.2.|join.fuelFlueGas_outlet.flueGas.xi_outflow.3.|join.fuelFlueGas_outlet.flueGas.xi_outflow.4.|join.fuelFlueGas_outlet.flueGas.xi_outflow.5.|join.fuelFlueGas_outlet.flueGas.xi_outflow.6.|join.fuelFlueGas_outlet.flueGas.xi_outflow.7.|join.fuelFlueGas_outlet.flueGas.xi_outflow.8.|join.fuelFlueGas_outlet.flueGas.xi_outflow.9.|join.fuelFlueGas_outlet.fuel.T_outflow|join.fuelFlueGas_outlet.fuel.fuelModel.C_LHV.1.|join.fuelFlueGas_outlet.fuel.fuelModel.C_LHV.2.|join.fuelFlueGas_outlet.fuel.fuelModel.C_LHV.3.|join.fuelFlueGas_outlet.fuel.fuelModel.C_cp.1.|join.fuelFlueGas_outlet.fuel.fuelModel.C_cp.2.|join.fuelFlueGas_outlet.fuel.fuel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w.2.|verticalMill_L3_1.inlet.flueGas.xi_outflow.3.|verticalMill_L3_1.inlet.flueGas.xi_outflow.4.|verticalMill_L3_1.inlet.flueGas.xi_outflow.5.|verticalMill_L3_1.inlet.flueGas.xi_outflow.6.|verticalMill_L3_1.inlet.flueGas.xi_outflow.7.|verticalMill_L3_1.inlet.flueGas.xi_outflow.8.|verticalMill_L3_1.inlet.flueGas.xi_outflow.9.|verticalMill_L3_1.inlet.fuel.T_outflow|verticalMill_L3_1.inlet.fuel.fuelModel.C_LHV.1.|verticalMill_L3_1.inlet.fuel.fuelModel.C_LHV.2.|verticalMill_L3_1.inlet.fuel.fuelModel.C_LHV.3.|verticalMill_L3_1.inlet.fuel.fuelModel.C_cp.1.|verticalMill_L3_1.inlet.fuel.fuelModel.C_cp.2.|verticalMill_L3_1.inlet.fuel.fuelModel.C_cp.3.|verticalMill_L3_1.inlet.fuel.fuelModel.C_rho.1.|verticalMill_L3_1.inlet.fuel.fuelModel.C_rho.2.|verticalMill_L3_1.inlet.fuel.fuelModel.C_rho.3.|verticalMill_L3_1.inlet.fuel.fuelModel.N_c|verticalMill_L3_1.inlet.fuel.fuelModel.N_e|verticalMill_L3_1.inlet.fuel.fuelModel.T_ref|verticalMill_L3_1.inlet.fuel.fuelModel.ashIndex|verticalMill_L3_1.inlet.fuel.fuelModel.defaultComposition.1.|verticalMill_L3_1.inlet.fuel.fuelModel.defaultComposition.2.|verticalMill_L3_1.inlet.fuel.fuelModel.waterIndex|verticalMill_L3_1.inlet.fuel.fuelModel.xi_e_waf.1,1.|verticalMill_L3_1.inlet.fuel.fuelModel.xi_e_waf.1,2.|verticalMill_L3_1.inlet.fuel.fuelModel.xi_e_waf.1,3.|verticalMill_L3_1.inlet.fuel.fuelModel.xi_e_waf.1,4.|verticalMill_L3_1.inlet.fuel.m_flow|verticalMill_L3_1.inlet.fuel.p|verticalMill_L3_1.inlet.fuel.xi_outflow.1.|verticalMill_L3_1.inlet.fuel.xi_outflow.2.|verticalMill_L3_1.inlet.fuelModel.C_LHV.1.|verticalMill_L3_1.inlet.fuelModel.C_LHV.2.|verticalMill_L3_1.inlet.fuelModel.C_LHV.3.|verticalMill_L3_1.inlet.fuelModel.C_cp.1.|verticalMill_L3_1.inlet.fuelModel.C_cp.2.|verticalMill_L3_1.inlet.fuelModel.C_cp.3.|verticalMill_L3_1.inlet.fuelModel.C_rho.1.|verticalMill_L3_1.inlet.fuelModel.C_rho.2.|verticalMill_L3_1.inlet.fuelModel.C_rho.3.|verticalMill_L3_1.inlet.fuelModel.N_c|verticalMill_L3_1.inlet.fuelModel.N_e|verticalMill_L3_1.inlet.fuelModel.T_ref|verticalMill_L3_1.inlet.fuelModel.ashIndex|verticalMill_L3_1.inlet.fuelModel.defaultComposition.1.|verticalMill_L3_1.inlet.fuelModel.defaultComposition.2.|verticalMill_L3_1.inlet.fuelModel.waterIndex|verticalMill_L3_1.inlet.fuelModel.xi_e_waf.1,1.|verticalMill_L3_1.inlet.fuelModel.xi_e_waf.1,2.|verticalMill_L3_1.inlet.fuelModel.xi_e_waf.1,3.|verticalMill_L3_1.inlet.fuelModel.xi_e_waf.1,4.|verticalMill_L3_1.m_flow_air_out_start|verticalMill_L3_1.mass_pca_start|verticalMill_L3_1.mass_pct_start|verticalMill_L3_1.mass_rct_start|verticalMill_L3_1.millKoeff.E_e|verticalMill_L3_1.millKoeff.K_1|verticalMill_L3_1.millKoeff.K_10|verticalMill_L3_1.millKoeff.K_11|verticalMill_L3_1.millKoeff.K_12|verticalMill_L3_1.millKoeff.K_2|verticalMill_L3_1.millKoeff.K_3|verticalMill_L3_1.millKoeff.K_4|verticalMill_L3_1.millKoeff.K_5|verticalMill_L3_1.millKoeff.K_6|verticalMill_L3_1.millKoeff.K_7|verticalMill_L3_1.millKoeff.K_8|verticalMill_L3_1.millKoeff.K_9|verticalMill_L3_1.millKoeff.P_nom|verticalMill_L3_1.outlet.flueGas.T_outflow|verticalMill_L3_1.outlet.flueGas.m_flow|verticalMill_L3_1.outlet.flueGas.p|verticalMill_L3_1.outlet.flueGas.xi_outflow.1.|verticalMill_L3_1.outlet.flueGas.xi_outflow.2.|verticalMill_L3_1.outlet.flueGas.xi_outflow.3.|verticalMill_L3_1.outlet.flueGas.xi_outflow.4.|verticalMill_L3_1.outlet.flueGas.xi_outflow.5.|verticalMill_L3_1.outlet.flueGas.xi_outflow.6.|verticalMill_L3_1.outlet.flueGas.xi_outflow.7.|verticalMill_L3_1.outlet.flueGas.xi_outflow.8.|verticalMill_L3_1.outlet.flueGas.xi_outflow.9.|verticalMill_L3_1.outlet.fuel.T_outflow|verticalMill_L3_1.outlet.fuel.fuelModel.C_LHV.1.|verticalMill_L3_1.outlet.fuel.fuelModel.C_LHV.2.|verticalMill_L3_1.outlet.fuel.fuelModel.C_LHV.3.|verticalMill_L3_1.outlet.fuel.fuelModel.C_cp.1.|verticalMill_L3_1.outlet.fuel.fuelModel.C_cp.2.|verticalMill_L3_1.outlet.fuel.fuelModel.C_cp.3.|verticalMill_L3_1.outlet.fuel.fuelModel.C_rho.1.|verticalMill_L3_1.outlet.fuel.fuelModel.C_rho.2.|verticalMill_L3_1.outlet.fuel.fuelModel.C_rho.3.|verticalMill_L3_1.outlet.fuel.fuelModel.N_c|verticalMill_L3_1.outlet.fuel.fuelModel.N_e|verticalMill_L3_1.outlet.fuel.fuelModel.T_ref|verticalMill_L3_1.outlet.fuel.fuelModel.ashIndex|verticalMill_L3_1.outlet.fuel.fuelModel.defaultComposition.1.|verticalMill_L3_1.outlet.fuel.fuelModel.defaultComposition.2.|verticalMill_L3_1.outlet.fuel.fuelModel.waterIndex|verticalMill_L3_1.outlet.fuel.fuelModel.xi_e_waf.1,1.|verticalMill_L3_1.outlet.fuel.fuelModel.xi_e_waf.1,2.|verticalMill_L3_1.outlet.fuel.fuelModel.xi_e_waf.1,3.|verticalMill_L3_1.outlet.fuel.fuelModel.xi_e_waf.1,4.|verticalMill_L3_1.outlet.fuel.m_flow|verticalMill_L3_1.outlet.fuel.p|verticalMill_L3_1.outlet.fuel.xi_outflow.1.|verticalMill_L3_1.outlet.fuel.xi_outflow.2.|verticalMill_L3_1.outlet.fuelModel.C_LHV.1.|verticalMill_L3_1.outlet.fuelModel.C_LHV.2.|verticalMill_L3_1.outlet.fuelModel.C_LHV.3.|verticalMill_L3_1.outlet.fuelModel.C_cp.1.|verticalMill_L3_1.outlet.fuelModel.C_cp.2.|verticalMill_L3_1.outlet.fuelModel.C_cp.3.|verticalMill_L3_1.outlet.fuelModel.C_rho.1.|verticalMill_L3_1.outlet.fuelModel.C_rho.2.|verticalMill_L3_1.outlet.fuelModel.C_rho.3.|verticalMill_L3_1.outlet.fuelModel.N_c|verticalMill_L3_1.outlet.fuelModel.N_e|verticalMill_L3_1.outlet.fuelModel.T_ref|verticalMill_L3_1.outlet.fuelModel.ashIndex|verticalMill_L3_1.outlet.fuelModel.defaultComposition.1.|verticalMill_L3_1.outlet.fuelModel.defaultComposition.2.|verticalMill_L3_1.outlet.fuelModel.waterIndex|verticalMill_L3_1.outlet.fuelModel.xi_e_waf.1,1.|verticalMill_L3_1.outlet.fuelModel.xi_e_waf.1,2.|verticalMill_L3_1.outlet.fuelModel.xi_e_waf.1,3.|verticalMill_L3_1.outlet.fuelModel.xi_e_waf.1,4.|verticalMill_L3_1.summary.LHV_in|verticalMill_L3_1.summary.LHV_out|verticalMill_L3_1.summary.P_grind|verticalMill_L3_1.summary.T_air_in|verticalMill_L3_1.summary.T_coal_in|verticalMill_L3_1.summary.T_out|verticalMill_L3_1.summary.m_flow_air_in|verticalMill_L3_1.summary.m_flow_air_out|verticalMill_L3_1.summary.m_flow_coal_in|verticalMill_L3_1.summary.m_flow_coal_out|verticalMill_L3_1.summary.m_flow_tot_in|verticalMill_L3_1.summary.m_flow_tot_out|verticalMill_L3_1.summary.mass_coal|verticalMill_L3_1.summary.rpm_classifier|verticalMill_L3_1.summary.xi_air_h2o_in|verticalMill_L3_1.summary.xi_air_h2o_out|verticalMill_L3_1.summary.xi_air_h2o_sat|verticalMill_L3_1.summary.xi_coal_h2o_in|verticalMill_L3_1.summary.xi_coal_h2o_out|verticalMill_L3_1.xi_coal_h2o_res|verticalMill_L3_1.xi_wc_start.1.|verticalMill_L3_1.xi_wc_start.2.",fileNamePrefix="ClaRa_dev_ClaRa.Components.Mills.HardCoalMills.Check.SimpleMillTester") Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/SMArtIInt 0.2.2-main/package.mo): time 0.01334/0.01334, allocations: 1.438 MB / 17.75 MB, free: 5.352 MB / 14.72 MB Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.8.1-main/package.mo): time 0.1144/0.1144, 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 0.001099/0.001099, allocations: 108 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 0.001674/0.001674, allocations: 194.4 kB / 56.26 MB, free: 9.473 MB / 46.55 MB Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/Modelica 4.0.0+maint.om/package.mo): time 1.427/1.427, allocations: 222.9 MB / 286.6 MB, free: 14 MB / 222.1 MB Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/ClaRa 1.8.2-main/package.mo): time 0.9229/0.9229, allocations: 127.8 MB / 471.3 MB, free: 0.6016 MB / 366.1 MB Notification: Performance of FrontEnd - loaded program: time 0.002569/0.002569, allocations: 123.8 kB / 0.6361 GB, free: 13.11 MB / 478.1 MB Notification: Performance of FrontEnd - Absyn->SCode: time 0.4478/0.4504, allocations: 82.34 MB / 0.7165 GB, free: 9.594 MB / 0.5138 GB Notification: Performance of NFInst.instantiate(ClaRa.Components.Mills.HardCoalMills.Check.SimpleMillTester): time 0.01286/0.4633, allocations: 12.04 MB / 0.7282 GB, free: 92 kB / 0.5138 GB Notification: Performance of NFInst.instExpressions: time 0.01814/0.4814, allocations: 11.6 MB / 0.7396 GB, free: 6.723 MB / 0.5294 GB Notification: Performance of NFInst.updateImplicitVariability: time 0.002384/0.4839, allocations: 37 kB / 0.7396 GB, free: 6.719 MB / 0.5294 GB Notification: Performance of NFTyping.typeComponents: time 0.003889/0.4878, allocations: 1.266 MB / 0.7408 GB, free: 5.887 MB / 0.5294 GB Notification: Performance of NFTyping.typeBindings: time 0.003889/0.4917, allocations: 1.386 MB / 0.7422 GB, free: 4.805 MB / 0.5294 GB Notification: Performance of NFTyping.typeClassSections: time 0.004861/0.4965, allocations: 1.685 MB / 0.7438 GB, free: 3.535 MB / 0.5294 GB Notification: Performance of NFFlatten.flatten: time 0.006179/0.5027, allocations: 3.953 MB / 0.7477 GB, free: 16 kB / 0.5294 GB Notification: Performance of NFFlatten.resolveConnections: time 0.00505/0.5078, allocations: 4.128 MB / 0.7517 GB, free: 11.82 MB / 0.545 GB Notification: Performance of NFEvalConstants.evaluate: time 0.004538/0.5124, allocations: 2.513 MB / 0.7542 GB, free: 9.301 MB / 0.545 GB Notification: Performance of NFSimplifyModel.simplify: time 0.004733/0.5172, allocations: 2.98 MB / 0.7571 GB, free: 6.312 MB / 0.545 GB Notification: Performance of NFPackage.collectConstants: time 0.001769/0.519, allocations: 0.6445 MB / 0.7577 GB, free: 5.668 MB / 0.545 GB Notification: Performance of NFFlatten.collectFunctions: time 0.005706/0.5247, allocations: 2.804 MB / 0.7605 GB, free: 2.859 MB / 0.545 GB Notification: Performance of NFScalarize.scalarize: time 0.003679/0.5284, allocations: 3.305 MB / 0.7637 GB, free: 15.55 MB / 0.5607 GB Notification: Performance of NFVerifyModel.verify: time 0.005914/0.5343, allocations: 3.6 MB / 0.7672 GB, free: 11.93 MB / 0.5607 GB Notification: Performance of NFConvertDAE.convert: time 0.01582/0.5501, allocations: 11.86 MB / 0.7788 GB, free: 28 kB / 0.5607 GB Notification: Performance of FrontEnd - DAE generated: time 5.901e-06/0.5502, allocations: 0 / 0.7788 GB, free: 28 kB / 0.5607 GB Notification: Performance of FrontEnd: time 1.873e-06/0.5502, allocations: 0 / 0.7788 GB, free: 28 kB / 0.5607 GB Notification: Performance of Transformations before backend: time 0.0002359/0.5504, allocations: 0 / 0.7788 GB, free: 28 kB / 0.5607 GB Notification: Model statistics after passing the front-end and creating the data structures used by the back-end: * Number of equations: 552 * Number of variables: 552 Notification: Performance of Generate backend data structure: time 0.0184/0.5689, allocations: 8.147 MB / 0.7867 GB, free: 7.777 MB / 0.5763 GB Notification: Performance of prepare preOptimizeDAE: time 4.53e-05/0.5689, allocations: 8.031 kB / 0.7867 GB, free: 7.77 MB / 0.5763 GB Notification: Performance of preOpt normalInlineFunction (simulation): time 0.003056/0.572, allocations: 0.7931 MB / 0.7875 GB, free: 6.973 MB / 0.5763 GB Notification: Performance of preOpt evaluateParameters (simulation): time 0.01635/0.5883, allocations: 8.315 MB / 0.7956 GB, free: 14.58 MB / 0.5919 GB Notification: Performance of preOpt simplifyIfEquations (simulation): time 0.0002243/0.5886, allocations: 161.7 kB / 0.7958 GB, free: 14.41 MB / 0.5919 GB Notification: Performance of preOpt expandDerOperator (simulation): time 0.0008932/0.5895, allocations: 172.3 kB / 0.796 GB, free: 14.25 MB / 0.5919 GB Notification: Performance of preOpt clockPartitioning (simulation): time 0.01099/0.6005, allocations: 7.537 MB / 0.8033 GB, free: 5.684 MB / 0.5919 GB Notification: Performance of preOpt findStateOrder (simulation): time 5.506e-05/0.6006, allocations: 4 kB / 0.8033 GB, free: 5.68 MB / 0.5919 GB Notification: Performance of preOpt replaceEdgeChange (simulation): time 0.0007248/0.6014, allocations: 128 kB / 0.8034 GB, free: 5.555 MB / 0.5919 GB Notification: Performance of preOpt inlineArrayEqn (simulation): time 0.000137/0.6015, allocations: 119.5 kB / 0.8036 GB, free: 5.438 MB / 0.5919 GB Notification: Performance of preOpt removeEqualRHS (simulation): time 0.01136/0.6129, allocations: 8.513 MB / 0.8119 GB, free: 12.91 MB / 0.6075 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 0.02845/0.6414, allocations: 15.27 MB / 0.8268 GB, free: 13.5 MB / 0.6232 GB Notification: Performance of preOpt comSubExp (simulation): time 0.004868/0.6463, allocations: 3.603 MB / 0.8303 GB, free: 9.871 MB / 0.6232 GB Notification: Performance of preOpt resolveLoops (simulation): time 0.002723/0.649, allocations: 2.193 MB / 0.8324 GB, free: 7.672 MB / 0.6232 GB Notification: Performance of preOpt evalFunc (simulation): time 0.0003576/0.6494, allocations: 113.1 kB / 0.8326 GB, free: 7.562 MB / 0.6232 GB Notification: Performance of preOpt encapsulateWhenConditions (simulation): time 6.938e-05/0.6495, allocations: 76.31 kB / 0.8326 GB, free: 7.477 MB / 0.6232 GB Notification: Performance of pre-optimization done (n=222): time 4.638e-06/0.6495, allocations: 4 kB / 0.8326 GB, free: 7.473 MB / 0.6232 GB Notification: Performance of matching and sorting (n=222): time 0.01389/0.6634, allocations: 7.892 MB / 0.8403 GB, free: 15.53 MB / 0.6388 GB Notification: Performance of inlineWhenForInitialization (initialization): time 0.0005995/0.664, allocations: 1.626 MB / 0.8419 GB, free: 13.52 MB / 0.6388 GB Notification: Performance of selectInitializationVariablesDAE (initialization): time 0.0151/0.6791, allocations: 9.215 MB / 0.8509 GB, free: 4.324 MB / 0.6388 GB Notification: Performance of collectPreVariables (initialization): time 0.0005242/0.6797, allocations: 61.7 kB / 0.851 GB, free: 4.258 MB / 0.6388 GB Notification: Performance of collectInitialEqns (initialization): time 0.002789/0.6825, allocations: 2.272 MB / 0.8532 GB, free: 1.977 MB / 0.6388 GB Notification: Performance of collectInitialBindings (initialization): time 0.001012/0.6835, allocations: 0.7823 MB / 0.854 GB, free: 1.188 MB / 0.6388 GB Notification: Performance of simplifyInitialFunctions (initialization): time 0.002396/0.6859, allocations: 0.7466 MB / 0.8547 GB, free: 444 kB / 0.6388 GB Notification: Performance of setup shared object (initialization): time 8.745e-05/0.6861, allocations: 309 kB / 0.855 GB, free: 132 kB / 0.6388 GB Notification: Performance of preBalanceInitialSystem (initialization): time 0.004082/0.6901, allocations: 3.292 MB / 0.8582 GB, free: 12.83 MB / 0.6544 GB Notification: Performance of partitionIndependentBlocks (initialization): time 0.005204/0.6954, allocations: 4.427 MB / 0.8625 GB, free: 8.008 MB / 0.6544 GB Notification: Performance of analyzeInitialSystem (initialization): time 0.007597/0.703, allocations: 6.107 MB / 0.8685 GB, free: 1.672 MB / 0.6544 GB Notification: Performance of solveInitialSystemEqSystem (initialization): time 2.203e-05/0.703, allocations: 8 kB / 0.8685 GB, free: 1.664 MB / 0.6544 GB Notification: Performance of matching and sorting (n=337) (initialization): time 0.01265/0.7157, allocations: 8.314 MB / 0.8766 GB, free: 9.289 MB / 0.67 GB Notification: Performance of prepare postOptimizeDAE: time 3.508e-05/0.7157, allocations: 12 kB / 0.8766 GB, free: 9.277 MB / 0.67 GB Notification: Performance of postOpt simplifyComplexFunction (initialization): time 6.822e-05/0.7158, allocations: 24.53 kB / 0.8767 GB, free: 9.254 MB / 0.67 GB Notification: Performance of postOpt tearingSystem (initialization): time 0.004451/0.7203, allocations: 1.825 MB / 0.8784 GB, free: 7.418 MB / 0.67 GB Notification: Performance of postOpt solveSimpleEquations (initialization): time 0.003591/0.7239, allocations: 487.2 kB / 0.8789 GB, free: 6.941 MB / 0.67 GB Notification: Performance of postOpt calculateStrongComponentJacobians (initialization): time 0.004294/0.7282, allocations: 3.988 MB / 0.8828 GB, free: 2.758 MB / 0.67 GB Notification: Performance of postOpt simplifyAllExpressions (initialization): time 0.004823/0.7331, allocations: 318.3 kB / 0.8831 GB, free: 2.445 MB / 0.67 GB Notification: Performance of postOpt collapseArrayExpressions (initialization): time 0.0008596/0.7339, allocations: 131.9 kB / 0.8832 GB, free: 2.316 MB / 0.67 GB Notification: Model statistics after passing the back-end for initialization: * Number of independent subsystems: 66 * 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 (228): * Single equations (assignments): 221 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 4 * When equations: 0 * If-equations: 0 * Equation systems (not torn): 0 * Torn equation systems: 3 * Mixed (continuous/discrete) equation systems: 0 Notification: Torn system details for strict tearing set: * Linear torn systems (#iteration vars, #inner vars, density): 1 system {(1,4,100.0%)} * Non-linear torn systems (#iteration vars, #inner vars): 2 systems {(3,25), (1,2)} Notification: Performance of prepare postOptimizeDAE: time 0.003979/0.7379, allocations: 1.763 MB / 0.8849 GB, free: 0.543 MB / 0.67 GB Notification: Performance of postOpt lateInlineFunction (simulation): time 0.001948/0.7399, allocations: 0.6249 MB / 0.8856 GB, free: 15.91 MB / 0.6857 GB Notification: Performance of postOpt wrapFunctionCalls (simulation): time 0.01052/0.7504, allocations: 5.6 MB / 0.891 GB, free: 10.29 MB / 0.6857 GB Notification: Performance of postOpt simplifysemiLinear (simulation): time 2.666e-05/0.7505, allocations: 7.969 kB / 0.891 GB, free: 10.28 MB / 0.6857 GB Notification: Performance of postOpt simplifyComplexFunction (simulation): time 4.295e-05/0.7505, allocations: 11.98 kB / 0.891 GB, free: 10.27 MB / 0.6857 GB Notification: Performance of postOpt removeConstants (simulation): time 0.01245/0.763, allocations: 6.471 MB / 0.8974 GB, free: 3.762 MB / 0.6857 GB Notification: Performance of postOpt simplifyTimeIndepFuncCalls (simulation): time 0.001692/0.7647, allocations: 40 kB / 0.8974 GB, free: 3.723 MB / 0.6857 GB Notification: Performance of postOpt simplifyAllExpressions (simulation): time 0.003076/0.7678, allocations: 76.48 kB / 0.8975 GB, free: 3.648 MB / 0.6857 GB Notification: Performance of postOpt findZeroCrossings (simulation): time 0.0005157/0.7683, allocations: 141.1 kB / 0.8976 GB, free: 3.512 MB / 0.6857 GB [/var/lib/jenkins1/ws/OpenModelicaLibraryTestingWork/OpenModelica/OMCompiler/Compiler/BackEnd/DAEMode.mo:528:7-530:90:writable] Error: Internal error DAEMode.traverserStrongComponents failed on equation: 1/1 (24): (verticalMill_L3_1.gasIn.d, verticalMill_L3_1.gasIn.kappa, verticalMill_L3_1.gasIn.drhodp_hxi, verticalMill_L3_1.gasIn.drhodh_pxi, verticalMill_L3_1.gasIn.drhodxi_ph, verticalMill_L3_1.gasIn.p_i, verticalMill_L3_1.gasIn.xi_gas) = TILMedia.Internals.GasObjectFunctions.additionalProperties_pTxi(verticalMill_L3_1.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]}, verticalMill_L3_1.gasIn.gasPointer) Variables: 1: verticalMill_L3_1.coalIn.p:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 ) "Pressure" type: Real 2: verticalMill_L3_1.gasIn.p_i[8]:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 ) "Partial pressure" type: Real [10] 3: verticalMill_L3_1.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] 4: verticalMill_L3_1.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] 5: verticalMill_L3_1.gasIn.p_i[4]:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 ) "Partial pressure" type: Real [10] 6: verticalMill_L3_1.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] 7: verticalMill_L3_1.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] 8: verticalMill_L3_1.gasIn.p_i[10]:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 ) "Partial pressure" type: Real [10] 9: verticalMill_L3_1.gasIn.drhodp_hxi:VARIABLE(unit = "s2/m2" ) "Derivative of density wrt pressure at specific enthalpy and mass fraction" type: Real 10: verticalMill_L3_1.gasIn.p_i[6]:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 ) "Partial pressure" type: Real [10] 11: verticalMill_L3_1.gasIn.drhodh_pxi:VARIABLE(unit = "kg.s2/m5" ) "Derivative of density wrt specific enthalpy at constant pressure and mass fraction" type: Real 12: verticalMill_L3_1.gasIn.p_i[1]:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 ) "Partial pressure" type: Real [10] 13: verticalMill_L3_1.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] 14: verticalMill_L3_1.gasIn.kappa:VARIABLE(unit = "1/Pa" ) "Isothermal compressibility" type: Real 15: verticalMill_L3_1.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] 16: verticalMill_L3_1.gasIn.p_i[2]:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 ) "Partial pressure" type: Real [10] 17: verticalMill_L3_1.gasIn.p_i[9]:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 ) "Partial pressure" type: Real [10] 18: verticalMill_L3_1.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] 19: verticalMill_L3_1.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] 20: verticalMill_L3_1.gasIn.p_i[5]:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 ) "Partial pressure" type: Real [10] 21: verticalMill_L3_1.gasIn.p_i[3]:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 ) "Partial pressure" type: Real [10] 22: verticalMill_L3_1.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] 23: verticalMill_L3_1.gasIn.xi_gas:VARIABLE(min = 0.0 max = 1.0 unit = "1" ) "Mass fraction of gasoues condensing component" type: Real 24: verticalMill_L3_1.gasIn.p_i[7]: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): verticalMill_L3_1.Delta_p_pa = verticalMill_L3_1.millKoeff.K_12 * abs(verticalMill_L3_1.m_flow_air_in) * verticalMill_L3_1.m_flow_air_in / $cse2 2/2 (1): $cse2 = max(verticalMill_L3_1.gasIn.d, 1e-4) 3/3 (24): (verticalMill_L3_1.gasIn.d, verticalMill_L3_1.gasIn.kappa, verticalMill_L3_1.gasIn.drhodp_hxi, verticalMill_L3_1.gasIn.drhodh_pxi, verticalMill_L3_1.gasIn.drhodxi_ph, verticalMill_L3_1.gasIn.p_i, verticalMill_L3_1.gasIn.xi_gas) = TILMedia.Internals.GasObjectFunctions.additionalProperties_pTxi(verticalMill_L3_1.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]}, verticalMill_L3_1.gasIn.gasPointer) 4/27 (1): verticalMill_L3_1.coalIn.p = boundaryGas_pTxi.p_const + verticalMill_L3_1.Delta_p_pa Variables: 1: verticalMill_L3_1.Delta_p_pa:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 protected = true ) "Primary air difference pressure" type: Real 2: verticalMill_L3_1.coalIn.p:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 ) "Pressure" type: Real 3: verticalMill_L3_1.gasIn.p_i[8]:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 ) "Partial pressure" type: Real [10] 4: verticalMill_L3_1.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] 5: verticalMill_L3_1.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] 6: verticalMill_L3_1.gasIn.p_i[4]:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 ) "Partial pressure" type: Real [10] 7: verticalMill_L3_1.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] 8: verticalMill_L3_1.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] 9: verticalMill_L3_1.gasIn.p_i[10]:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 ) "Partial pressure" type: Real [10] 10: verticalMill_L3_1.gasIn.drhodp_hxi:VARIABLE(unit = "s2/m2" ) "Derivative of density wrt pressure at specific enthalpy and mass fraction" type: Real 11: verticalMill_L3_1.gasIn.p_i[6]:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 ) "Partial pressure" type: Real [10] 12: verticalMill_L3_1.gasIn.drhodh_pxi:VARIABLE(unit = "kg.s2/m5" ) "Derivative of density wrt specific enthalpy at constant pressure and mass fraction" type: Real 13: verticalMill_L3_1.gasIn.p_i[1]:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 ) "Partial pressure" type: Real [10] 14: verticalMill_L3_1.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: verticalMill_L3_1.gasIn.kappa:VARIABLE(unit = "1/Pa" ) "Isothermal compressibility" type: Real 16: verticalMill_L3_1.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] 17: verticalMill_L3_1.gasIn.p_i[2]:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 ) "Partial pressure" type: Real [10] 18: verticalMill_L3_1.gasIn.p_i[9]:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 ) "Partial pressure" type: Real [10] 19: verticalMill_L3_1.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] 20: verticalMill_L3_1.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] 21: verticalMill_L3_1.gasIn.p_i[5]:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 ) "Partial pressure" type: Real [10] 22: verticalMill_L3_1.gasIn.p_i[3]:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 ) "Partial pressure" type: Real [10] 23: verticalMill_L3_1.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] 24: verticalMill_L3_1.gasIn.xi_gas:VARIABLE(min = 0.0 max = 1.0 unit = "1" ) "Mass fraction of gasoues condensing component" type: Real 25: verticalMill_L3_1.gasIn.p_i[7]:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 ) "Partial pressure" type: Real [10] 26: verticalMill_L3_1.gasIn.d:VARIABLE(min = 0.0 start = 1.0 unit = "kg/m3" ) "Density" type: Real 27: $cse2: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 postOpt createDAEmodeBDAE (simulation): time 0.001467/0.7698, allocations: 0.8938 MB / 0.8985 GB, free: 2.531 MB / 0.6857 GB Error: post-optimization module createDAEmodeBDAE (simulation) failed. Error: Internal error SimCode DAEmode: The model ClaRa.Components.Mills.HardCoalMills.Check.SimpleMillTester could not be translated