Running: ./testmodel.py --libraries=/home/hudson/saved_omc/libraries/.openmodelica/libraries --ompython_omhome=/usr ClaRa_dev_ClaRa.Components.VolumesValvesFittings.Valves.Check.TestThreeWayGasValve.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.VolumesValvesFittings.Valves.Check.TestThreeWayGasValve,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|Time|_derdummy|_dummy|massFlowSource_h1.T_const|massFlowSource_h1.contributeToCycleSummary|massFlowSource_h1.energyType|massFlowSource_h1.eyeOut.T|massFlowSource_h1.eyeOut.h|massFlowSource_h1.eyeOut.m_flow|massFlowSource_h1.eyeOut.p|massFlowSource_h1.eyeOut.s|massFlowSource_h1.eyeOut.xi.1.|massFlowSource_h1.eyeOut.xi.2.|massFlowSource_h1.eyeOut.xi.3.|massFlowSource_h1.eyeOut.xi.4.|massFlowSource_h1.eyeOut.xi.5.|massFlowSource_h1.eyeOut.xi.6.|massFlowSource_h1.eyeOut.xi.7.|massFlowSource_h1.eyeOut.xi.8.|massFlowSource_h1.eyeOut.xi.9.|massFlowSource_h1.eye_int.1..T|massFlowSource_h1.eye_int.1..h|massFlowSource_h1.eye_int.1..m_flow|massFlowSource_h1.eye_int.1..p|massFlowSource_h1.eye_int.1..s|massFlowSource_h1.eye_int.1..xi.1.|massFlowSource_h1.eye_int.1..xi.2.|massFlowSource_h1.eye_int.1..xi.3.|massFlowSource_h1.eye_int.1..xi.4.|massFlowSource_h1.eye_int.1..xi.5.|massFlowSource_h1.eye_int.1..xi.6.|massFlowSource_h1.eye_int.1..xi.7.|massFlowSource_h1.eye_int.1..xi.8.|massFlowSource_h1.eye_int.1..xi.9.|massFlowSource_h1.gas_a.T_outflow|massFlowSource_h1.gas_a.m_flow|massFlowSource_h1.gas_a.p|massFlowSource_h1.gas_a.xi_outflow.1.|massFlowSource_h1.gas_a.xi_outflow.2.|massFlowSource_h1.gas_a.xi_outflow.3.|massFlowSource_h1.gas_a.xi_outflow.4.|massFlowSource_h1.gas_a.xi_outflow.5.|massFlowSource_h1.gas_a.xi_outflow.6.|massFlowSource_h1.gas_a.xi_outflow.7.|massFlowSource_h1.gas_a.xi_outflow.8.|massFlowSource_h1.gas_a.xi_outflow.9.|massFlowSource_h1.p_const|massFlowSource_h1.variable_T|massFlowSource_h1.variable_p|massFlowSource_h1.variable_xi|massFlowSource_h1.xi_const.1.|massFlowSource_h1.xi_const.2.|massFlowSource_h1.xi_const.3.|massFlowSource_h1.xi_const.4.|massFlowSource_h1.xi_const.5.|massFlowSource_h1.xi_const.6.|massFlowSource_h1.xi_const.7.|massFlowSource_h1.xi_const.8.|massFlowSource_h1.xi_const.9.|pressureSink_ph2.T_const|pressureSink_ph2.contributeToCycleSummary|pressureSink_ph2.energyType|pressureSink_ph2.eyeOut.T|pressureSink_ph2.eyeOut.h|pressureSink_ph2.eyeOut.m_flow|pressureSink_ph2.eyeOut.p|pressureSink_ph2.eyeOut.s|pressureSink_ph2.eyeOut.xi.1.|pressureSink_ph2.eyeOut.xi.2.|pressureSink_ph2.eyeOut.xi.3.|pressureSink_ph2.eyeOut.xi.4.|pressureSink_ph2.eyeOut.xi.5.|pressureSink_ph2.eyeOut.xi.6.|pressureSink_ph2.eyeOut.xi.7.|pressureSink_ph2.eyeOut.xi.8.|pressureSink_ph2.eyeOut.xi.9.|pressureSink_ph2.eye_int.1..T|pressureSink_ph2.eye_int.1..h|pressureSink_ph2.eye_int.1..m_flow|pressureSink_ph2.eye_int.1..p|pressureSink_ph2.eye_int.1..s|pressureSink_ph2.eye_int.1..xi.1.|pressureSink_ph2.eye_int.1..xi.2.|pressureSink_ph2.eye_int.1..xi.3.|pressureSink_ph2.eye_int.1..xi.4.|pressureSink_ph2.eye_int.1..xi.5.|pressureSink_ph2.eye_int.1..xi.6.|pressureSink_ph2.eye_int.1..xi.7.|pressureSink_ph2.eye_int.1..xi.8.|pressureSink_ph2.eye_int.1..xi.9.|pressureSink_ph2.gas_a.T_outflow|pressureSink_ph2.gas_a.m_flow|pressureSink_ph2.gas_a.p|pressureSink_ph2.gas_a.xi_outflow.1.|pressureSink_ph2.gas_a.xi_outflow.2.|pressureSink_ph2.gas_a.xi_outflow.3.|pressureSink_ph2.gas_a.xi_outflow.4.|pressureSink_ph2.gas_a.xi_outflow.5.|pressureSink_ph2.gas_a.xi_outflow.6.|pressureSink_ph2.gas_a.xi_outflow.7.|pressureSink_ph2.gas_a.xi_outflow.8.|pressureSink_ph2.gas_a.xi_outflow.9.|pressureSink_ph2.p_const|pressureSink_ph2.variable_T|pressureSink_ph2.variable_p|pressureSink_ph2.variable_xi|pressureSink_ph2.xi_const.1.|pressureSink_ph2.xi_const.2.|pressureSink_ph2.xi_const.3.|pressureSink_ph2.xi_const.4.|pressureSink_ph2.xi_const.5.|pressureSink_ph2.xi_const.6.|pressureSink_ph2.xi_const.7.|pressureSink_ph2.xi_const.8.|pressureSink_ph2.xi_const.9.|pressureSink_ph3.T_const|pressureSink_ph3.contributeToCycleSummary|pressureSink_ph3.energyType|pressureSink_ph3.eyeOut.T|pressureSink_ph3.eyeOut.h|pressureSink_ph3.eyeOut.m_flow|pressureSink_ph3.eyeOut.p|pressureSink_ph3.eyeOut.s|pressureSink_ph3.eyeOut.xi.1.|pressureSink_ph3.eyeOut.xi.2.|pressureSink_ph3.eyeOut.xi.3.|pressureSink_ph3.eyeOut.xi.4.|pressureSink_ph3.eyeOut.xi.5.|pressureSink_ph3.eyeOut.xi.6.|pressureSink_ph3.eyeOut.xi.7.|pressureSink_ph3.eyeOut.xi.8.|pressureSink_ph3.eyeOut.xi.9.|pressureSink_ph3.eye_int.1..T|pressureSink_ph3.eye_int.1..h|pressureSink_ph3.eye_int.1..m_flow|pressureSink_ph3.eye_int.1..p|pressureSink_ph3.eye_int.1..s|pressureSink_ph3.eye_int.1..xi.1.|pressureSink_ph3.eye_int.1..xi.2.|pressureSink_ph3.eye_int.1..xi.3.|pressureSink_ph3.eye_int.1..xi.4.|pressureSink_ph3.eye_int.1..xi.5.|pressureSink_ph3.eye_int.1..xi.6.|pressureSink_ph3.eye_int.1..xi.7.|pressureSink_ph3.eye_int.1..xi.8.|pressureSink_ph3.eye_int.1..xi.9.|pressureSink_ph3.gas_a.T_outflow|pressureSink_ph3.gas_a.m_flow|pressureSink_ph3.gas_a.p|pressureSink_ph3.gas_a.xi_outflow.1.|pressureSink_ph3.gas_a.xi_outflow.2.|pressureSink_ph3.gas_a.xi_outflow.3.|pressureSink_ph3.gas_a.xi_outflow.4.|pressureSink_ph3.gas_a.xi_outflow.5.|pressureSink_ph3.gas_a.xi_outflow.6.|pressureSink_ph3.gas_a.xi_outflow.7.|pressureSink_ph3.gas_a.xi_outflow.8.|pressureSink_ph3.gas_a.xi_outflow.9.|pressureSink_ph3.p_const|pressureSink_ph3.variable_T|pressureSink_ph3.variable_p|pressureSink_ph3.variable_xi|pressureSink_ph3.xi_const.1.|pressureSink_ph3.xi_const.2.|pressureSink_ph3.xi_const.3.|pressureSink_ph3.xi_const.4.|pressureSink_ph3.xi_const.5.|pressureSink_ph3.xi_const.6.|pressureSink_ph3.xi_const.7.|pressureSink_ph3.xi_const.8.|pressureSink_ph3.xi_const.9.|ramp.duration|ramp.height|ramp.offset|ramp.startTime|ramp.y|simCenter.MaxSimTime|simCenter.T_amb|simCenter.T_amb_start|simCenter.contributeToCycleSummary|simCenter.cycleSumPort.power_aux|simCenter.cycleSumPort.power_in|simCenter.cycleSumPort.power_out_elMech|simCenter.cycleSumPort.power_out_th|simCenter.fuelModel1.C_LHV.1.|simCenter.fuelModel1.C_LHV.2.|simCenter.fuelModel1.C_LHV.3.|simCenter.fuelModel1.C_cp.1.|simCenter.fuelModel1.C_cp.2.|simCenter.fuelModel1.C_cp.3.|simCenter.fuelModel1.C_rho.1.|simCenter.fuelModel1.C_rho.2.|simCenter.fuelModel1.C_rho.3.|simCenter.fuelModel1.N_c|simCenter.fuelModel1.N_e|simCenter.fuelModel1.T_ref|simCenter.fuelModel1.ashIndex|simCenter.fuelModel1.defaultComposition.1.|simCenter.fuelModel1.defaultComposition.2.|simCenter.fuelModel1.waterIndex|simCenter.fuelModel1.xi_e_waf.1,1.|simCenter.fuelModel1.xi_e_waf.1,2.|simCenter.fuelModel1.xi_e_waf.1,3.|simCenter.fuelModel1.xi_e_waf.1,4.|simCenter.fuelModel2.C_LHV.1.|simCenter.fuelModel2.C_LHV.2.|simCenter.fuelModel2.C_LHV.3.|simCenter.fuelModel2.C_cp.1.|simCenter.fuelModel2.C_cp.2.|simCenter.fuelModel2.C_cp.3.|simCenter.fuelModel2.C_rho.1.|simCenter.fuelModel2.C_rho.2.|simCenter.fuelModel2.C_rho.3.|simCenter.fuelModel2.N_c|simCenter.fuelModel2.N_e|simCenter.fuelModel2.T_ref|simCenter.fuelModel2.ashIndex|simCenter.fuelModel2.defaultComposition.1.|simCenter.fuelModel2.defaultComposition.2.|simCenter.fuelModel2.waterIndex|simCenter.fuelModel2.xi_e_waf.1,1.|simCenter.fuelModel2.xi_e_waf.1,2.|simCenter.fuelModel2.xi_e_waf.1,3.|simCenter.fuelModel2.xi_e_waf.1,4.|simCenter.h_amb_fluid1|simCenter.h_amb_fluid2|simCenter.h_amb_fluid3|simCenter.largeFonts|simCenter.p_amb|simCenter.p_amb_start|simCenter.rh_amb|simCenter.s_amb_fluid1|simCenter.s_amb_fluid2|simCenter.s_amb_fluid3|simCenter.showExpertSummary|simCenter.slagModel.cp|simCenter.steamCycleAllowFlowReversal|simCenter.summary.eta_gross|simCenter.summary.eta_net|simCenter.summary.eta_util|simCenter.summary.spec_heat_cons|simCenter.useClaRaDelay|simCenter.useHomotopy|threeWayValve_Gas_L1.Delta_p_smooth|threeWayValve_Gas_L1.Tau|threeWayValve_Gas_L1.eye1.T|threeWayValve_Gas_L1.eye1.h|threeWayValve_Gas_L1.eye1.m_flow|threeWayValve_Gas_L1.eye1.p|threeWayValve_Gas_L1.eye1.s|threeWayValve_Gas_L1.eye1.xi.1.|threeWayValve_Gas_L1.eye1.xi.2.|threeWayValve_Gas_L1.eye1.xi.3.|threeWayValve_Gas_L1.eye1.xi.4.|threeWayValve_Gas_L1.eye1.xi.5.|threeWayValve_Gas_L1.eye1.xi.6.|threeWayValve_Gas_L1.eye1.xi.7.|threeWayValve_Gas_L1.eye1.xi.8.|threeWayValve_Gas_L1.eye1.xi.9.|threeWayValve_Gas_L1.eye2.T|threeWayValve_Gas_L1.eye2.h|threeWayValve_Gas_L1.eye2.m_flow|threeWayValve_Gas_L1.eye2.p|threeWayValve_Gas_L1.eye2.s|threeWayValve_Gas_L1.eye2.xi.1.|threeWayValve_Gas_L1.eye2.xi.2.|threeWayValve_Gas_L1.eye2.xi.3.|threeWayValve_Gas_L1.eye2.xi.4.|threeWayValve_Gas_L1.eye2.xi.5.|threeWayValve_Gas_L1.eye2.xi.6.|threeWayValve_Gas_L1.eye2.xi.7.|threeWayValve_Gas_L1.eye2.xi.8.|threeWayValve_Gas_L1.eye2.xi.9.|threeWayValve_Gas_L1.eye_int.1..T|threeWayValve_Gas_L1.eye_int.1..h|threeWayValve_Gas_L1.eye_int.1..m_flow|threeWayValve_Gas_L1.eye_int.1..p|threeWayValve_Gas_L1.eye_int.1..s|threeWayValve_Gas_L1.eye_int.1..xi.1.|threeWayValve_Gas_L1.eye_int.1..xi.2.|threeWayValve_Gas_L1.eye_int.1..xi.3.|threeWayValve_Gas_L1.eye_int.1..xi.4.|threeWayValve_Gas_L1.eye_int.1..xi.5.|threeWayValve_Gas_L1.eye_int.1..xi.6.|threeWayValve_Gas_L1.eye_int.1..xi.7.|threeWayValve_Gas_L1.eye_int.1..xi.8.|threeWayValve_Gas_L1.eye_int.1..xi.9.|threeWayValve_Gas_L1.eye_int.2..T|threeWayValve_Gas_L1.eye_int.2..h|threeWayValve_Gas_L1.eye_int.2..m_flow|threeWayValve_Gas_L1.eye_int.2..p|threeWayValve_Gas_L1.eye_int.2..s|threeWayValve_Gas_L1.eye_int.2..xi.1.|threeWayValve_Gas_L1.eye_int.2..xi.2.|threeWayValve_Gas_L1.eye_int.2..xi.3.|threeWayValve_Gas_L1.eye_int.2..xi.4.|threeWayValve_Gas_L1.eye_int.2..xi.5.|threeWayValve_Gas_L1.eye_int.2..xi.6.|threeWayValve_Gas_L1.eye_int.2..xi.7.|threeWayValve_Gas_L1.eye_int.2..xi.8.|threeWayValve_Gas_L1.eye_int.2..xi.9.|threeWayValve_Gas_L1.iCom.m_flow_in|threeWayValve_Gas_L1.iCom.opening_|threeWayValve_Gas_L1.iCom.p_in|threeWayValve_Gas_L1.iCom.p_out1|threeWayValve_Gas_L1.iCom.p_out2|threeWayV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alve_Gas_L1.iCom.rho_in|threeWayValve_Gas_L1.iCom.rho_out1|threeWayValve_Gas_L1.iCom.rho_out2|threeWayValve_Gas_L1.inlet.T_outflow|threeWayValve_Gas_L1.inlet.m_flow|threeWayValve_Gas_L1.inlet.p|threeWayValve_Gas_L1.inlet.xi_outflow.1.|threeWayValve_Gas_L1.inlet.xi_outflow.2.|threeWayValve_Gas_L1.inlet.xi_outflow.3.|threeWayValve_Gas_L1.inlet.xi_outflow.4.|threeWayValve_Gas_L1.inlet.xi_outflow.5.|threeWayValve_Gas_L1.inlet.xi_outflow.6.|threeWayValve_Gas_L1.inlet.xi_outflow.7.|threeWayValve_Gas_L1.inlet.xi_outflow.8.|threeWayValve_Gas_L1.inlet.xi_outflow.9.|threeWayValve_Gas_L1.outlet1.T_outflow|threeWayValve_Gas_L1.outlet1.m_flow|threeWayValve_Gas_L1.outlet1.p|threeWayValve_Gas_L1.outlet1.xi_outflow.1.|threeWayValve_Gas_L1.outlet1.xi_outflow.2.|threeWayValve_Gas_L1.outlet1.xi_outflow.3.|threeWayValve_Gas_L1.outlet1.xi_outflow.4.|threeWayValve_Gas_L1.outlet1.xi_outflow.5.|threeWayValve_Gas_L1.outlet1.xi_outflow.6.|threeWayValve_Gas_L1.outlet1.xi_outflow.7.|threeWayValve_Gas_L1.outlet1.xi_outflow.8.|threeWayValve_Gas_L1.outlet1.xi_outflow.9.|threeWayValve_Gas_L1.outlet2.T_outflow|threeWayValve_Gas_L1.outlet2.m_flow|threeWayValve_Gas_L1.outlet2.p|threeWayValve_Gas_L1.outlet2.xi_outflow.1.|threeWayValve_Gas_L1.outlet2.xi_outflow.2.|threeWayValve_Gas_L1.outlet2.xi_outflow.3.|threeWayValve_Gas_L1.outlet2.xi_outflow.4.|threeWayValve_Gas_L1.outlet2.xi_outflow.5.|threeWayValve_Gas_L1.outlet2.xi_outflow.6.|threeWayValve_Gas_L1.outlet2.xi_outflow.7.|threeWayValve_Gas_L1.outlet2.xi_outflow.8.|threeWayValve_Gas_L1.outlet2.xi_outflow.9.|threeWayValve_Gas_L1.pressureLoss.CharLineValve_.1,1.|threeWayValve_Gas_L1.pressureLoss.CharLineValve_.1,2.|threeWayValve_Gas_L1.pressureLoss.CharLineValve_.2,1.|threeWayValve_Gas_L1.pressureLoss.CharLineValve_.2,2.|threeWayValve_Gas_L1.pressureLoss.Delta_p.1.|threeWayValve_Gas_L1.pressureLoss.Delta_p.2.|threeWayValve_Gas_L1.pressureLoss.Delta_p_smooth|threeWayValve_Gas_L1.pressureLoss.Tau|threeWayValve_Gas_L1.pressureLoss.aperture_|threeWayValve_Gas_L1.pressureLoss.effectiveFlowArea1|threeWayValve_Gas_L1.pressureLoss.effectiveFlowArea2|threeWayValve_Gas_L1.pressureLoss.m_flow_1|threeWayValve_Gas_L1.pressureLoss.m_flow_2|threeWayValve_Gas_L1.pressureLoss.smoothness|threeWayValve_Gas_L1.pressureLoss.useStabilisedMassFlow|threeWayValve_Gas_L1.showData|threeWayValve_Gas_L1.splitRatio|threeWayValve_Gas_L1.splitRatio_external|threeWayValve_Gas_L1.splitRatio_fixed|threeWayValve_Gas_L1.splitRatio_input|threeWayValve_Gas_L1.summary.inlet.H_flow|threeWayValve_Gas_L1.summary.inlet.T|threeWayValve_Gas_L1.summary.inlet.h|threeWayValve_Gas_L1.summary.inlet.m_flow|threeWayValve_Gas_L1.summary.inlet.p|threeWayValve_Gas_L1.summary.inlet.xi.1.|threeWayValve_Gas_L1.summary.inlet.xi.2.|threeWayValve_Gas_L1.summary.inlet.xi.3.|threeWayValve_Gas_L1.summary.inlet.xi.4.|threeWayValve_Gas_L1.summary.inlet.xi.5.|threeWayValve_Gas_L1.summary.inlet.xi.6.|threeWayValve_Gas_L1.summary.inlet.xi.7.|threeWayValve_Gas_L1.summary.inlet.xi.8.|threeWayValve_Gas_L1.summary.inlet.xi.9.|threeWayValve_Gas_L1.summary.outlet1.H_flow|threeWayValve_Gas_L1.summary.outlet1.T|threeWayValve_Gas_L1.summary.outlet1.h|threeWayValve_Gas_L1.summary.outlet1.m_flow|threeWayValve_Gas_L1.summary.outlet1.p|threeWayValve_Gas_L1.summary.outlet1.xi.1.|threeWayValve_Gas_L1.summary.outlet1.xi.2.|threeWayValve_Gas_L1.summary.outlet1.xi.3.|threeWayValve_Gas_L1.summary.outlet1.xi.4.|threeWayValve_Gas_L1.summary.outlet1.xi.5.|threeWayValve_Gas_L1.summary.outlet1.xi.6.|threeWayValve_Gas_L1.summary.outlet1.xi.7.|threeWayValve_Gas_L1.summary.outlet1.xi.8.|threeWayValve_Gas_L1.summary.outlet1.xi.9.|threeWayValve_Gas_L1.summary.outlet2.H_flow|threeWayValve_Gas_L1.summary.outlet2.T|threeWayValve_Gas_L1.summary.outlet2.h|threeWayValve_Gas_L1.summary.outlet2.m_flow|threeWayValve_Gas_L1.summary.outlet2.p|threeWayValve_Gas_L1.summary.outlet2.xi.1.|threeWayValve_Gas_L1.summary.outlet2.xi.2.|threeWayValve_Gas_L1.summary.outlet2.xi.3.|threeWayValve_Gas_L1.summary.outlet2.xi.4.|threeWayValve_Gas_L1.summary.outlet2.xi.5.|threeWayValve_Gas_L1.summary.outlet2.xi.6.|threeWayValve_Gas_L1.summary.outlet2.xi.7.|threeWayValve_Gas_L1.summary.outlet2.xi.8.|threeWayValve_Gas_L1.summary.outlet2.xi.9.|threeWayValve_Gas_L1.useStabilisedMassFlow",fileNamePrefix="ClaRa_dev_ClaRa.Components.VolumesValvesFittings.Valves.Check.TestThreeWayGasValve")
Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/SMArtIInt 0.2.2-main/package.mo): time 0.009956/0.009956, allocations: 1.437 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 0.1092/0.1092, allocations: 22.37 MB / 41.16 MB, free: 7.77 MB / 34.91 MB
Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/ModelicaServices 4.0.0+maint.om/package.mo): time 0.001119/0.001119, allocations: 104 kB / 48.66 MB, free: 252 kB / 34.91 MB
Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/Complex 4.0.0+maint.om/package.mo): time 0.001307/0.001307, allocations: 198.2 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 1.348/1.348, allocations: 222.9 MB / 286.6 MB, free: 13.98 MB / 222.1 MB
Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/ClaRa 1.8.2-main/package.mo): time 0.8441/0.8441, allocations: 127.8 MB / 471.3 MB, free: 0.5508 MB / 366.1 MB
Notification: Performance of FrontEnd - loaded program: time 0.002237/0.002237, allocations: 127.8 kB / 0.636 GB, free: 13.16 MB / 478.1 MB
Notification: Performance of FrontEnd - Absyn->SCode: time 0.427/0.4293, allocations: 82.34 MB / 0.7164 GB, free: 9.668 MB / 0.5138 GB
Notification: Performance of NFInst.instantiate(ClaRa.Components.VolumesValvesFittings.Valves.Check.TestThreeWayGasValve): time 0.01045/0.4398, allocations: 9.337 MB / 0.7255 GB, free: 2.305 MB / 0.5138 GB
Notification: Performance of NFInst.instExpressions: time 0.01414/0.454, allocations: 9.442 MB / 0.7348 GB, free: 10.77 MB / 0.5294 GB
Notification: Performance of NFInst.updateImplicitVariability: time 0.001572/0.4556, allocations: 29.81 kB / 0.7348 GB, free: 10.77 MB / 0.5294 GB
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/ClaRa 1.8.2-main/SimCenter.mo:69:5-70:35:writable] Warning: Connector cycleSumPort is not balanced: The number of potential variables (0) is not equal to the number of flow variables (4).
Notification: Performance of NFTyping.typeComponents: time 0.0032/0.4588, allocations: 0.9805 MB / 0.7357 GB, free: 10.13 MB / 0.5294 GB
Notification: Performance of NFTyping.typeBindings: time 0.003498/0.4623, allocations: 0.7731 MB / 0.7365 GB, free: 9.516 MB / 0.5294 GB
Notification: Performance of NFTyping.typeClassSections: time 0.004992/0.4673, allocations: 1.352 MB / 0.7378 GB, free: 8.48 MB / 0.5294 GB
Notification: Performance of NFFlatten.flatten: time 0.005562/0.4729, allocations: 2.706 MB / 0.7405 GB, free: 6.891 MB / 0.5294 GB
Notification: Performance of NFFlatten.resolveConnections: time 0.005922/0.4789, allocations: 3.978 MB / 0.7443 GB, free: 3.371 MB / 0.5294 GB
Notification: Performance of NFEvalConstants.evaluate: time 0.003446/0.4824, allocations: 1.905 MB / 0.7462 GB, free: 1.461 MB / 0.5294 GB
Notification: Performance of NFSimplifyModel.simplify: time 0.00399/0.4864, allocations: 2.765 MB / 0.7489 GB, free: 14.69 MB / 0.545 GB
Notification: Performance of NFPackage.collectConstants: time 0.001837/0.4882, allocations: 0.7421 MB / 0.7496 GB, free: 13.95 MB / 0.545 GB
Notification: Performance of NFFlatten.collectFunctions: time 0.004641/0.4929, allocations: 2.025 MB / 0.7516 GB, free: 11.92 MB / 0.545 GB
Notification: Performance of NFScalarize.scalarize: time 0.003819/0.4967, allocations: 3.278 MB / 0.7548 GB, free: 8.637 MB / 0.545 GB
Notification: Performance of NFVerifyModel.verify: time 0.005931/0.5027, allocations: 3.6 MB / 0.7583 GB, free: 5.02 MB / 0.545 GB
Notification: Performance of NFConvertDAE.convert: time 0.01397/0.5167, allocations: 12.19 MB / 0.7702 GB, free: 8.789 MB / 0.5607 GB
Notification: Performance of FrontEnd - DAE generated: time 8.496e-06/0.5167, allocations: 4 kB / 0.7702 GB, free: 8.785 MB / 0.5607 GB
Notification: Performance of FrontEnd: time 1.893e-06/0.5167, allocations: 0 / 0.7702 GB, free: 8.785 MB / 0.5607 GB
Notification: Performance of Transformations before backend: time 0.0002174/0.517, allocations: 4 kB / 0.7702 GB, free: 8.781 MB / 0.5607 GB
Notification: Model statistics after passing the front-end and creating the data structures used by the back-end:
 * Number of equations: 572
 * Number of variables: 572
Notification: Performance of Generate backend data structure: time 0.01796/0.5349, allocations: 8.345 MB / 0.7784 GB, free: 344 kB / 0.5607 GB
Notification: Performance of prepare preOptimizeDAE: time 4.711e-05/0.535, allocations: 8.031 kB / 0.7784 GB, free: 336 kB / 0.5607 GB
Notification: Performance of preOpt normalInlineFunction (simulation): time 0.002452/0.5375, allocations: 0.7808 MB / 0.7792 GB, free: 15.54 MB / 0.5763 GB
Notification: Performance of preOpt evaluateParameters (simulation): time 0.01672/0.5542, allocations: 9.743 MB / 0.7887 GB, free: 5.707 MB / 0.5763 GB
Notification: Performance of preOpt simplifyIfEquations (simulation): time 9.371e-05/0.5543, allocations: 111.4 kB / 0.7888 GB, free: 5.598 MB / 0.5763 GB
Notification: Performance of preOpt expandDerOperator (simulation): time 0.0004966/0.5548, allocations: 148.4 kB / 0.7889 GB, free: 5.453 MB / 0.5763 GB
Notification: Performance of preOpt clockPartitioning (simulation): time 0.008496/0.5633, allocations: 6.769 MB / 0.7955 GB, free: 13.59 MB / 0.5919 GB
Notification: Performance of preOpt findStateOrder (simulation): time 3.53e-05/0.5634, allocations: 7.938 kB / 0.7955 GB, free: 13.59 MB / 0.5919 GB
Notification: Performance of preOpt replaceEdgeChange (simulation): time 0.0003773/0.5638, allocations: 123.9 kB / 0.7957 GB, free: 13.46 MB / 0.5919 GB
Notification: Performance of preOpt inlineArrayEqn (simulation): time 0.0001606/0.5639, allocations: 163.3 kB / 0.7958 GB, free: 13.3 MB / 0.5919 GB
Notification: Performance of preOpt removeEqualRHS (simulation): time 0.01034/0.5743, allocations: 7.014 MB / 0.8027 GB, free: 6.281 MB / 0.5919 GB
Notification: Performance of preOpt removeSimpleEquations (simulation): time 0.02918/0.6035, allocations: 16.48 MB / 0.8188 GB, free: 5.441 MB / 0.6075 GB
Notification: Performance of preOpt comSubExp (simulation): time 0.002886/0.6064, allocations: 2.008 MB / 0.8207 GB, free: 3.414 MB / 0.6075 GB
Notification: Performance of preOpt resolveLoops (simulation): time 0.001988/0.6084, allocations: 1.537 MB / 0.8222 GB, free: 1.867 MB / 0.6075 GB
Notification: Performance of preOpt evalFunc (simulation): time 0.0002202/0.6087, allocations: 49.34 kB / 0.8223 GB, free: 1.82 MB / 0.6075 GB
Notification: Performance of preOpt encapsulateWhenConditions (simulation): time 3.84e-05/0.6087, allocations: 51.5 kB / 0.8223 GB, free: 1.758 MB / 0.6075 GB
Notification: Performance of pre-optimization done (n=243): time 3.927e-06/0.6087, allocations: 0 / 0.8223 GB, free: 1.758 MB / 0.6075 GB
Notification: Performance of matching and sorting (n=243): time 0.008863/0.6176, allocations: 5.373 MB / 0.8276 GB, free: 12.34 MB / 0.6232 GB
Notification: Performance of inlineWhenForInitialization (initialization): time 6.266e-05/0.6177, allocations: 94.09 kB / 0.8276 GB, free: 12.23 MB / 0.6232 GB
Notification: Performance of selectInitializationVariablesDAE (initialization): time 0.01117/0.6289, allocations: 6.344 MB / 0.8338 GB, free: 5.906 MB / 0.6232 GB
Notification: Performance of collectPreVariables (initialization): time 0.0002975/0.6292, allocations: 53.7 kB / 0.8339 GB, free: 5.848 MB / 0.6232 GB
Notification: Performance of collectInitialEqns (initialization): time 0.002133/0.6313, allocations: 2.512 MB / 0.8363 GB, free: 3.328 MB / 0.6232 GB
Notification: Performance of collectInitialBindings (initialization): time 0.0008022/0.6321, allocations: 0.8326 MB / 0.8372 GB, free: 2.488 MB / 0.6232 GB
Notification: Performance of simplifyInitialFunctions (initialization): time 0.001028/0.6332, allocations: 0.5479 MB / 0.8377 GB, free: 1.93 MB / 0.6232 GB
Notification: Performance of setup shared object (initialization): time 0.0001021/0.6333, allocations: 309.1 kB / 0.838 GB, free: 1.625 MB / 0.6232 GB
Notification: Performance of preBalanceInitialSystem (initialization): time 0.002546/0.6358, allocations: 1.754 MB / 0.8397 GB, free: 15.86 MB / 0.6388 GB
Notification: Performance of partitionIndependentBlocks (initialization): time 0.003294/0.6391, allocations: 2.554 MB / 0.8422 GB, free: 12.96 MB / 0.6388 GB
Notification: Performance of analyzeInitialSystem (initialization): time 0.006355/0.6455, allocations: 4.272 MB / 0.8464 GB, free: 8.309 MB / 0.6388 GB
Notification: Performance of solveInitialSystemEqSystem (initialization): time 3.165e-05/0.6456, allocations: 8 kB / 0.8464 GB, free: 8.301 MB / 0.6388 GB
Notification: Performance of matching and sorting (n=372) (initialization): time 0.009831/0.6554, allocations: 5.126 MB / 0.8514 GB, free: 3.121 MB / 0.6388 GB
Notification: Performance of prepare postOptimizeDAE: time 5.176e-05/0.6555, allocations: 12 kB / 0.8514 GB, free: 3.109 MB / 0.6388 GB
Notification: Performance of postOpt simplifyComplexFunction (initialization): time 0.0001152/0.6556, allocations: 59.92 kB / 0.8515 GB, free: 3.051 MB / 0.6388 GB
Notification: Performance of postOpt tearingSystem (initialization): time 0.002394/0.658, allocations: 2.047 MB / 0.8534 GB, free: 1 MB / 0.6388 GB
Notification: Performance of postOpt solveSimpleEquations (initialization): time 0.004082/0.6622, allocations: 0.5421 MB / 0.854 GB, free: 468 kB / 0.6388 GB
Notification: Performance of postOpt calculateStrongComponentJacobians (initialization): time 0.001488/0.6637, allocations: 1.622 MB / 0.8556 GB, free: 14.78 MB / 0.6544 GB
Notification: Performance of postOpt simplifyAllExpressions (initialization): time 0.003567/0.6672, allocations: 301.7 kB / 0.8559 GB, free: 14.48 MB / 0.6544 GB
Notification: Performance of postOpt collapseArrayExpressions (initialization): time 0.0004747/0.6677, allocations: 139.9 kB / 0.856 GB, free: 14.34 MB / 0.6544 GB
Notification: Model statistics after passing the back-end for initialization:
 * Number of independent subsystems: 113
 * 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 (254):
 * Single equations (assignments): 245
 * Array equations: 0
 * Algorithm blocks: 0
 * Record equations: 7
 * 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
   {(1,2), (1,2)}
Notification: Performance of prepare postOptimizeDAE: time 0.003418/0.6712, allocations: 1.832 MB / 0.8578 GB, free: 12.5 MB / 0.6544 GB
Notification: Performance of postOpt lateInlineFunction (simulation): time 0.001325/0.6725, allocations: 0.5858 MB / 0.8583 GB, free: 11.91 MB / 0.6544 GB
Notification: Performance of postOpt wrapFunctionCalls (simulation): time 0.007592/0.6801, allocations: 3.872 MB / 0.8621 GB, free: 8.02 MB / 0.6544 GB
Notification: Performance of postOpt simplifysemiLinear (simulation): time 1.968e-05/0.6802, allocations: 3.984 kB / 0.8621 GB, free: 8.016 MB / 0.6544 GB
Notification: Performance of postOpt simplifyComplexFunction (simulation): time 5.922e-05/0.6802, allocations: 27.97 kB / 0.8622 GB, free: 7.988 MB / 0.6544 GB
Notification: Performance of postOpt removeConstants (simulation): time 0.00256/0.6828, allocations: 1.101 MB / 0.8632 GB, free: 6.863 MB / 0.6544 GB
Notification: Performance of postOpt simplifyTimeIndepFuncCalls (simulation): time 0.0009059/0.6837, allocations: 24 kB / 0.8633 GB, free: 6.84 MB / 0.6544 GB
Notification: Performance of postOpt simplifyAllExpressions (simulation): time 0.001926/0.6856, allocations: 39.97 kB / 0.8633 GB, free: 6.801 MB / 0.6544 GB
Notification: Performance of postOpt findZeroCrossings (simulation): time 0.0002525/0.6859, allocations: 84.88 kB / 0.8634 GB, free: 6.715 MB / 0.6544 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): (threeWayValve_Gas_L1.iCom.rho_out1, threeWayValve_Gas_L1.gasOut1.kappa, threeWayValve_Gas_L1.gasOut1.drhodp_hxi, threeWayValve_Gas_L1.gasOut1.drhodh_pxi, threeWayValve_Gas_L1.gasOut1.drhodxi_ph, threeWayValve_Gas_L1.gasOut1.p_i, threeWayValve_Gas_L1.gasOut1.xi_gas) = TILMedia.Internals.GasObjectFunctions.additionalProperties_pTxi(pressureSink_ph2.p_const, threeWayValve_Gas_L1.summary.outlet1.T, {9.910802775024783e-4, 9.910802775024783e-4, 9.910802775024783e-4, 9.910802775024783e-4, 0.9910802775024783, 9.910802775024783e-4, 9.910802775024783e-4, 9.910802775024783e-4, 9.910802775024783e-4}, threeWayValve_Gas_L1.gasOut1.gasPointer)

Variables:
1: threeWayValve_Gas_L1.gasOut1.p_i[8]:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 protected = true )  "Partial pressure" type: Real [10]
2: threeWayValve_Gas_L1.gasOut1.drhodp_hxi:VARIABLE(unit = "s2/m2" protected = true )  "Derivative of density wrt pressure at specific enthalpy and mass fraction" type: Real
3: threeWayValve_Gas_L1.gasOut1.p_i[9]:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 protected = true )  "Partial pressure" type: Real [10]
4: threeWayValve_Gas_L1.gasOut1.p_i[2]:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 protected = true )  "Partial pressure" type: Real [10]
5: threeWayValve_Gas_L1.gasOut1.p_i[10]:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 protected = true )  "Partial pressure" type: Real [10]
6: threeWayValve_Gas_L1.gasOut1.drhodxi_ph[7]:VARIABLE(unit = "kg/(m3)" protected = true )  "Derivative of density wrt mass fraction of water at constant pressure and specific enthalpy" type: Real [9]
7: threeWayValve_Gas_L1.gasOut1.drhodxi_ph[5]:VARIABLE(unit = "kg/(m3)" protected = true )  "Derivative of density wrt mass fraction of water at constant pressure and specific enthalpy" type: Real [9]
8: threeWayValve_Gas_L1.gasOut1.p_i[3]:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 protected = true )  "Partial pressure" type: Real [10]
9: threeWayValve_Gas_L1.gasOut1.drhodxi_ph[1]:VARIABLE(unit = "kg/(m3)" protected = true )  "Derivative of density wrt mass fraction of water at constant pressure and specific enthalpy" type: Real [9]
10: threeWayValve_Gas_L1.gasOut1.p_i[4]:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 protected = true )  "Partial pressure" type: Real [10]
11: threeWayValve_Gas_L1.iCom.rho_out1:VARIABLE(min = 0.0 unit = "kg/m3" nominal = 1000.0 )  "Outlet density at straight flange" type: Real
12: threeWayValve_Gas_L1.gasOut1.drhodxi_ph[3]:VARIABLE(unit = "kg/(m3)" protected = true )  "Derivative of density wrt mass fraction of water at constant pressure and specific enthalpy" type: Real [9]
13: threeWayValve_Gas_L1.gasOut1.p_i[5]:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 protected = true )  "Partial pressure" type: Real [10]
14: threeWayValve_Gas_L1.gasOut1.p_i[1]:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 protected = true )  "Partial pressure" type: Real [10]
15: threeWayValve_Gas_L1.gasOut1.kappa:VARIABLE(unit = "1/Pa" protected = true )  "Isothermal compressibility" type: Real
16: threeWayValve_Gas_L1.gasOut1.xi_gas:VARIABLE(min = 0.0 max = 1.0 unit = "1" protected = true )  "Mass fraction of gasoues condensing component" type: Real
17: threeWayValve_Gas_L1.gasOut1.p_i[7]:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 protected = true )  "Partial pressure" type: Real [10]
18: threeWayValve_Gas_L1.gasOut1.drhodh_pxi:VARIABLE(unit = "kg.s2/m5" protected = true )  "Derivative of density wrt specific enthalpy at constant pressure and mass fraction" type: Real
19: threeWayValve_Gas_L1.gasOut1.p_i[6]:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 protected = true )  "Partial pressure" type: Real [10]
20: threeWayValve_Gas_L1.gasOut1.drhodxi_ph[9]:VARIABLE(unit = "kg/(m3)" protected = true )  "Derivative of density wrt mass fraction of water at constant pressure and specific enthalpy" type: Real [9]
21: threeWayValve_Gas_L1.gasOut1.drhodxi_ph[6]:VARIABLE(unit = "kg/(m3)" protected = true )  "Derivative of density wrt mass fraction of water at constant pressure and specific enthalpy" type: Real [9]
22: threeWayValve_Gas_L1.gasOut1.drhodxi_ph[8]:VARIABLE(unit = "kg/(m3)" protected = true )  "Derivative of density wrt mass fraction of water at constant pressure and specific enthalpy" type: Real [9]
23: threeWayValve_Gas_L1.gasOut1.drhodxi_ph[2]:VARIABLE(unit = "kg/(m3)" protected = true )  "Derivative of density wrt mass fraction of water at constant pressure and specific enthalpy" type: Real [9]
24: threeWayValve_Gas_L1.gasOut1.drhodxi_ph[4]:VARIABLE(unit = "kg/(m3)" protected = true )  "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): threeWayValve_Gas_L1.pressureLoss.m_flow_1 = 1.4142135623730951 * sqrt(threeWayValve_Gas_L1.iCom.rho_out1) * $cse1 * threeWayValve_Gas_L1.pressureLoss.aperture_ * threeWayValve_Gas_L1.pressureLoss.effectiveFlowArea1
2/2 (1): threeWayValve_Gas_L1.summary.outlet1.T = if noEvent((-threeWayValve_Gas_L1.pressureLoss.m_flow_1) > 0.0) then pressureSink_ph2.T_const else massFlowSource_h1.T_const
3/3 (24): (threeWayValve_Gas_L1.iCom.rho_out1, threeWayValve_Gas_L1.gasOut1.kappa, threeWayValve_Gas_L1.gasOut1.drhodp_hxi, threeWayValve_Gas_L1.gasOut1.drhodh_pxi, threeWayValve_Gas_L1.gasOut1.drhodxi_ph, threeWayValve_Gas_L1.gasOut1.p_i, threeWayValve_Gas_L1.gasOut1.xi_gas) = TILMedia.Internals.GasObjectFunctions.additionalProperties_pTxi(pressureSink_ph2.p_const, threeWayValve_Gas_L1.summary.outlet1.T, {9.910802775024783e-4, 9.910802775024783e-4, 9.910802775024783e-4, 9.910802775024783e-4, 0.9910802775024783, 9.910802775024783e-4, 9.910802775024783e-4, 9.910802775024783e-4, 9.910802775024783e-4}, threeWayValve_Gas_L1.gasOut1.gasPointer)

Variables:
1: threeWayValve_Gas_L1.gasOut1.p_i[8]:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 protected = true )  "Partial pressure" type: Real [10]
2: threeWayValve_Gas_L1.gasOut1.drhodp_hxi:VARIABLE(unit = "s2/m2" protected = true )  "Derivative of density wrt pressure at specific enthalpy and mass fraction" type: Real
3: threeWayValve_Gas_L1.gasOut1.p_i[9]:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 protected = true )  "Partial pressure" type: Real [10]
4: threeWayValve_Gas_L1.gasOut1.p_i[2]:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 protected = true )  "Partial pressure" type: Real [10]
5: threeWayValve_Gas_L1.gasOut1.p_i[10]:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 protected = true )  "Partial pressure" type: Real [10]
6: threeWayValve_Gas_L1.gasOut1.drhodxi_ph[7]:VARIABLE(unit = "kg/(m3)" protected = true )  "Derivative of density wrt mass fraction of water at constant pressure and specific enthalpy" type: Real [9]
7: threeWayValve_Gas_L1.gasOut1.drhodxi_ph[5]:VARIABLE(unit = "kg/(m3)" protected = true )  "Derivative of density wrt mass fraction of water at constant pressure and specific enthalpy" type: Real [9]
8: threeWayValve_Gas_L1.gasOut1.p_i[3]:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 protected = true )  "Partial pressure" type: Real [10]
9: threeWayValve_Gas_L1.gasOut1.drhodxi_ph[1]:VARIABLE(unit = "kg/(m3)" protected = true )  "Derivative of density wrt mass fraction of water at constant pressure and specific enthalpy" type: Real [9]
10: threeWayValve_Gas_L1.gasOut1.p_i[4]:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 protected = true )  "Partial pressure" type: Real [10]
11: threeWayValve_Gas_L1.iCom.rho_out1:VARIABLE(min = 0.0 unit = "kg/m3" nominal = 1000.0 )  "Outlet density at straight flange" type: Real
12: threeWayValve_Gas_L1.gasOut1.drhodxi_ph[3]:VARIABLE(unit = "kg/(m3)" protected = true )  "Derivative of density wrt mass fraction of water at constant pressure and specific enthalpy" type: Real [9]
13: threeWayValve_Gas_L1.gasOut1.p_i[5]:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 protected = true )  "Partial pressure" type: Real [10]
14: threeWayValve_Gas_L1.gasOut1.p_i[1]:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 protected = true )  "Partial pressure" type: Real [10]
15: threeWayValve_Gas_L1.gasOut1.kappa:VARIABLE(unit = "1/Pa" protected = true )  "Isothermal compressibility" type: Real
16: threeWayValve_Gas_L1.gasOut1.xi_gas:VARIABLE(min = 0.0 max = 1.0 unit = "1" protected = true )  "Mass fraction of gasoues condensing component" type: Real
17: threeWayValve_Gas_L1.gasOut1.p_i[7]:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 protected = true )  "Partial pressure" type: Real [10]
18: threeWayValve_Gas_L1.gasOut1.drhodh_pxi:VARIABLE(unit = "kg.s2/m5" protected = true )  "Derivative of density wrt specific enthalpy at constant pressure and mass fraction" type: Real
19: threeWayValve_Gas_L1.gasOut1.p_i[6]:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 protected = true )  "Partial pressure" type: Real [10]
20: threeWayValve_Gas_L1.gasOut1.drhodxi_ph[9]:VARIABLE(unit = "kg/(m3)" protected = true )  "Derivative of density wrt mass fraction of water at constant pressure and specific enthalpy" type: Real [9]
21: threeWayValve_Gas_L1.gasOut1.drhodxi_ph[6]:VARIABLE(unit = "kg/(m3)" protected = true )  "Derivative of density wrt mass fraction of water at constant pressure and specific enthalpy" type: Real [9]
22: threeWayValve_Gas_L1.gasOut1.drhodxi_ph[8]:VARIABLE(unit = "kg/(m3)" protected = true )  "Derivative of density wrt mass fraction of water at constant pressure and specific enthalpy" type: Real [9]
23: threeWayValve_Gas_L1.gasOut1.drhodxi_ph[2]:VARIABLE(unit = "kg/(m3)" protected = true )  "Derivative of density wrt mass fraction of water at constant pressure and specific enthalpy" type: Real [9]
24: threeWayValve_Gas_L1.gasOut1.drhodxi_ph[4]:VARIABLE(unit = "kg/(m3)" protected = true )  "Derivative of density wrt mass fraction of water at constant pressure and specific enthalpy" type: Real [9]
25: threeWayValve_Gas_L1.summary.outlet1.T:VARIABLE(min = 0.0 start = 288.15 unit = "K" nominal = 300.0 )  "Temperature" type: Real
26: threeWayValve_Gas_L1.pressureLoss.m_flow_1:VARIABLE(unit = "kg/s" nominal = 1.0 )  "Mass flow through straight flange" 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 0.001222/0.6871, allocations: 0.8428 MB / 0.8642 GB, free: 5.77 MB / 0.6544 GB
Error: post-optimization module createDAEmodeBDAE (simulation) failed.
Error: Internal error SimCode DAEmode: The model ClaRa.Components.VolumesValvesFittings.Valves.Check.TestThreeWayGasValve could not be translated