Running: ./testmodel.py --libraries=/home/hudson/saved_omc/libraries/.openmodelica/libraries --ompython_omhome=/usr ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion.conf.json
loadFile("/home/hudson/saved_omc/libraries/.openmodelica/libraries/ModelicaServices 4.1.0+maint.om/package.mo", uses=false) [Timeout 180]
"Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/ModelicaServices 4.1.0+maint.om/package.mo): time 0.000837/0.000837, allocations: 90.56 kB / 20.21 MB, free: 4.055 MB / 18.57 MB
"
[Timeout remaining time 180]
loadFile("/home/hudson/saved_omc/libraries/.openmodelica/libraries/Complex 4.1.0+maint.om/package.mo", uses=false) [Timeout 180]
"Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/Complex 4.1.0+maint.om/package.mo): time 0.000933/0.000933, allocations: 169.3 kB / 23.54 MB, free: 0.7344 MB / 18.57 MB
"
[Timeout remaining time 180]
loadFile("/home/hudson/saved_omc/libraries/.openmodelica/libraries/Modelica 4.1.0+maint.om/package.mo", uses=false) [Timeout 180]
"Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/Modelica 4.1.0+maint.om/package.mo): time 0.8654/0.8654, allocations: 177.1 MB / 203.9 MB, free: 5.586 MB / 186.7 MB
"
[Timeout remaining time 179]
loadFile("/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermofluidStream 1.4.0/package.mo", uses=false) [Timeout 180]
"Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermofluidStream 1.4.0/package.mo): time 0.6121/0.6121, allocations: 118.6 MB / 379 MB, free: 1.48 MB / 346.7 MB
"
[Timeout remaining time 179]
Using package ThermofluidStream with version 1.4.0 (/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermofluidStream 1.4.0/package.mo)
Using package Modelica with version 4.1.0 (/home/hudson/saved_omc/libraries/.openmodelica/libraries/Modelica 4.1.0+maint.om/package.mo)
Using package Complex with version 4.1.0 (/home/hudson/saved_omc/libraries/.openmodelica/libraries/Complex 4.1.0+maint.om/package.mo)
Using package ModelicaServices with version 4.1.0 (/home/hudson/saved_omc/libraries/.openmodelica/libraries/ModelicaServices 4.1.0+maint.om/package.mo)
Running command: translateModel(ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion,tolerance=1e-06,outputFormat="mat",numberOfIntervals=100,variableFilter="CPUtime|EventCounter|NonlinearSystems.initialization.1..Calls|NonlinearSystems.initialization.1..Iterations|NonlinearSystems.initialization.1..Jacobians|NonlinearSystems.initialization.1..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|Time|boiler.L|boiler.P|boiler.Q_flow|boiler.T_out_fixed|boiler.assertionLevel|boiler.clip_p_out|boiler.dT|boiler.dT_fixed|boiler.dh|boiler.dh_fixed|boiler.dp|boiler.dr_corr|boiler.du|boiler.h_in|boiler.h_out|boiler.h_out_fixed|boiler.initM_flow|der.boiler.inlet.m_flow.|boiler.inlet.m_flow|boiler.inlet.r|boiler.inlet.state.T|boiler.inlet.state.d|boiler.inlet.state.h|boiler.inlet.state.p|boiler.inlet.state.phase|boiler.m_acceleration_0|boiler.m_flow|boiler.m_flowStateSelect|boiler.m_flow_0|boiler.outlet.m_flow|boiler.outlet.r|boiler.outlet.state.T|boiler.outlet.state.d|boiler.outlet.state.h|boiler.outlet.state.p|boiler.outlet.state.phase|boiler.outletSpec|boiler.outletSpec_actual|boiler.outletSpec_prescribed|boiler.outletValueSpec|boiler.p|boiler.p_in|boiler.p_inf|boiler.p_min|boiler.p_out|boiler.q|boiler.rho_in|boiler.rho_out|boiler.singularityRegime|boiler.systemSpec|boiler.u_in|boiler.u_out|boiler.v_in|boiler.v_out|boiler.w_amb|boiler.w_exp|boiler.w_exp_net|condenser.L|condenser.P|condenser.Q_flow|condenser.T_out_fixed|condenser.assertionLevel|condenser.clip_p_out|condenser.dT|condenser.dT_fixed|condenser.dh|condenser.dh_fixed|condenser.dp|condenser.dr_corr|condenser.du|condenser.h_in|condenser.h_out|condenser.h_out_fixed|condenser.initM_flow|der.condenser.inlet.m_flow.|condenser.inlet.m_flow|condenser.inlet.r|condenser.inlet.state.T|condenser.inlet.state.d|condenser.inlet.state.h|condenser.inlet.state.p|condenser.inlet.state.phase|condenser.m_acceleration_0|condenser.m_flow|condenser.m_flowStateSelect|condenser.m_flow_0|condenser.outlet.m_flow|condenser.outlet.r|condenser.outlet.state.T|condenser.outlet.state.d|condenser.outlet.state.h|condenser.outlet.state.p|condenser.outlet.state.phase|condenser.outletSpec|condenser.outletSpec_actual|condenser.outletValueSpec|condenser.p|condenser.p_in|condenser.p_inf|condenser.p_min|condenser.p_out|condenser.q|condenser.rho_in|condenser.rho_out|condenser.singularityRegime|condenser.systemSpec|condenser.u_in|condenser.u_out|condenser.v_in|condenser.v_out|condenser.w_amb|condenser.w_exp|condenser.w_exp_net|dropOfCommons.L|dropOfCommons.assertionLevel|dropOfCommons.g|dropOfCommons.instanceNameColor.1.|dropOfCommons.instanceNameColor.2.|dropOfCommons.instanceNameColor.3.|dropOfCommons.k_volume_damping|dropOfCommons.m_flow_reg|dropOfCommons.omega_reg|dropOfCommons.p_min|dropOfCommons.rho_min|efficiencyExtensive.displayVariablefinal|efficiencyExtensive.showNumber|efficiencyExtensive.significantDigits|efficiencySpecific.displayVariablefinal|efficiencySpecific.showNumber|efficiencySpecific.significantDigits|firstOrder.T|der.firstOrder.y.|firstOrder.initType|firstOrder.k|firstOrder.u|firstOrder.y|firstOrder.y_start|h_bubble.y|h_dew.y|inverseBlockConstraints.u1|inverseBlockConstraints.u2|inverseBlockConstraints.y1|inverseBlockConstraints.y2|loopBreaker.L|loopBreaker.T_out|loopBreaker.T_out_fixed|loopBreaker.XiSpec|loopBreaker.assertionLevel|loopBreaker.dh|loopBreaker.dm_flow|loopBreaker.dp|loopBreaker.h_out|loopBreaker.h_out_fixed|loopBreaker.inlet.m_flow|loopBreaker.inlet.r|loopBreaker.inlet.state.T|loopBreaker.inlet.state.d|loopBreaker.inlet.state.h|loopBreaker.inlet.state.p|loopBreaker.inlet.state.phase|loopBreaker.m_flowSpec|loopBreaker.m_flow_in|loopBreaker.m_flow_in_par|loopBreaker.m_flow_in_prescribed|der.loopBreaker.outlet.m_flow.|loopBreaker.outlet.m_flow|loopBreaker.outlet.r|loopBreaker.outlet.state.T|loopBreaker.outlet.state.d|loopBreaker.outlet.state.h|loopBreaker.outlet.state.p|loopBreaker.outlet.state.phase|loopBreaker.pSpec|loopBreaker.p_out|loopBreaker.p_out_fixed|loopBreaker.thermalSpec|loopBreaker.thermalValueSpec|loopBreaker.tol_Xi|loopBreaker.tol_h|loopBreaker.tol_m_flow|loopBreaker.tol_p|massFlowRate.height|massFlowRate.offset|massFlowRate.startTime|massFlowRate.y|outletPressure.duration|outletPressure.height|outletPressure.offset|outletPressure.startTime|outletPressure.y|preheater.L|preheater.P|preheater.Q_flow|preheater.T_out_fixed|preheater.assertionLevel|preheater.clip_p_out|preheater.dT|preheater.dT_fixed|preheater.dh|preheater.dh_fixed|preheater.dp|preheater.dr_corr|preheater.du|preheater.h_in|preheater.h_out|preheater.h_out_fixed|preheater.initM_flow|der.preheater.inlet.m_flow.|preheater.inlet.m_flow|preheater.inlet.r|preheater.inlet.state.T|preheater.inlet.state.d|preheater.inlet.state.h|preheater.inlet.state.p|preheater.inlet.state.phase|preheater.m_acceleration_0|preheater.m_flow|preheater.m_flowStateSelect|preheater.m_flow_0|preheater.outlet.m_flow|preheater.outlet.r|preheater.outlet.state.T|preheater.outlet.state.d|preheater.outlet.state.h|preheater.outlet.state.p|preheater.outlet.state.phase|preheater.outletSpec|preheater.outletSpec_actual|preheater.outletSpec_prescribed|preheater.outletValueSpec|preheater.p|preheater.p_in|preheater.p_inf|preheater.p_min|preheater.p_out|preheater.q|preheater.rho_in|preheater.rho_out|preheater.singularityRegime|preheater.systemSpec|preheater.u_in|preheater.u_out|preheater.v_in|preheater.v_out|preheater.w_amb|preheater.w_exp|preheater.w_exp_net|pump.L|pump.P|pump.P_nom|pump.TC|pump.adiabaticModel.eta_is|pump.adiabaticModel.h_in|pump.adiabaticModel.h_out|pump.adiabaticModel.h_out_is|pump.adiabaticModel.p_out|pump.adiabaticModel.s_in|pump.adiabaticModel.state_in.T|pump.adiabaticModel.state_in.d|pump.adiabaticModel.state_in.h|pump.adiabaticModel.state_in.p|pump.adiabaticModel.state_in.phase|pump.adiabaticModel.w_t|pump.adiabaticModel.w_t_is|pump.assertionLevel|pump.clip_p_out|pump.dh|pump.dp|pump.dp_fixed|pump.dp_nom|pump.dp_start|pump.dr_corr|pump.etaSpec|pump.eta_actual|pump.eta_fixed|pump.eta_is|pump.h_in|pump.h_out|pump.initM_flow|der.pump.inlet.m_flow.|pump.inlet.m_flow|pump.inlet.r|pump.inlet.state.T|pump.inlet.state.d|pump.inlet.state.h|pump.inlet.state.p|pump.inlet.state.phase|pump.m_acceleration_0|pump.m_flow|pump.m_flowStateSelect|pump.m_flow_0|pump.outlet.m_flow|pump.outlet.r|pump.outlet.state.T|pump.outlet.state.d|pump.outlet.state.h|pump.outlet.state.p|pump.outlet.state.phase|pump.outletSpec|pump.outletSpec_actual|pump.outletSpec_prescribed|pump.outletValueSpec|pump.pRatio|pump.pRatio_fixed|pump.p_in|pump.p_min|pump.p_out|pump.p_out_fixed|pump.singularityRegime|superheater.L|superheater.P|superheater.Q_flow|superheater.T_out_fixed|superheater.assertionLevel|superheater.clip_p_out|superheater.dT|superheater.dT_fixed|superheater.dh|superheater.dh_fixed|superheater.dp|superheater.dr_corr|superheater.du|superheater.h_in|superheater.h_out|superheater.h_out_fixed|superheater.initM_flow|der.superheater.inlet.m_flow.|superheater.inlet.m_flow|superheater.inlet.r|superheater.inlet.state.T|superheater.inlet.state.d|superheater.inlet.state.h|superheater.inlet.state.p|superheater.inlet.state.phase|superheater.m_acceleration_0|superheater.m_flow|superheater.m_flowStateSelect|superheater.m_flow_0|superheater.outlet.m_flow|superheater.outlet.r|superheater.outlet.state.T|superheater.outlet.state.d|superheater.outlet.state.h|superheater.outlet.state.p|superheater.outlet.state.phase|superheater.outletSpec|superheater.outletSpec_actual|superheater.outletSpec_prescribed|superheater.outletValueSpec|superheater.p|superheater.p_in|superheater.p_inf|superheater.p_min|superheater.p_out|superheater.q|superheater.rho_in|superheater.rho_out|superheater.singularityRegime|superheater.systemSpec|superheater.u_in|superheater.u_out|superheater.v_in|superheater.v_out|superheater.w_amb|superheater.w_exp|superheater.w_exp_net|turbine.L|turbine.P|turbine.P_nom|turbine.TC|turbine.adiabaticModel.eta_is|turbine.adiabaticModel.h_in|turbine.adiabaticModel.h_out|turbine.adiabaticModel.h_out_is|turbine.adiabaticModel.p_out|turbine.adiabaticModel.s_in|turbine.adiabaticModel.state_in.T|turbine.adiabaticModel.state_in.d|turbine.adiabaticModel.state_in.h|turbine.adiabaticModel.state_in.p|turbine.adiabaticModel.state_in.phase|turbine.adiabaticModel.w_t|turbine.adiabaticModel.w_t_is|turbine.assertionLevel|turbine.clip_p_out|turbine.dh|turbine.dp|turbine.dp_fixed|turbine.dp_nom|turbine.dp_start|turbine.dr_corr|turbine.etaSpec|turbine.eta_actual|turbine.eta_fixed|turbine.eta_is|turbine.h_in|turbine.h_out|turbine.initM_flow|der.turbine.inlet.m_flow.|turbine.inlet.m_flow|turbine.inlet.r|turbine.inlet.state.T|turbine.inlet.state.d|turbine.inlet.state.h|turbine.inlet.state.p|turbine.inlet.state.phase|turbine.m_acceleration_0|turbine.m_flow|turbine.m_flowStateSelect|turbine.m_flow_0|turbine.outlet.m_flow|turbine.outlet.r|turbine.outlet.state.T|turbine.outlet.state.d|turbine.outlet.state.h|turbine.outlet.state.p|turbine.outlet.state.phase|turbine.outletSpec|turbine.outletSpec_actual|turbine.outletValueSpec|turbine.pRatio|turbine.pRatio_fixed|turbine.p_in|turbine.p_min|turbine.p_out|turbine.p_out_fixed|turbine.singularityRegime|vaporQualitySensor.TC|vaporQualitySensor.digits|vaporQualitySensor.direct_value|vaporQualitySensor.init|vaporQualitySensor.inlet.m_flow|vaporQualitySensor.inlet.r|vaporQualitySensor.inlet.state.T|vaporQualitySensor.inlet.state.d|vaporQualitySensor.inlet.state.h|vaporQualitySensor.inlet.state.p|vaporQualitySensor.inlet.state.phase|vaporQualitySensor.quantity|vaporQualitySensor.value|vaporQualitySensor.value_0|vaporQualitySensor.value_out|vaporQualitySetpoint.y",fileNamePrefix="ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion")
translateModel(ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion,tolerance=1e-06,outputFormat="mat",numberOfIntervals=100,variableFilter="CPUtime|EventCounter|NonlinearSystems.initialization.1..Calls|NonlinearSystems.initialization.1..Iterations|NonlinearSystems.initialization.1..Jacobians|NonlinearSystems.initialization.1..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|Time|boiler.L|boiler.P|boiler.Q_flow|boiler.T_out_fixed|boiler.assertionLevel|boiler.clip_p_out|boiler.dT|boiler.dT_fixed|boiler.dh|boiler.dh_fixed|boiler.dp|boiler.dr_corr|boiler.du|boiler.h_in|boiler.h_out|boiler.h_out_fixed|boiler.initM_flow|der.boiler.inlet.m_flow.|boiler.inlet.m_flow|boiler.inlet.r|boiler.inlet.state.T|boiler.inlet.state.d|boiler.inlet.state.h|boiler.inlet.state.p|boiler.inlet.state.phase|boiler.m_acceleration_0|boiler.m_flow|boiler.m_flowStateSelect|boiler.m_flow_0|boiler.outlet.m_flow|boiler.outlet.r|boiler.outlet.state.T|boiler.outlet.state.d|boiler.outlet.state.h|boiler.outlet.state.p|boiler.outlet.state.phase|boiler.outletSpec|boiler.outletSpec_actual|boiler.outletSpec_prescribed|boiler.outletValueSpec|boiler.p|boiler.p_in|boiler.p_inf|boiler.p_min|boiler.p_out|boiler.q|boiler.rho_in|boiler.rho_out|boiler.singularityRegime|boiler.systemSpec|boiler.u_in|boiler.u_out|boiler.v_in|boiler.v_out|boiler.w_amb|boiler.w_exp|boiler.w_exp_net|condenser.L|condenser.P|condenser.Q_flow|condenser.T_out_fixed|condenser.assertionLevel|condenser.clip_p_out|condenser.dT|condenser.dT_fixed|condenser.dh|condenser.dh_fixed|condenser.dp|condenser.dr_corr|condenser.du|condenser.h_in|condenser.h_out|condenser.h_out_fixed|condenser.initM_flow|der.condenser.inlet.m_flow.|condenser.inlet.m_flow|condenser.inlet.r|condenser.inlet.state.T|condenser.inlet.state.d|condenser.inlet.state.h|condenser.inlet.state.p|condenser.inlet.state.phase|condenser.m_acceleration_0|condenser.m_flow|condenser.m_flowStateSelect|condenser.m_flow_0|condenser.outlet.m_flow|condenser.outlet.r|condenser.outlet.state.T|condenser.outlet.state.d|condenser.outlet.state.h|condenser.outlet.state.p|condenser.outlet.state.phase|condenser.outletSpec|condenser.outletSpec_actual|condenser.outletValueSpec|condenser.p|condenser.p_in|condenser.p_inf|condenser.p_min|condenser.p_out|condenser.q|condenser.rho_in|condenser.rho_out|condenser.singularityRegime|condenser.systemSpec|condenser.u_in|condenser.u_out|condenser.v_in|condenser.v_out|condenser.w_amb|condenser.w_exp|condenser.w_exp_net|dropOfCommons.L|dropOfCommons.assertionLevel|dropOfCommons.g|dropOfCommons.instanceNameColor.1.|dropOfCommons.instanceNameColor.2.|dropOfCommons.instanceNameColor.3.|dropOfCommons.k_volume_damping|dropOfCommons.m_flow_reg|dropOfCommons.omega_reg|dropOfCommons.p_min|dropOfCommons.rho_min|efficiencyExtensive.displayVariablefinal|efficiencyExtensive.showNumber|efficiencyExtensive.significantDigits|efficiencySpecific.displayVariablefinal|efficiencySpecific.showNumber|efficiencySpecific.significantDigits|firstOrder.T|der.firstOrder.y.|firstOrder.initType|firstOrder.k|firstOrder.u|firstOrder.y|firstOrder.y_start|h_bubble.y|h_dew.y|inverseBlockConstraints.u1|inverseBlockConstraints.u2|inverseBlockConstraints.y1|inverseBlockConstraints.y2|loopBreaker.L|loopBreaker.T_out|loopBreaker.T_out_fixed|loopBreaker.XiSpec|loopBreaker.assertionLevel|loopBreaker.dh|loopBreaker.dm_flow|loopBreaker.dp|loopBreaker.h_out|loopBreaker.h_out_fixed|loopBreaker.inlet.m_flow|loopBreaker.inlet.r|loopBreaker.inlet.state.T|loopBreaker.inlet.state.d|loopBreaker.inlet.state.h|loopBreaker.inlet.state.p|loopBreaker.inlet.state.phase|loopBreaker.m_flowSpec|loopBreaker.m_flow_in|loopBreaker.m_flow_in_par|loopBreaker.m_flow_in_prescribed|der.loopBreaker.outlet.m_flow.|loopBreaker.outlet.m_flow|loopBreaker.outlet.r|loopBreaker.outlet.state.T|loopBreaker.outlet.state.d|loopBreaker.outlet.state.h|loopBreaker.outlet.state.p|loopBreaker.outlet.state.phase|loopBreaker.pSpec|loopBreaker.p_out|loopBreaker.p_out_fixed|loopBreaker.thermalSpec|loopBreaker.thermalValueSpec|loopBreaker.tol_Xi|loopBreaker.tol_h|loopBreaker.tol_m_flow|loopBreaker.tol_p|massFlowRate.height|massFlowRate.offset|massFlowRate.startTime|massFlowRate.y|outletPressure.duration|outletPressure.height|outletPressure.offset|outletPressure.startTime|outletPressure.y|preheater.L|preheater.P|preheater.Q_flow|preheater.T_out_fixed|preheater.assertionLevel|preheater.clip_p_out|preheater.dT|preheater.dT_fixed|preheater.dh|preheater.dh_fixed|preheater.dp|preheater.dr_corr|preheater.du|preheater.h_in|preheater.h_out|preheater.h_out_fixed|preheater.initM_flow|der.preheater.inlet.m_flow.|preheater.inlet.m_flow|preheater.inlet.r|preheater.inlet.state.T|preheater.inlet.state.d|preheater.inlet.state.h|preheater.inlet.state.p|preheater.inlet.state.phase|preheater.m_acceleration_0|preheater.m_flow|preheater.m_flowStateSelect|preheater.m_flow_0|preheater.outlet.m_flow|preheater.outlet.r|preheater.outlet.state.T|preheater.outlet.state.d|preheater.outlet.state.h|preheater.outlet.state.p|preheater.outlet.state.phase|preheater.outletSpec|preheater.outletSpec_actual|preheater.outletSpec_prescribed|preheater.outletValueSpec|preheater.p|preheater.p_in|preheater.p_inf|preheater.p_min|preheater.p_out|preheater.q|preheater.rho_in|preheater.rho_out|preheater.singularityRegime|preheater.systemSpec|preheater.u_in|preheater.u_out|preheater.v_in|preheater.v_out|preheater.w_amb|preheater.w_exp|preheater.w_exp_net|pump.L|pump.P|pump.P_nom|pump.TC|pump.adiabaticModel.eta_is|pump.adiabaticModel.h_in|pump.adiabaticModel.h_out|pump.adiabaticModel.h_out_is|pump.adiabaticModel.p_out|pump.adiabaticModel.s_in|pump.adiabaticModel.state_in.T|pump.adiabaticModel.state_in.d|pump.adiabaticModel.state_in.h|pump.adiabaticModel.state_in.p|pump.adiabaticModel.state_in.phase|pump.adiabaticModel.w_t|pump.adiabaticModel.w_t_is|pump.assertionLevel|pump.clip_p_out|pump.dh|pump.dp|pump.dp_fixed|pump.dp_nom|pump.dp_start|pump.dr_corr|pump.etaSpec|pump.eta_actual|pump.eta_fixed|pump.eta_is|pump.h_in|pump.h_out|pump.initM_flow|der.pump.inlet.m_flow.|pump.inlet.m_flow|pump.inlet.r|pump.inlet.state.T|pump.inlet.state.d|pump.inlet.state.h|pump.inlet.state.p|pump.inlet.state.phase|pump.m_acceleration_0|pump.m_flow|pump.m_flowStateSelect|pump.m_flow_0|pump.outlet.m_flow|pump.outlet.r|pump.outlet.state.T|pump.outlet.state.d|pump.outlet.state.h|pump.outlet.state.p|pump.outlet.state.phase|pump.outletSpec|pump.outletSpec_actual|pump.outletSpec_prescribed|pump.outletValueSpec|pump.pRatio|pump.pRatio_fixed|pump.p_in|pump.p_min|pump.p_out|pump.p_out_fixed|pump.singularityRegime|superheater.L|superheater.P|superheater.Q_flow|superheater.T_out_fixed|superheater.assertionLevel|superheater.clip_p_out|superheater.dT|superheater.dT_fixed|superheater.dh|superheater.dh_fixed|superheater.dp|superheater.dr_corr|superheater.du|superheater.h_in|superheater.h_out|superheater.h_out_fixed|superheater.initM_flow|der.superheater.inlet.m_flow.|superheater.inlet.m_flow|superheater.inlet.r|superheater.inlet.state.T|superheater.inlet.state.d|superheater.inlet.state.h|superheater.inlet.state.p|superheater.inlet.state.phase|superheater.m_acceleration_0|superheater.m_flow|superheater.m_flowStateSelect|superheater.m_flow_0|superheater.outlet.m_flow|superheater.outlet.r|superheater.outlet.state.T|superheater.outlet.state.d|superheater.outlet.state.h|superheater.outlet.state.p|superheater.outlet.state.phase|superheater.outletSpec|superheater.outletSpec_actual|superheater.outletSpec_prescribed|superheater.outletValueSpec|superheater.p|superheater.p_in|superheater.p_inf|superheater.p_min|superheater.p_out|superheater.q|superheater.rho_in|superheater.rho_out|superheater.singularityRegime|superheater.systemSpec|superheater.u_in|superheater.u_out|superheater.v_in|superheater.v_out|superheater.w_amb|superheater.w_exp|superheater.w_exp_net|turbine.L|turbine.P|turbine.P_nom|turbine.TC|turbine.adiabaticModel.eta_is|turbine.adiabaticModel.h_in|turbine.adiabaticModel.h_out|turbine.adiabaticModel.h_out_is|turbine.adiabaticModel.p_out|turbine.adiabaticModel.s_in|turbine.adiabaticModel.state_in.T|turbine.adiabaticModel.state_in.d|turbine.adiabaticModel.state_in.h|turbine.adiabaticModel.state_in.p|turbine.adiabaticModel.state_in.phase|turbine.adiabaticModel.w_t|turbine.adiabaticModel.w_t_is|turbine.assertionLevel|turbine.clip_p_out|turbine.dh|turbine.dp|turbine.dp_fixed|turbine.dp_nom|turbine.dp_start|turbine.dr_corr|turbine.etaSpec|turbine.eta_actual|turbine.eta_fixed|turbine.eta_is|turbine.h_in|turbine.h_out|turbine.initM_flow|der.turbine.inlet.m_flow.|turbine.inlet.m_flow|turbine.inlet.r|turbine.inlet.state.T|turbine.inlet.state.d|turbine.inlet.state.h|turbine.inlet.state.p|turbine.inlet.state.phase|turbine.m_acceleration_0|turbine.m_flow|turbine.m_flowStateSelect|turbine.m_flow_0|turbine.outlet.m_flow|turbine.outlet.r|turbine.outlet.state.T|turbine.outlet.state.d|turbine.outlet.state.h|turbine.outlet.state.p|turbine.outlet.state.phase|turbine.outletSpec|turbine.outletSpec_actual|turbine.outletValueSpec|turbine.pRatio|turbine.pRatio_fixed|turbine.p_in|turbine.p_min|turbine.p_out|turbine.p_out_fixed|turbine.singularityRegime|vaporQualitySensor.TC|vaporQualitySensor.digits|vaporQualitySensor.direct_value|vaporQualitySensor.init|vaporQualitySensor.inlet.m_flow|vaporQualitySensor.inlet.r|vaporQualitySensor.inlet.state.T|vaporQualitySensor.inlet.state.d|vaporQualitySensor.inlet.state.h|vaporQualitySensor.inlet.state.p|vaporQualitySensor.inlet.state.phase|vaporQualitySensor.quantity|vaporQualitySensor.value|vaporQualitySensor.value_0|vaporQualitySensor.value_out|vaporQualitySetpoint.y",fileNamePrefix="ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion") [Timeout 660]
"Notification: Performance of FrontEnd - loaded program: time 9.82e-07/9.82e-07, allocations: 0 / 483.7 MB, free: 8.227 MB / 410.7 MB
Notification: Performance of FrontEnd - Absyn->SCode: time 1.14e-05/1.238e-05, allocations: 2.312 kB / 483.7 MB, free: 8.223 MB / 410.7 MB
Notification: Performance of NFInst.instantiate(ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion): time 0.04054/0.04056, allocations: 65.77 MB / 0.5366 GB, free: 15.05 MB / 474.7 MB
Notification: Performance of NFInst.instExpressions: time 0.02093/0.06148, allocations: 27.45 MB / 0.5634 GB, free: 3.512 MB / 490.7 MB
Notification: Performance of NFInst.updateImplicitVariability: time 0.00094/0.06242, allocations: 67.38 kB / 0.5635 GB, free: 3.445 MB / 490.7 MB
Notification: Performance of NFTyping.typeComponents: time 0.001317/0.06374, allocations: 0.7018 MB / 0.5642 GB, free: 2.738 MB / 490.7 MB
Notification: Performance of NFTyping.typeBindings: time 0.01306/0.0768, allocations: 7.798 MB / 0.5718 GB, free: 10.91 MB / 0.4948 GB
Notification: Performance of NFTyping.typeClassSections: time 0.003617/0.08042, allocations: 2.088 MB / 0.5738 GB, free: 8.809 MB / 0.4948 GB
Notification: Performance of NFFlatten.flatten: time 0.001741/0.08216, allocations: 2.218 MB / 0.576 GB, free: 6.578 MB / 0.4948 GB
Notification: Performance of NFFlatten.resolveConnections: time 0.0003428/0.0825, allocations: 245.2 kB / 0.5762 GB, free: 6.309 MB / 0.4948 GB
Notification: Performance of NFEvalConstants.evaluate: time 0.0109/0.0934, allocations: 9.2 MB / 0.5852 GB, free: 12.97 MB / 0.5105 GB
Notification: Performance of NFSimplifyModel.simplify: time 0.0005791/0.09398, allocations: 0.5762 MB / 0.5858 GB, free: 12.39 MB / 0.5105 GB
Notification: Performance of NFPackage.collectConstants: time 0.0001134/0.0941, allocations: 92 kB / 0.5859 GB, free: 12.3 MB / 0.5105 GB
Notification: Performance of NFFlatten.collectFunctions: time 0.0127/0.1068, allocations: 10.77 MB / 0.5964 GB, free: 1.52 MB / 0.5105 GB
Notification: Performance of NFScalarize.scalarize: time 0.0001686/0.107, allocations: 270.5 kB / 0.5966 GB, free: 1.254 MB / 0.5105 GB
Notification: Performance of NFVerifyModel.verify: time 0.000391/0.1074, allocations: 0.4947 MB / 0.5971 GB, free: 0.7578 MB / 0.5105 GB
Notification: Performance of NFConvertDAE.convert: time 0.01103/0.1184, allocations: 9.902 MB / 0.6068 GB, free: 6.832 MB / 0.5261 GB
Notification: Performance of FrontEnd - DAE generated: time 7.444e-06/0.1184, allocations: 4 kB / 0.6068 GB, free: 6.828 MB / 0.5261 GB
Notification: Performance of FrontEnd: time 1.883e-06/0.1184, allocations: 0 / 0.6068 GB, free: 6.828 MB / 0.5261 GB
Notification: Performance of Transformations before backend: time 4.704e-05/0.1184, allocations: 0 / 0.6068 GB, free: 6.828 MB / 0.5261 GB
Notification: Model statistics after passing the front-end and creating the data structures used by the back-end:
 * Number of equations: 304
 * Number of variables: 304
Notification: Performance of Generate backend data structure: time 0.004495/0.1229, allocations: 2.777 MB / 0.6095 GB, free: 4.004 MB / 0.5261 GB
Notification: Performance of prepare preOptimizeDAE: time 3.883e-05/0.123, allocations: 8.031 kB / 0.6095 GB, free: 3.996 MB / 0.5261 GB
Notification: Performance of preOpt normalInlineFunction (simulation): time 0.001418/0.1244, allocations: 0.6277 MB / 0.6101 GB, free: 3.367 MB / 0.5261 GB
Notification: Performance of preOpt evaluateParameters (simulation): time 0.001105/0.1255, allocations: 0.9225 MB / 0.611 GB, free: 2.391 MB / 0.5261 GB
Notification: Performance of preOpt simplifyIfEquations (simulation): time 0.0001269/0.1256, allocations: 193.8 kB / 0.6112 GB, free: 2.176 MB / 0.5261 GB
Notification: Performance of preOpt expandDerOperator (simulation): time 0.0001052/0.1257, allocations: 124.3 kB / 0.6113 GB, free: 2.055 MB / 0.5261 GB
Notification: Performance of preOpt clockPartitioning (simulation): time 0.001719/0.1275, allocations: 1.499 MB / 0.6128 GB, free: 424 kB / 0.5261 GB
Notification: Performance of preOpt findStateOrder (simulation): time 1.93e-05/0.1275, allocations: 0 / 0.6128 GB, free: 424 kB / 0.5261 GB
Notification: Performance of preOpt replaceEdgeChange (simulation): time 5.998e-05/0.1275, allocations: 52 kB / 0.6128 GB, free: 372 kB / 0.5261 GB
Notification: Performance of preOpt inlineArrayEqn (simulation): time 1.842e-05/0.1276, allocations: 32 kB / 0.6129 GB, free: 340 kB / 0.5261 GB
Notification: Performance of preOpt removeEqualRHS (simulation): time 0.001489/0.129, allocations: 1.011 MB / 0.6139 GB, free: 15.31 MB / 0.5417 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 0.00386/0.1329, allocations: 4.88 MB / 0.6186 GB, free: 10.29 MB / 0.5417 GB
Notification: Performance of preOpt comSubExp (simulation): time 0.001308/0.1342, allocations: 0.8645 MB / 0.6195 GB, free: 9.418 MB / 0.5417 GB
Notification: Performance of preOpt resolveLoops (simulation): time 0.0004188/0.1346, allocations: 370.6 kB / 0.6198 GB, free: 9.055 MB / 0.5417 GB
Notification: Performance of preOpt evalFunc (simulation): time 0.211/0.3456, allocations: 36.45 MB / 0.6554 GB, free: 162.7 MB / 0.5573 GB
Notification: Performance of preOpt encapsulateWhenConditions (simulation): time 3.589e-05/0.3457, allocations: 44.19 kB / 0.6555 GB, free: 162.7 MB / 0.5573 GB
Notification: Performance of pre-optimization done (n=85): time 2.926e-06/0.3457, allocations: 0 / 0.6555 GB, free: 162.7 MB / 0.5573 GB
Notification: Performance of matching and sorting (n=85): time 0.002719/0.3484, allocations: 1.49 MB / 0.6569 GB, free: 162.2 MB / 0.5573 GB
Notification: Performance of inlineWhenForInitialization (initialization): time 2.139e-05/0.3484, allocations: 86.55 kB / 0.657 GB, free: 162.2 MB / 0.5573 GB
Notification: Performance of selectInitializationVariablesDAE (initialization): time 0.0006999/0.3491, allocations: 0.8407 MB / 0.6578 GB, free: 161.8 MB / 0.5573 GB
Notification: Performance of collectPreVariables (initialization): time 2.759e-05/0.3491, allocations: 37.14 kB / 0.6579 GB, free: 161.8 MB / 0.5573 GB
Notification: Performance of collectInitialEqns (initialization): time 0.0002397/0.3494, allocations: 0.6545 MB / 0.6585 GB, free: 161.4 MB / 0.5573 GB
Notification: Performance of collectInitialBindings (initialization): time 0.0001121/0.3495, allocations: 307.8 kB / 0.6588 GB, free: 161.2 MB / 0.5573 GB
Notification: Performance of simplifyInitialFunctions (initialization): time 0.0001499/0.3496, allocations: 189.2 kB / 0.659 GB, free: 161.1 MB / 0.5573 GB
Notification: Performance of setup shared object (initialization): time 4.415e-05/0.3497, allocations: 347.6 kB / 0.6593 GB, free: 160.8 MB / 0.5573 GB
Notification: Performance of preBalanceInitialSystem (initialization): time 0.0003106/0.35, allocations: 244.9 kB / 0.6595 GB, free: 160.7 MB / 0.5573 GB
Notification: Performance of partitionIndependentBlocks (initialization): time 0.0003874/0.3504, allocations: 0.5665 MB / 0.6601 GB, free: 160.2 MB / 0.5573 GB
Notification: Performance of analyzeInitialSystem (initialization): time 0.0007437/0.3511, allocations: 0.8675 MB / 0.6609 GB, free: 159.6 MB / 0.5573 GB
Notification: Performance of solveInitialSystemEqSystem (initialization): time 6.031e-06/0.3511, allocations: 3.719 kB / 0.6609 GB, free: 159.6 MB / 0.5573 GB
Notification: Performance of matching and sorting (n=126) (initialization): time 0.00107/0.3522, allocations: 1.054 MB / 0.662 GB, free: 159.1 MB / 0.5573 GB
Notification: Performance of prepare postOptimizeDAE: time 1.999e-05/0.3522, allocations: 9.625 kB / 0.662 GB, free: 159.1 MB / 0.5573 GB
Notification: Performance of postOpt simplifyComplexFunction (initialization): time 1.113e-05/0.3522, allocations: 8.812 kB / 0.662 GB, free: 159.1 MB / 0.5573 GB
Notification: Performance of postOpt tearingSystem (initialization): time 0.0005171/0.3528, allocations: 142 kB / 0.6621 GB, free: 159.1 MB / 0.5573 GB
Notification: Performance of postOpt solveSimpleEquations (initialization): time 0.0004431/0.3532, allocations: 223.3 kB / 0.6623 GB, free: 159.1 MB / 0.5573 GB
Notification: Performance of postOpt calculateStrongComponentJacobians (initialization): time 0.0004358/0.3536, allocations: 1.729 MB / 0.664 GB, free: 157.4 MB / 0.5573 GB
Notification: Performance of postOpt simplifyAllExpressions (initialization): time 0.0003448/0.354, allocations: 104.3 kB / 0.6641 GB, free: 157.4 MB / 0.5573 GB
Notification: Performance of postOpt collapseArrayExpressions (initialization): time 5.019e-05/0.354, allocations: 45.27 kB / 0.6642 GB, free: 157.3 MB / 0.5573 GB
Notification: Model statistics after passing the back-end for initialization:
 * Number of independent subsystems: 42
 * Number of states: 0 ()
 * Number of discrete variables: 7 (superheater.outlet.state.phase,loopBreaker.outlet.state.phase,turbine.outlet.state.phase,condenser.outlet.state.phase,preheater.outlet.state.phase,boiler.outlet.state.phase,pump.outlet.state.phase)
 * Number of discrete states: 0 ()
 * Number of clocked states: 0 ()
 * Top-level inputs: 0
Notification: Strong component statistics for initialization (120):
 * Single equations (assignments): 117
 * Array equations: 0
 * Algorithm blocks: 0
 * Record equations: 0
 * When equations: 0
 * If-equations: 0
 * Equation systems (not torn): 1
 * Torn equation systems: 2
 * Mixed (continuous/discrete) equation systems: 0
Notification: Equation system details (not torn):
 * Constant Jacobian (size): 0 systems
 * Linear Jacobian (size,density): 0 systems
 * Non-linear Jacobian (size): 1 system
   {1}
 * Without analytic Jacobian (size): 0 systems
Notification: Torn system details for strict tearing set:
 * Linear torn systems (#iteration vars, #inner vars, density): 0 systems
 * Non-linear torn systems (#iteration vars, #inner vars): 2 systems
   {(1,4), (1,2)}
Notification: Performance of prepare postOptimizeDAE: time 0.000269/0.3543, allocations: 271.2 kB / 0.6644 GB, free: 157.1 MB / 0.5573 GB
Notification: Performance of postOpt lateInlineFunction (simulation): time 0.0001144/0.3544, allocations: 156.5 kB / 0.6646 GB, free: 157.1 MB / 0.5573 GB
Notification: Performance of postOpt wrapFunctionCalls (simulation): time 0.00218/0.3566, allocations: 3.08 MB / 0.6676 GB, free: 155.7 MB / 0.5573 GB
Notification: Performance of postOpt simplifysemiLinear (simulation): time 8.736e-06/0.3566, allocations: 6.094 kB / 0.6676 GB, free: 155.7 MB / 0.5573 GB
Notification: Performance of postOpt simplifyComplexFunction (simulation): time 4.028e-06/0.3566, allocations: 7.938 kB / 0.6676 GB, free: 155.7 MB / 0.5573 GB
Notification: Performance of postOpt removeConstants (simulation): time 0.0002417/0.3568, allocations: 239.3 kB / 0.6678 GB, free: 155.5 MB / 0.5573 GB
Notification: Performance of postOpt simplifyTimeIndepFuncCalls (simulation): time 7.453e-05/0.3569, allocations: 39.23 kB / 0.6679 GB, free: 155.5 MB / 0.5573 GB
Notification: Performance of postOpt simplifyAllExpressions (simulation): time 0.0002345/0.3572, allocations: 39.48 kB / 0.6679 GB, free: 155.5 MB / 0.5573 GB
Notification: Performance of postOpt findZeroCrossings (simulation): time 8.984e-05/0.3572, allocations: 59.73 kB / 0.6679 GB, free: 155.5 MB / 0.5573 GB
[/var/lib/jenkins/ws/OpenModelicaLibraryTestingWork/OpenModelica/OMCompiler/Compiler/BackEnd/DAEMode.mo:531:7-533:90:writable] Error: Internal error DAEMode.traverserStrongComponents failed on equation:
1/1 (1): condenser.T_in = $cse2.T
2/2 (1): 0.95 = ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion.vaporQualitySensor.getQuantity(ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion.vaporQualitySensor.inlet.Medium.ThermodynamicState(0, condenser.h_in, condenser.rho_in, condenser.T_in, turbine.p_out_fixed), vaporQualitySensor.quantity)
3/3 (1): condenser.rho_in = $cse2.rho
4/4 (16): $cse2 = ThermofluidStream.Media.myMedia.Water.IF97_Utilities.waterBaseProp_ph(turbine.p_out_fixed, condenser.h_in, 0, 0)

Variables:
1: $cse2.cv:VARIABLE(protected = true )  type: Real unreplaceable
2: $cse2.dpT:VARIABLE(protected = true )  type: Real unreplaceable
3: $cse2.s:VARIABLE(protected = true )  type: Real unreplaceable
4: $cse2.pd:VARIABLE(protected = true )  type: Real unreplaceable
5: $cse2.phase:DISCRETE(protected = true )  type: Integer unreplaceable
6: $cse2.R_s:VARIABLE(protected = true )  type: Real unreplaceable
7: $cse2.vp:VARIABLE(protected = true )  type: Real unreplaceable
8: $cse2.x:VARIABLE(protected = true )  type: Real unreplaceable
9: condenser.h_in:VARIABLE(min = -1e10 max = 1e10 start = 1e5 unit = \"J/kg\" nominal = 5e5 )  \"Inlet specific enthalpy\" type: Real
10: $cse2.cp:VARIABLE(protected = true )  type: Real unreplaceable
11: $cse2.p:VARIABLE(protected = true )  type: Real unreplaceable
12: $cse2.vt:VARIABLE(protected = true )  type: Real unreplaceable
13: $cse2.region:DISCRETE(protected = true )  type: Integer unreplaceable
14: $cse2.pt:VARIABLE(protected = true )  type: Real unreplaceable
15: $cse2.h:VARIABLE(protected = true )  type: Real unreplaceable
16: $cse2.rho:VARIABLE(protected = true )  type: Real unreplaceable
17: $cse2.T:VARIABLE(protected = true )  type: Real unreplaceable
18: condenser.rho_in:VARIABLE(min = 0.0 max = 1e5 start = 150.0 unit = \"kg/m3\" nominal = 500.0 )  \"Inlet density\" type: Real
19: condenser.T_in:VARIABLE(min = 273.15 max = 2273.15 start = 500.0 unit = \"K\" nominal = 500.0 )  \"Inlet state temperature\" type: Real
[/var/lib/jenkins/ws/OpenModelicaLibraryTestingWork/OpenModelica/OMCompiler/Compiler/BackEnd/BackendDAEUtil.mo:9780:5-9781:77:writable] Error: Internal error BackendDAEUtil.traverseEqSystemStrongComponents failed with function:
omc_DAEMode_traverserStrongComponents
Notification: Performance of <failed> postOpt createDAEmodeBDAE (simulation): time 0.0007221/0.358, allocations: 363.2 kB / 0.6683 GB, free: 155.3 MB / 0.5573 GB
Error: post-optimization module createDAEmodeBDAE (simulation) failed.
Error: Internal error SimCode DAEmode: The model ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion could not be translated
"
[Timeout remaining time 660]
[Calling sys.exit(0), Time elapsed: 2.4823032850399613]