Running: ./testmodel.py --libraries=/home/hudson/saved_omc/libraries/.openmodelica/libraries --ompython_omhome=/usr ThermofluidStream_dev_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 0.0007923/0.0007923, allocations: 80.25 kB / 20.03 MB, free: 4.484 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 0.0007895/0.0007895, allocations: 174 kB / 23.35 MB, free: 1.172 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 0.8836/0.8836, allocations: 177.1 MB / 203.7 MB, free: 5.707 MB / 186.7 MB
"
[Timeout remaining time 179]
loadFile("/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermofluidStream main/package.mo", uses=false) [Timeout 180]
"Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermofluidStream main/package.mo): time 0.6277/0.6277, allocations: 116 MB / 376.1 MB, free: 4.188 MB / 346.7 MB
"
[Timeout remaining time 179]
Using package ThermofluidStream with version 1.3.0 (/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermofluidStream main/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_dev_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_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion") [Timeout 660]
"Notification: Performance of FrontEnd - loaded program: time 3.116e-06/3.116e-06, allocations: 0 / 0.5548 GB, free: 12.68 MB / 490.7 MB
Notification: Performance of FrontEnd - Absyn->SCode: time 4.396e-05/4.708e-05, allocations: 6.25 kB / 0.5548 GB, free: 12.68 MB / 490.7 MB
Notification: Performance of NFInst.instantiate(ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion): time 0.04587/0.04592, allocations: 65.72 MB / 0.619 GB, free: 10.73 MB / 0.5417 GB
Notification: Performance of NFInst.instExpressions: time 0.2966/0.3425, allocations: 27.42 MB / 0.6457 GB, free: 11.34 MB / 0.5573 GB
Notification: Performance of NFInst.updateImplicitVariability: time 0.001348/0.3438, allocations: 54.94 kB / 0.6458 GB, free: 11.34 MB / 0.5573 GB
Notification: Performance of NFTyping.typeComponents: time 0.001551/0.3454, allocations: 0.6957 MB / 0.6465 GB, free: 11.34 MB / 0.5573 GB
Notification: Performance of NFTyping.typeBindings: time 0.01667/0.362, allocations: 7.798 MB / 0.6541 GB, free: 10.81 MB / 0.5573 GB
Notification: Performance of NFTyping.typeClassSections: time 0.00461/0.3667, allocations: 2.078 MB / 0.6561 GB, free: 10.54 MB / 0.5573 GB
Notification: Performance of NFFlatten.flatten: time 0.002616/0.3693, allocations: 2.198 MB / 0.6582 GB, free: 9.828 MB / 0.5573 GB
Notification: Performance of NFFlatten.resolveConnections: time 0.0004024/0.3697, allocations: 245 kB / 0.6585 GB, free: 9.754 MB / 0.5573 GB
Notification: Performance of NFEvalConstants.evaluate: time 0.01042/0.3801, allocations: 9.183 MB / 0.6674 GB, free: 7.23 MB / 0.5573 GB
Notification: Performance of NFSimplifyModel.simplify: time 0.001038/0.3811, allocations: 0.5641 MB / 0.668 GB, free: 7.152 MB / 0.5573 GB
Notification: Performance of NFPackage.collectConstants: time 0.000121/0.3813, allocations: 94.53 kB / 0.6681 GB, free: 7.152 MB / 0.5573 GB
Notification: Performance of NFFlatten.collectFunctions: time 0.01775/0.399, allocations: 10.78 MB / 0.6786 GB, free: 6.977 MB / 0.5573 GB
Notification: Performance of NFScalarize.scalarize: time 0.0003608/0.3994, allocations: 266.3 kB / 0.6789 GB, free: 6.902 MB / 0.5573 GB
Notification: Performance of NFVerifyModel.verify: time 0.0007959/0.4002, allocations: 0.4907 MB / 0.6793 GB, free: 6.828 MB / 0.5573 GB
Notification: Performance of NFConvertDAE.convert: time 0.01738/0.4175, allocations: 9.871 MB / 0.689 GB, free: 3.637 MB / 0.5573 GB
Notification: Performance of FrontEnd - DAE generated: time 5.069e-06/0.4175, allocations: 2.688 kB / 0.689 GB, free: 3.637 MB / 0.5573 GB
Notification: Performance of FrontEnd: time 1.824e-06/0.4175, allocations: 0 / 0.689 GB, free: 3.637 MB / 0.5573 GB
Notification: Performance of Transformations before backend: time 2.376e-05/0.4176, allocations: 0 / 0.689 GB, free: 3.637 MB / 0.5573 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 0.004952/0.4225, allocations: 2.744 MB / 0.6917 GB, free: 2.027 MB / 0.5573 GB
Notification: Performance of prepare preOptimizeDAE: time 4.695e-05/0.4226, allocations: 8.25 kB / 0.6917 GB, free: 2.027 MB / 0.5573 GB
Notification: Performance of preOpt normalInlineFunction (simulation): time 0.001025/0.4236, allocations: 369.9 kB / 0.692 GB, free: 1.883 MB / 0.5573 GB
Notification: Performance of preOpt evaluateParameters (simulation): time 0.0009908/0.4246, allocations: 0.8453 MB / 0.6929 GB, free: 1.457 MB / 0.5573 GB
Notification: Performance of preOpt simplifyIfEquations (simulation): time 0.0001004/0.4247, allocations: 202.8 kB / 0.693 GB, free: 1.32 MB / 0.5573 GB
Notification: Performance of preOpt expandDerOperator (simulation): time 9.796e-05/0.4248, allocations: 118.9 kB / 0.6932 GB, free: 1.32 MB / 0.5573 GB
Notification: Performance of preOpt clockPartitioning (simulation): time 0.001505/0.4263, allocations: 1.486 MB / 0.6946 GB, free: 0.6445 MB / 0.5573 GB
Notification: Performance of preOpt findStateOrder (simulation): time 2.067e-05/0.4263, allocations: 6.812 kB / 0.6946 GB, free: 0.6445 MB / 0.5573 GB
Notification: Performance of preOpt replaceEdgeChange (simulation): time 5.866e-05/0.4264, allocations: 49.66 kB / 0.6947 GB, free: 0.6445 MB / 0.5573 GB
Notification: Performance of preOpt inlineArrayEqn (simulation): time 1.587e-05/0.4264, allocations: 31.67 kB / 0.6947 GB, free: 0.6445 MB / 0.5573 GB
Notification: Performance of preOpt removeEqualRHS (simulation): time 0.001242/0.4276, allocations: 1.024 MB / 0.6957 GB, free: 476 kB / 0.5573 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 0.003725/0.4313, allocations: 4.848 MB / 0.7004 GB, free: 13.12 MB / 0.573 GB
Notification: Performance of preOpt comSubExp (simulation): time 0.001151/0.4325, allocations: 0.8332 MB / 0.7012 GB, free: 12.68 MB / 0.573 GB
Notification: Performance of preOpt resolveLoops (simulation): time 0.000394/0.4329, allocations: 371.1 kB / 0.7016 GB, free: 12.52 MB / 0.573 GB
Notification: Performance of preOpt evalFunc (simulation): time 0.06175/0.4946, allocations: 36.51 MB / 0.7373 GB, free: 14.05 MB / 0.6042 GB
Notification: Performance of preOpt encapsulateWhenConditions (simulation): time 4.857e-05/0.4947, allocations: 39.56 kB / 0.7373 GB, free: 14 MB / 0.6042 GB
Notification: Performance of pre-optimization done (n=85): time 2.735e-06/0.4947, allocations: 0 / 0.7373 GB, free: 14 MB / 0.6042 GB
Notification: Performance of matching and sorting (n=85): time 0.002894/0.4976, allocations: 1.39 MB / 0.7387 GB, free: 12.62 MB / 0.6042 GB
Notification: Performance of inlineWhenForInitialization (initialization): time 3.693e-05/0.4976, allocations: 86.11 kB / 0.7387 GB, free: 12.52 MB / 0.6042 GB
Notification: Performance of selectInitializationVariablesDAE (initialization): time 0.0006971/0.4983, allocations: 0.799 MB / 0.7395 GB, free: 11.7 MB / 0.6042 GB
Notification: Performance of collectPreVariables (initialization): time 3.805e-05/0.4984, allocations: 41.7 kB / 0.7396 GB, free: 11.66 MB / 0.6042 GB
Notification: Performance of collectInitialEqns (initialization): time 0.0003031/0.4987, allocations: 0.6337 MB / 0.7402 GB, free: 11.02 MB / 0.6042 GB
Notification: Performance of collectInitialBindings (initialization): time 0.0001622/0.4988, allocations: 308.9 kB / 0.7405 GB, free: 10.72 MB / 0.6042 GB
Notification: Performance of simplifyInitialFunctions (initialization): time 0.0001632/0.499, allocations: 189.9 kB / 0.7406 GB, free: 10.54 MB / 0.6042 GB
Notification: Performance of setup shared object (initialization): time 9.196e-05/0.4991, allocations: 345.9 kB / 0.741 GB, free: 10.19 MB / 0.6042 GB
Notification: Performance of preBalanceInitialSystem (initialization): time 0.0003117/0.4994, allocations: 253.9 kB / 0.7412 GB, free: 9.941 MB / 0.6042 GB
Notification: Performance of partitionIndependentBlocks (initialization): time 0.000439/0.4998, allocations: 0.5702 MB / 0.7418 GB, free: 9.234 MB / 0.6042 GB
Notification: Performance of analyzeInitialSystem (initialization): time 0.0008219/0.5006, allocations: 0.8621 MB / 0.7426 GB, free: 8.281 MB / 0.6042 GB
Notification: Performance of solveInitialSystemEqSystem (initialization): time 4.99e-06/0.5007, allocations: 0 / 0.7426 GB, free: 8.281 MB / 0.6042 GB
Notification: Performance of matching and sorting (n=126) (initialization): time 0.001077/0.5017, allocations: 0.9992 MB / 0.7436 GB, free: 7.328 MB / 0.6042 GB
Notification: Performance of prepare postOptimizeDAE: time 2.068e-05/0.5017, allocations: 12.22 kB / 0.7436 GB, free: 7.316 MB / 0.6042 GB
Notification: Performance of postOpt simplifyComplexFunction (initialization): time 1.108e-05/0.5018, allocations: 12 kB / 0.7436 GB, free: 7.305 MB / 0.6042 GB
Notification: Performance of postOpt tearingSystem (initialization): time 0.0005118/0.5023, allocations: 140.5 kB / 0.7438 GB, free: 7.164 MB / 0.6042 GB
Notification: Performance of postOpt solveSimpleEquations (initialization): time 0.000407/0.5027, allocations: 220.7 kB / 0.744 GB, free: 6.961 MB / 0.6042 GB
Notification: Performance of postOpt calculateStrongComponentJacobians (initialization): time 0.0009564/0.5036, allocations: 1.726 MB / 0.7456 GB, free: 5.172 MB / 0.6042 GB
Notification: Performance of postOpt simplifyAllExpressions (initialization): time 0.0004152/0.504, allocations: 103.6 kB / 0.7457 GB, free: 5.07 MB / 0.6042 GB
Notification: Performance of postOpt collapseArrayExpressions (initialization): time 4.421e-05/0.5041, allocations: 51.92 kB / 0.7458 GB, free: 5.02 MB / 0.6042 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 0.000359/0.5045, allocations: 273.8 kB / 0.7461 GB, free: 4.762 MB / 0.6042 GB
Notification: Performance of postOpt lateInlineFunction (simulation): time 9.875e-05/0.5046, allocations: 119.2 kB / 0.7462 GB, free: 4.645 MB / 0.6042 GB
Notification: Performance of postOpt wrapFunctionCalls (simulation): time 0.002248/0.5068, allocations: 3.076 MB / 0.7492 GB, free: 1.582 MB / 0.6042 GB
Notification: Performance of postOpt simplifysemiLinear (simulation): time 7.494e-06/0.5068, allocations: 3.984 kB / 0.7492 GB, free: 1.578 MB / 0.6042 GB
Notification: Performance of postOpt simplifyComplexFunction (simulation): time 7.323e-06/0.5068, allocations: 7.922 kB / 0.7492 GB, free: 1.57 MB / 0.6042 GB
Notification: Performance of postOpt removeConstants (simulation): time 0.0003074/0.5071, allocations: 234.3 kB / 0.7494 GB, free: 1.34 MB / 0.6042 GB
Notification: Performance of postOpt simplifyTimeIndepFuncCalls (simulation): time 7.729e-05/0.5072, allocations: 28.39 kB / 0.7494 GB, free: 1.312 MB / 0.6042 GB
Notification: Performance of postOpt simplifyAllExpressions (simulation): time 0.0002132/0.5074, allocations: 39.97 kB / 0.7495 GB, free: 1.273 MB / 0.6042 GB
Notification: Performance of postOpt findZeroCrossings (simulation): time 8.239e-05/0.5075, allocations: 60.45 kB / 0.7495 GB, free: 1.219 MB / 0.6042 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:9771:5-9772:77:writable] Error: Internal error BackendDAEUtil.traverseEqSystemStrongComponents failed with function:
omc_DAEMode_traverserStrongComponents
Notification: Performance of <failed> postOpt createDAEmodeBDAE (simulation): time 0.0007079/0.5082, allocations: 364 kB / 0.7499 GB, free: 0.8711 MB / 0.6042 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 659]
[Calling sys.exit(0), Time elapsed: 2.8975194161757827]
Failed to read output from testmodel.py, exit status != 0:
0.5161319319158792 0.5227176649999999 0.10335784999999995
Calling exit ...
<OMPython.OMCSessionZMQ object at 0x7aea65660fe0>