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 0.001914/0.001914, allocations: 101.5 kB / 18.95 MB, free: 1.184 MB / 13.93 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 0.002275/0.002275, allocations: 218.8 kB / 22.25 MB, free: 3.57 MB / 13.93 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 1.669/1.669, allocations: 230.6 MB / 256 MB, free: 9.621 MB / 202.7 MB " [Timeout remaining time 178] 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 1.2/1.2, allocations: 154.1 MB / 466.5 MB, free: 3.301 MB / 362.7 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 0.00276/0.00276, allocations: 83.88 kB / 0.6443 GB, free: 27.78 MB / 490.7 MB Notification: Performance of FrontEnd - Absyn->SCode: time 0.1534/0.1561, allocations: 88.77 MB / 0.731 GB, free: 2.816 MB / 0.5417 GB Notification: Performance of NFInst.instantiate(ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion): time 0.09241/0.2485, allocations: 66.29 MB / 0.7957 GB, free: 312 kB / 0.6042 GB Notification: Performance of NFInst.instExpressions: time 0.04406/0.2926, allocations: 27.5 MB / 0.8226 GB, free: 4.715 MB / 0.6355 GB Notification: Performance of NFInst.updateImplicitVariability: time 0.001695/0.2943, allocations: 63.38 kB / 0.8226 GB, free: 4.652 MB / 0.6355 GB Notification: Performance of NFTyping.typeComponents: time 0.002344/0.2966, allocations: 0.6866 MB / 0.8233 GB, free: 3.961 MB / 0.6355 GB Notification: Performance of NFTyping.typeBindings: time 0.3764/0.673, allocations: 7.668 MB / 0.8308 GB, free: 6.988 MB / 0.6355 GB Notification: Performance of NFTyping.typeClassSections: time 0.005471/0.6785, allocations: 2.049 MB / 0.8328 GB, free: 6.973 MB / 0.6355 GB Notification: Performance of NFFlatten.flatten: time 0.003122/0.6816, allocations: 2.119 MB / 0.8349 GB, free: 6.969 MB / 0.6355 GB Notification: Performance of NFFlatten.resolveConnections: time 0.0005598/0.6821, allocations: 246 kB / 0.8351 GB, free: 6.898 MB / 0.6355 GB Notification: Performance of NFEvalConstants.evaluate: time 0.02234/0.7045, allocations: 8.851 MB / 0.8437 GB, free: 4.523 MB / 0.6355 GB Notification: Performance of NFSimplifyModel.simplify: time 0.001723/0.7062, allocations: 0.6893 MB / 0.8444 GB, free: 4.523 MB / 0.6355 GB Notification: Performance of NFPackage.collectConstants: time 0.0003726/0.7066, allocations: 94.25 kB / 0.8445 GB, free: 4.523 MB / 0.6355 GB Notification: Performance of NFFlatten.collectFunctions: time 0.02186/0.7284, allocations: 10.76 MB / 0.855 GB, free: 4.477 MB / 0.6355 GB Notification: Performance of NFScalarize.scalarize: time 0.000489/0.7289, allocations: 261.2 kB / 0.8553 GB, free: 4.441 MB / 0.6355 GB Notification: Performance of NFVerifyModel.verify: time 0.00145/0.7304, allocations: 0.6077 MB / 0.8559 GB, free: 4.258 MB / 0.6355 GB Notification: Performance of NFConvertDAE.convert: time 0.01914/0.7495, allocations: 8.262 MB / 0.8639 GB, free: 3.648 MB / 0.6355 GB Notification: Performance of FrontEnd - DAE generated: time 6.612e-06/0.7495, allocations: 0 / 0.8639 GB, free: 3.648 MB / 0.6355 GB Notification: Performance of FrontEnd: time 1.864e-06/0.7495, allocations: 0 / 0.8639 GB, free: 3.648 MB / 0.6355 GB Notification: Performance of Transformations before backend: time 3.435e-05/0.7496, allocations: 0 / 0.8639 GB, free: 3.648 MB / 0.6355 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 0.006913/0.7565, allocations: 2.795 MB / 0.8666 GB, free: 2.297 MB / 0.6355 GB Notification: Performance of prepare preOptimizeDAE: time 3.932e-05/0.7565, allocations: 8.781 kB / 0.8667 GB, free: 2.297 MB / 0.6355 GB Notification: Performance of preOpt normalInlineFunction (simulation): time 0.001744/0.7582, allocations: 375.1 kB / 0.867 GB, free: 2.199 MB / 0.6355 GB Notification: Performance of preOpt evaluateParameters (simulation): time 0.001743/0.76, allocations: 0.8589 MB / 0.8679 GB, free: 1.852 MB / 0.6355 GB Notification: Performance of preOpt simplifyIfEquations (simulation): time 0.0001568/0.7601, allocations: 202.7 kB / 0.868 GB, free: 1.719 MB / 0.6355 GB Notification: Performance of preOpt expandDerOperator (simulation): time 0.0001566/0.7603, allocations: 122.3 kB / 0.8682 GB, free: 1.715 MB / 0.6355 GB Notification: Performance of preOpt clockPartitioning (simulation): time 0.002665/0.763, allocations: 1.488 MB / 0.8696 GB, free: 1.27 MB / 0.6355 GB Notification: Performance of preOpt findStateOrder (simulation): time 3.497e-05/0.763, allocations: 6.188 kB / 0.8696 GB, free: 1.27 MB / 0.6355 GB Notification: Performance of preOpt replaceEdgeChange (simulation): time 8.715e-05/0.7631, allocations: 48.69 kB / 0.8697 GB, free: 1.27 MB / 0.6355 GB Notification: Performance of preOpt inlineArrayEqn (simulation): time 2.044e-05/0.7631, allocations: 30.97 kB / 0.8697 GB, free: 1.27 MB / 0.6355 GB Notification: Performance of preOpt removeEqualRHS (simulation): time 0.002104/0.7652, allocations: 1.02 MB / 0.8707 GB, free: 1.09 MB / 0.6355 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 0.006938/0.7722, allocations: 4.823 MB / 0.8754 GB, free: 13.95 MB / 0.6511 GB Notification: Performance of preOpt comSubExp (simulation): time 0.002062/0.7742, allocations: 0.837 MB / 0.8762 GB, free: 13.8 MB / 0.6511 GB Notification: Performance of preOpt resolveLoops (simulation): time 0.0006237/0.7748, allocations: 373.1 kB / 0.8766 GB, free: 13.75 MB / 0.6511 GB Notification: Performance of preOpt evalFunc (simulation): time 0.1401/0.9149, allocations: 36.48 MB / 0.9122 GB, free: 3.445 MB / 0.6667 GB Notification: Performance of preOpt encapsulateWhenConditions (simulation): time 6.248e-05/0.915, allocations: 45.94 kB / 0.9122 GB, free: 3.402 MB / 0.6667 GB Notification: Performance of pre-optimization done (n=85): time 2.845e-06/0.915, allocations: 0 / 0.9122 GB, free: 3.402 MB / 0.6667 GB Notification: Performance of matching and sorting (n=85): time 0.004854/0.9198, allocations: 1.391 MB / 0.9136 GB, free: 2.328 MB / 0.6667 GB Notification: Performance of inlineWhenForInitialization (initialization): time 8.354e-05/0.9199, allocations: 93.98 kB / 0.9137 GB, free: 2.219 MB / 0.6667 GB Notification: Performance of selectInitializationVariablesDAE (initialization): time 0.001308/0.9212, allocations: 0.8451 MB / 0.9145 GB, free: 1.543 MB / 0.6667 GB Notification: Performance of collectPreVariables (initialization): time 9.231e-05/0.9213, allocations: 34.7 kB / 0.9146 GB, free: 1.512 MB / 0.6667 GB Notification: Performance of collectInitialEqns (initialization): time 0.0006183/0.9219, allocations: 0.6465 MB / 0.9152 GB, free: 0.9336 MB / 0.6667 GB Notification: Performance of collectInitialBindings (initialization): time 0.0003511/0.9223, allocations: 313.9 kB / 0.9155 GB, free: 0.6328 MB / 0.6667 GB Notification: Performance of simplifyInitialFunctions (initialization): time 0.0003095/0.9226, allocations: 194.5 kB / 0.9157 GB, free: 448 kB / 0.6667 GB Notification: Performance of setup shared object (initialization): time 0.0002129/0.9228, allocations: 341.9 kB / 0.916 GB, free: 100 kB / 0.6667 GB Notification: Performance of preBalanceInitialSystem (initialization): time 0.0006174/0.9234, allocations: 249.4 kB / 0.9162 GB, free: 15.86 MB / 0.6823 GB Notification: Performance of partitionIndependentBlocks (initialization): time 0.0009692/0.9244, allocations: 0.5726 MB / 0.9168 GB, free: 15.15 MB / 0.6823 GB Notification: Performance of analyzeInitialSystem (initialization): time 0.001609/0.926, allocations: 0.8616 MB / 0.9176 GB, free: 14.2 MB / 0.6823 GB Notification: Performance of solveInitialSystemEqSystem (initialization): time 9.719e-06/0.926, allocations: 4 kB / 0.9176 GB, free: 14.2 MB / 0.6823 GB Notification: Performance of matching and sorting (n=126) (initialization): time 0.00218/0.9282, allocations: 1.003 MB / 0.9186 GB, free: 13.23 MB / 0.6823 GB Notification: Performance of prepare postOptimizeDAE: time 2.438e-05/0.9282, allocations: 8 kB / 0.9186 GB, free: 13.23 MB / 0.6823 GB Notification: Performance of postOpt simplifyComplexFunction (initialization): time 1.885e-05/0.9282, allocations: 12.09 kB / 0.9186 GB, free: 13.21 MB / 0.6823 GB Notification: Performance of postOpt tearingSystem (initialization): time 0.0008534/0.9291, allocations: 145.5 kB / 0.9188 GB, free: 13.07 MB / 0.6823 GB Notification: Performance of postOpt solveSimpleEquations (initialization): time 0.0008674/0.93, allocations: 219.6 kB / 0.919 GB, free: 12.87 MB / 0.6823 GB Notification: Performance of postOpt calculateStrongComponentJacobians (initialization): time 0.001833/0.9318, allocations: 1.725 MB / 0.9207 GB, free: 11.08 MB / 0.6823 GB Notification: Performance of postOpt simplifyAllExpressions (initialization): time 0.000845/0.9326, allocations: 111.4 kB / 0.9208 GB, free: 10.97 MB / 0.6823 GB Notification: Performance of postOpt collapseArrayExpressions (initialization): time 9.868e-05/0.9327, allocations: 53.41 kB / 0.9208 GB, free: 10.92 MB / 0.6823 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 0.0005641/0.9333, allocations: 260.2 kB / 0.9211 GB, free: 10.67 MB / 0.6823 GB Notification: Performance of postOpt lateInlineFunction (simulation): time 0.0002598/0.9336, allocations: 127.1 kB / 0.9212 GB, free: 10.54 MB / 0.6823 GB Notification: Performance of postOpt wrapFunctionCalls (simulation): time 0.00451/0.9381, allocations: 3.07 MB / 0.9242 GB, free: 7.508 MB / 0.6823 GB Notification: Performance of postOpt inlineArrayEqn (simulation): time 5.546e-05/0.9381, allocations: 39.95 kB / 0.9242 GB, free: 7.469 MB / 0.6823 GB Notification: Performance of postOpt constantLinearSystem (simulation): time 1.214e-05/0.9381, allocations: 3.938 kB / 0.9242 GB, free: 7.465 MB / 0.6823 GB Notification: Performance of postOpt simplifysemiLinear (simulation): time 1.828e-05/0.9381, allocations: 7.969 kB / 0.9242 GB, free: 7.457 MB / 0.6823 GB Notification: Performance of postOpt removeSimpleEquations (simulation): time 0.007066/0.9452, allocations: 4.205 MB / 0.9283 GB, free: 3.262 MB / 0.6823 GB Notification: Performance of postOpt simplifyComplexFunction (simulation): time 1.072e-05/0.9452, allocations: 0 / 0.9283 GB, free: 3.262 MB / 0.6823 GB Notification: Performance of postOpt solveSimpleEquations (simulation): time 0.0006056/0.9458, allocations: 131.1 kB / 0.9285 GB, free: 3.141 MB / 0.6823 GB Notification: Performance of postOpt tearingSystem (simulation): time 0.001268/0.9471, allocations: 0.6315 MB / 0.9291 GB, free: 2.508 MB / 0.6823 GB Notification: Performance of postOpt inputDerivativesUsed (simulation): time 8.009e-05/0.9472, allocations: 24 kB / 0.9291 GB, free: 2.484 MB / 0.6823 GB Notification: Performance of postOpt calculateStrongComponentJacobians (simulation): time 0.002244/0.9494, allocations: 2.317 MB / 0.9314 GB, free: 100 kB / 0.6823 GB Notification: Performance of postOpt calculateStateSetsJacobians (simulation): time 3.166e-06/0.9494, allocations: 3.062 kB / 0.9314 GB, free: 100 kB / 0.6823 GB Notification: Performance of postOpt symbolicJacobian (simulation): time 0.00495/0.9544, allocations: 2.986 MB / 0.9343 GB, free: 13.12 MB / 0.698 GB Notification: Performance of postOpt removeConstants (simulation): time 0.0006736/0.955, allocations: 238.3 kB / 0.9345 GB, free: 12.89 MB / 0.698 GB Notification: Performance of postOpt simplifyTimeIndepFuncCalls (simulation): time 0.000183/0.9552, allocations: 35.83 kB / 0.9346 GB, free: 12.86 MB / 0.698 GB Notification: Performance of postOpt simplifyAllExpressions (simulation): time 0.0004754/0.9557, allocations: 40.05 kB / 0.9346 GB, free: 12.82 MB / 0.698 GB Notification: Performance of postOpt findZeroCrossings (simulation): time 0.0001542/0.9559, allocations: 60.88 kB / 0.9347 GB, free: 12.76 MB / 0.698 GB Notification: Performance of postOpt collapseArrayExpressions (simulation): time 5.645e-05/0.9559, allocations: 23.98 kB / 0.9347 GB, free: 12.73 MB / 0.698 GB Notification: Performance of sorting global known variables: time 0.001272/0.9572, allocations: 0.6305 MB / 0.9353 GB, free: 12.1 MB / 0.698 GB Notification: Performance of sort global known variables: time 1e-07/0.9572, allocations: 4 kB / 0.9353 GB, free: 12.1 MB / 0.698 GB Notification: Performance of remove unused functions: time 0.00601/0.9632, allocations: 1.873 MB / 0.9371 GB, free: 10.22 MB / 0.698 GB Notification: Model statistics after passing the back-end for simulation: * Number of independent subsystems: 1 * Number of states: 1 (firstOrder.y) * Number of discrete variables: 18 ($cse1.phase,$cse1.region,$cse2.phase,$cse2.region,$cse3.phase,$cse3.region,$cse4.phase,$cse4.region,$cse5.phase,$cse5.region,$cse6.phase,$cse6.region,$cse9.phase,$cse9.region,$cse10.phase,$cse10.region,$cse11.region3boundary,$cse13.region3boundary) * Number of discrete states: 0 () * Number of clocked states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for simulation (87): * Single equations (assignments): 76 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 8 * When equations: 0 * If-equations: 0 * Equation systems (not torn): 0 * Torn equation systems: 3 * Mixed (continuous/discrete) equation systems: 0 Notification: Torn system details for strict tearing set: * Linear torn systems (#iteration vars, #inner vars, density): 0 systems * Non-linear torn systems (#iteration vars, #inner vars): 3 systems {(1,1), (1,5), (1,3)} Notification: Performance of Backend phase and start with SimCode phase: time 0.009425/0.9726, allocations: 2.061 MB / 0.9391 GB, free: 8.34 MB / 0.698 GB Notification: Performance of simCode: created initialization part: time 0.002356/0.975, allocations: 0.9989 MB / 0.9401 GB, free: 7.379 MB / 0.698 GB Notification: Performance of simCode: created event and clocks part: time 3.837e-06/0.975, allocations: 0 / 0.9401 GB, free: 7.379 MB / 0.698 GB Notification: Performance of simCode: created simulation system equations: time 0.001153/0.9761, allocations: 0.6123 MB / 0.9407 GB, free: 6.785 MB / 0.698 GB Notification: Performance of simCode: created of all other equations (e.g. parameter, nominal, assert, etc): time 0.003138/0.9793, allocations: 0.6042 MB / 0.9413 GB, free: 6.223 MB / 0.698 GB [/var/lib/jenkins1/ws/OpenModelicaLibraryTestingWork/OpenModelica/OMCompiler/Compiler/SimCode/SimCodeUtil.mo:10546:11-10546:220:writable] Error: Internal error Unexpected expression (should have been handled earlier, probably in the front-end. Unit/displayUnit expression is not a string literal: ThermofluidStream.Sensors.Internal.getTwoPhaseUnit(vaporQualitySensor.quantity) Notification: Performance of simCode: created linear, non-linear and system jacobian parts: time 0.005863/0.9851, allocations: 3.037 MB / 0.9443 GB, free: 3.172 MB / 0.698 GB Notification: Performance of simCode: some other stuff during SimCode phase: time 0.0009294/0.9861, allocations: 0.7353 MB / 0.945 GB, free: 2.395 MB / 0.698 GB Notification: Performance of simCode: alias equations: time 0.001035/0.9871, allocations: 334 kB / 0.9453 GB, free: 2.074 MB / 0.698 GB Notification: Performance of simCode: all other stuff during SimCode phase: time 0.0002443/0.9873, allocations: 103.4 kB / 0.9454 GB, free: 1.977 MB / 0.698 GB Notification: Performance of SimCode: time 8.51e-07/0.9873, allocations: 0 / 0.9454 GB, free: 1.977 MB / 0.698 GB Notification: Performance of Templates: time 0.1285/1.116, allocations: 75.12 MB / 1.019 GB, free: 7.512 MB / 0.7761 GB " [Timeout remaining time 659] make -j1 -f ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion.makefile [Timeout 660] (rm -f ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion.pipe ; mkfifo ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion.pipe ; head -c 1048576 < ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion.pipe >> ../files/ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion.sim & ./ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion -abortSlowSimulation -alarm=1200 -emit_protected -lv LOG_STATS > ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion.pipe 2>&1) [Timeout 1200] diffSimulationResults("ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat","/mnt/ReferenceFiles/ThermofluidStream-main-regression/ReferenceData/ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_ref.mat","/var/lib/jenkins1/ws/OpenModelicaLibraryTestingWork/OpenModelicaLibraryTesting/files/ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion.diff",relTol=0.003,relTolDiffMinMax=0.003,rangeDelta=0.001) [Timeout 660] "Error: Could not read variable CPUtime in file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable CPUtime from file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable EventCounter in file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable EventCounter from file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable NonlinearSystems.initialization[1].Calls in file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable NonlinearSystems.initialization[1].Calls from file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable NonlinearSystems.initialization[1].Iterations in file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable NonlinearSystems.initialization[1].Iterations from file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable NonlinearSystems.initialization[1].Jacobians in file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable NonlinearSystems.initialization[1].Jacobians from file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable NonlinearSystems.initialization[1].Residues in file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable NonlinearSystems.initialization[1].Residues from file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable NonlinearSystems.simulation[1].Calls in file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable NonlinearSystems.simulation[1].Calls from file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable NonlinearSystems.simulation[1].Iterations in file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable NonlinearSystems.simulation[1].Iterations from file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable NonlinearSystems.simulation[1].Jacobians in file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable NonlinearSystems.simulation[1].Jacobians from file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable NonlinearSystems.simulation[1].Residues in file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable NonlinearSystems.simulation[1].Residues from file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable NonlinearSystems.simulation[2].Calls in file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable NonlinearSystems.simulation[2].Calls from file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable NonlinearSystems.simulation[2].Iterations in file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable NonlinearSystems.simulation[2].Iterations from file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable NonlinearSystems.simulation[2].Jacobians in file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable NonlinearSystems.simulation[2].Jacobians from file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable NonlinearSystems.simulation[2].Residues in file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable NonlinearSystems.simulation[2].Residues from file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable boiler.P in file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable boiler.P from file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable boiler.T_out_fixed in file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable boiler.T_out_fixed from file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable boiler.assertionLevel in file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable boiler.assertionLevel from file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable boiler.dh_fixed in file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable boiler.dh_fixed from file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable boiler.du in file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable boiler.du from file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable boiler.h_out_fixed in file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable boiler.h_out_fixed from file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable boiler.p_inf in file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable boiler.p_inf from file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable boiler.u_in in file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable boiler.u_in from file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable boiler.u_out in file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable boiler.u_out from file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable boiler.v_in in file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable boiler.v_in from file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable boiler.v_out in file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable boiler.v_out from file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable boiler.w_amb in file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable boiler.w_amb from file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable boiler.w_exp in file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable boiler.w_exp from file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable boiler.w_exp_net in file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable boiler.w_exp_net from file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable condenser.P in file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable condenser.P from file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable condenser.assertionLevel in file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable condenser.assertionLevel from file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable condenser.dh_fixed in file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable condenser.dh_fixed from file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable condenser.du in file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable condenser.du from file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable condenser.h_out_fixed in file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable condenser.h_out_fixed from file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable condenser.p_inf in file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable condenser.p_inf from file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable condenser.u_in in file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable condenser.u_in from file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable condenser.u_out in file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable condenser.u_out from file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable condenser.v_in in file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable condenser.v_in from file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable condenser.v_out in file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable condenser.v_out from file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable condenser.w_amb in file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable condenser.w_amb from file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable condenser.w_exp in file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable condenser.w_exp from file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable condenser.w_exp_net in file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable condenser.w_exp_net from file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable dropOfCommons.instanceNameColor[1] in file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable dropOfCommons.instanceNameColor[1] from file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable dropOfCommons.instanceNameColor[2] in file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable dropOfCommons.instanceNameColor[2] from file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable dropOfCommons.instanceNameColor[3] in file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable dropOfCommons.instanceNameColor[3] from file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable loopBreaker.h_out_fixed in file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable loopBreaker.h_out_fixed from file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable loopBreaker.m_flow_in_par in file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable loopBreaker.m_flow_in_par from file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable preheater.P in file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable preheater.P from file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable preheater.T_out_fixed in file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable preheater.T_out_fixed from file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable preheater.assertionLevel in file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable preheater.assertionLevel from file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable preheater.dh_fixed in file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable preheater.dh_fixed from file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable preheater.du in file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable preheater.du from file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable preheater.h_out_fixed in file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable preheater.h_out_fixed from file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable preheater.p_inf in file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable preheater.p_inf from file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable preheater.rho_out in file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable preheater.rho_out from file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable preheater.u_in in file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable preheater.u_in from file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable preheater.u_out in file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable preheater.u_out from file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable preheater.v_in in file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable preheater.v_in from file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable preheater.v_out in file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable preheater.v_out from file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable preheater.w_amb in file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable preheater.w_amb from file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable preheater.w_exp in file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable preheater.w_exp from file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable preheater.w_exp_net in file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable preheater.w_exp_net from file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable pump.P_nom in file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable pump.P_nom from file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable pump.TC in file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable pump.TC from file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable pump.assertionLevel in file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable pump.assertionLevel from file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable pump.dp_fixed in file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable pump.dp_fixed from file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable pump.dp_nom in file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable pump.dp_nom from file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable pump.dp_start in file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable pump.dp_start from file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable pump.pRatio_fixed in file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable pump.pRatio_fixed from file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable pump.p_out_fixed in file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable pump.p_out_fixed from file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable superheater.P in file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable superheater.P from file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable superheater.T_out_fixed in file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable superheater.T_out_fixed from file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable superheater.assertionLevel in file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable superheater.assertionLevel from file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable superheater.dh_fixed in file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable superheater.dh_fixed from file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable superheater.du in file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable superheater.du from file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable superheater.h_out_fixed in file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable superheater.h_out_fixed from file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable superheater.p_inf in file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable superheater.p_inf from file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable superheater.u_in in file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable superheater.u_in from file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable superheater.u_out in file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable superheater.u_out from file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable superheater.v_in in file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable superheater.v_in from file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable superheater.v_out in file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable superheater.v_out from file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable superheater.w_amb in file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable superheater.w_amb from file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable superheater.w_exp in file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable superheater.w_exp from file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable superheater.w_exp_net in file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable superheater.w_exp_net from file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable turbine.P_nom in file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable turbine.P_nom from file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable turbine.TC in file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable turbine.TC from file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable turbine.assertionLevel in file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable turbine.assertionLevel from file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable turbine.dp_fixed in file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable turbine.dp_fixed from file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable turbine.dp_nom in file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable turbine.dp_nom from file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable turbine.dp_start in file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable turbine.dp_start from file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable turbine.inlet.der(m_flow) in file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable turbine.inlet.der(m_flow) from file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable turbine.pRatio_fixed in file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable turbine.pRatio_fixed from file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! " [Timeout remaining time 660] "" Variables in the reference: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 Variables in the result:$cse7.R_s,$cse7.T,$cse7.cp,$cse7.cv,$cse7.dpT,$cse7.h,$cse7.p,$cse7.pd,$cse7.phase,$cse7.pt,$cse7.region,$cse7.rho,$cse7.s,$cse7.vp,$cse7.vt,$cse7.x,$cse8.R_s,$cse8.T,$cse8.cp,$cse8.cv,$cse8.dpT,$cse8.h,$cse8.p,$cse8.pd,$cse8.phase,$cse8.pt,$cse8.region,$cse8.rho,$cse8.s,$cse8.vp,$cse8.vt,$cse8.x,boiler.L,boiler.Q_flow,boiler.T_in,boiler.clip_p_out,boiler.dT,boiler.dT_fixed,boiler.dh,boiler.dp,boiler.dr_corr,boiler.h_in,boiler.h_out,boiler.iconIsHeating,boiler.initM_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.isCycle,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_min,boiler.p_out,boiler.q,boiler.rho_in,boiler.singularityRegime,boiler.systemSpec,condenser.L,condenser.Q_flow,condenser.T_in,condenser.T_out_fixed,condenser.clip_p_out,condenser.dT,condenser.dT_fixed,condenser.dh,condenser.dp,condenser.dr_corr,condenser.h_in,condenser.h_out,condenser.iconIsHeating,condenser.initM_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.isCycle,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_min,condenser.p_out,condenser.q,condenser.rho_in,condenser.rho_out,condenser.singularityRegime,condenser.systemSpec,der(firstOrder.y),dropOfCommons.L,dropOfCommons.assertionLevel,dropOfCommons.g,dropOfCommons.k_volume_damping,dropOfCommons.m_flow_reg,dropOfCommons.omega_reg,dropOfCommons.p_min,dropOfCommons.rho_min,efficiencyExtensive.displayVariablefinal,efficiencyExtensive.number,efficiencyExtensive.showNumber,efficiencyExtensive.significantDigits,efficiencySpecific.displayVariablefinal,efficiencySpecific.number,efficiencySpecific.showNumber,efficiencySpecific.significantDigits,firstOrder.T,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_in,loopBreaker.h_out,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_prescribed,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.Q_flow,preheater.T_in,preheater.clip_p_out,preheater.dT,preheater.dT_fixed,preheater.dh,preheater.dp,preheater.dr_corr,preheater.h_in,preheater.h_out,preheater.iconIsHeating,preheater.initM_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.isCycle,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_min,preheater.p_out,preheater.q,preheater.rho_in,preheater.singularityRegime,preheater.systemSpec,pump.L,pump.P,pump.P_in_internal,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.clip_p_out,pump.dh,pump.dp,pump.dr_corr,pump.etaSpec,pump.eta_actual,pump.eta_fixed,pump.eta_is,pump.h_in,pump.h_out,pump.iconIsCompression,pump.initM_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.p_in,pump.p_min,pump.p_out,pump.singularityRegime,superheater.L,superheater.Q_flow,superheater.T_in,superheater.clip_p_out,superheater.dT,superheater.dT_fixed,superheater.dh,superheater.dp,superheater.dr_corr,superheater.h_in,superheater.h_out,superheater.iconIsHeating,superheater.initM_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.isCycle,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_min,superheater.p_out,superheater.q,superheater.rho_in,superheater.rho_out,superheater.singularityRegime,superheater.systemSpec,time,turbine.L,turbine.P,turbine.P_in_internal,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.clip_p_out,turbine.dh,turbine.dp,turbine.dr_corr,turbine.etaSpec,turbine.eta_actual,turbine.eta_fixed,turbine.eta_is,turbine.h_in,turbine.h_out,turbine.iconIsCompression,turbine.initM_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.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 [Calling sys.exit(0), Time elapsed: 12.023992659989744]