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 0.001455/0.001455, allocations: 99.64 kB / 18.95 MB, free: 2.668 MB / 14.72 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 0.001572/0.001572, allocations: 214.3 kB / 22.25 MB, free: 5.262 MB / 14.72 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 1.485/1.485, allocations: 230.6 MB / 256 MB, free: 7.797 MB / 206.1 MB " [Timeout remaining time 178] 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 1.106/1.106, allocations: 150.8 MB / 463.3 MB, free: 1.477 MB / 366.1 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 0.002648/0.002648, allocations: 88.19 kB / 0.6397 GB, free: 3.133 MB / 478.1 MB Notification: Performance of FrontEnd - Absyn->SCode: time 0.1767/0.1794, allocations: 88.08 MB / 0.7257 GB, free: 10.86 MB / 0.5606 GB Notification: Performance of NFInst.instantiate(ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion): time 0.4112/0.5906, allocations: 66.21 MB / 0.7904 GB, free: 10.96 MB / 0.5919 GB Notification: Performance of NFInst.instExpressions: time 0.03975/0.6303, allocations: 27.49 MB / 0.8172 GB, free: 8.379 MB / 0.6075 GB Notification: Performance of NFInst.updateImplicitVariability: time 0.001876/0.6322, allocations: 54.59 kB / 0.8172 GB, free: 8.344 MB / 0.6075 GB Notification: Performance of NFTyping.typeComponents: time 0.00228/0.6345, allocations: 0.6792 MB / 0.8179 GB, free: 7.781 MB / 0.6075 GB Notification: Performance of NFTyping.typeBindings: time 0.02432/0.6588, allocations: 7.676 MB / 0.8254 GB, free: 2.336 MB / 0.6075 GB Notification: Performance of NFTyping.typeClassSections: time 0.006428/0.6652, allocations: 2.05 MB / 0.8274 GB, free: 0.7773 MB / 0.6075 GB Notification: Performance of NFFlatten.flatten: time 0.003223/0.6684, allocations: 2.091 MB / 0.8295 GB, free: 15.54 MB / 0.6231 GB Notification: Performance of NFFlatten.resolveConnections: time 0.0005247/0.669, allocations: 247.3 kB / 0.8297 GB, free: 15.36 MB / 0.6231 GB Notification: Performance of NFEvalConstants.evaluate: time 0.01846/0.6874, allocations: 8.831 MB / 0.8383 GB, free: 9.828 MB / 0.6231 GB Notification: Performance of NFSimplifyModel.simplify: time 0.001586/0.689, allocations: 0.6838 MB / 0.839 GB, free: 9.418 MB / 0.6231 GB Notification: Performance of NFPackage.collectConstants: time 0.0001841/0.6892, allocations: 93.31 kB / 0.8391 GB, free: 9.418 MB / 0.6231 GB Notification: Performance of NFFlatten.collectFunctions: time 0.02566/0.7148, allocations: 10.76 MB / 0.8496 GB, free: 148 kB / 0.6231 GB Notification: Performance of NFScalarize.scalarize: time 0.0005273/0.7154, allocations: 258.7 kB / 0.8498 GB, free: 15.89 MB / 0.6387 GB Notification: Performance of NFVerifyModel.verify: time 0.001121/0.7165, allocations: 0.5985 MB / 0.8504 GB, free: 15.29 MB / 0.6387 GB Notification: Performance of NFConvertDAE.convert: time 0.02305/0.7395, allocations: 8.221 MB / 0.8584 GB, free: 7.039 MB / 0.6387 GB Notification: Performance of FrontEnd - DAE generated: time 6.993e-06/0.7396, allocations: 0 / 0.8584 GB, free: 7.039 MB / 0.6387 GB Notification: Performance of FrontEnd: time 2.685e-06/0.7396, allocations: 0 / 0.8584 GB, free: 7.039 MB / 0.6387 GB Notification: Performance of Transformations before backend: time 2.243e-05/0.7396, allocations: 0 / 0.8584 GB, free: 7.039 MB / 0.6387 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 0.008195/0.7478, allocations: 2.75 MB / 0.8611 GB, free: 4.242 MB / 0.6387 GB Notification: Performance of prepare preOptimizeDAE: time 4.981e-05/0.7478, allocations: 12.03 kB / 0.8611 GB, free: 4.23 MB / 0.6387 GB Notification: Performance of preOpt normalInlineFunction (simulation): time 0.00208/0.7499, allocations: 371.4 kB / 0.8615 GB, free: 3.867 MB / 0.6387 GB Notification: Performance of preOpt evaluateParameters (simulation): time 0.001813/0.7517, allocations: 0.7968 MB / 0.8623 GB, free: 3.039 MB / 0.6387 GB Notification: Performance of preOpt simplifyIfEquations (simulation): time 0.0002113/0.7519, allocations: 201.2 kB / 0.8625 GB, free: 2.816 MB / 0.6387 GB Notification: Performance of preOpt expandDerOperator (simulation): time 0.0001719/0.7521, allocations: 120 kB / 0.8626 GB, free: 2.699 MB / 0.6387 GB Notification: Performance of preOpt clockPartitioning (simulation): time 0.003211/0.7553, allocations: 1.48 MB / 0.864 GB, free: 1.078 MB / 0.6387 GB Notification: Performance of preOpt findStateOrder (simulation): time 3.327e-05/0.7553, allocations: 7.938 kB / 0.864 GB, free: 1.07 MB / 0.6387 GB Notification: Performance of preOpt replaceEdgeChange (simulation): time 0.000109/0.7555, allocations: 55.98 kB / 0.8641 GB, free: 1.016 MB / 0.6387 GB Notification: Performance of preOpt inlineArrayEqn (simulation): time 3.095e-05/0.7555, allocations: 32 kB / 0.8641 GB, free: 0.9844 MB / 0.6387 GB Notification: Performance of preOpt removeEqualRHS (simulation): time 0.002539/0.758, allocations: 1.019 MB / 0.8651 GB, free: 15.95 MB / 0.6544 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 0.007338/0.7654, allocations: 4.823 MB / 0.8698 GB, free: 11 MB / 0.6544 GB Notification: Performance of preOpt comSubExp (simulation): time 0.002273/0.7676, allocations: 0.8305 MB / 0.8706 GB, free: 10.16 MB / 0.6544 GB Notification: Performance of preOpt resolveLoops (simulation): time 0.0007441/0.7684, allocations: 376.3 kB / 0.871 GB, free: 9.793 MB / 0.6544 GB Notification: Performance of preOpt evalFunc (simulation): time 0.1315/0.8999, allocations: 36.47 MB / 0.9066 GB, free: 5.285 MB / 0.6856 GB Notification: Performance of preOpt encapsulateWhenConditions (simulation): time 6.088e-05/0.8999, allocations: 47.56 kB / 0.9066 GB, free: 5.227 MB / 0.6856 GB Notification: Performance of pre-optimization done (n=85): time 2.845e-06/0.8999, allocations: 3.938 kB / 0.9066 GB, free: 5.223 MB / 0.6856 GB Notification: Performance of matching and sorting (n=85): time 0.004402/0.9043, allocations: 1.391 MB / 0.908 GB, free: 3.82 MB / 0.6856 GB Notification: Performance of inlineWhenForInitialization (initialization): time 8.021e-05/0.9044, allocations: 86.11 kB / 0.9081 GB, free: 3.719 MB / 0.6856 GB Notification: Performance of selectInitializationVariablesDAE (initialization): time 0.001126/0.9055, allocations: 0.7913 MB / 0.9089 GB, free: 2.906 MB / 0.6856 GB Notification: Performance of collectPreVariables (initialization): time 6.65e-05/0.9056, allocations: 41.7 kB / 0.9089 GB, free: 2.859 MB / 0.6856 GB Notification: Performance of collectInitialEqns (initialization): time 0.0005308/0.9061, allocations: 0.6369 MB / 0.9095 GB, free: 2.215 MB / 0.6856 GB Notification: Performance of collectInitialBindings (initialization): time 0.0002824/0.9064, allocations: 305.4 kB / 0.9098 GB, free: 1.914 MB / 0.6856 GB Notification: Performance of simplifyInitialFunctions (initialization): time 0.0002779/0.9067, allocations: 194.5 kB / 0.91 GB, free: 1.715 MB / 0.6856 GB Notification: Performance of setup shared object (initialization): time 0.0001893/0.9069, allocations: 349.9 kB / 0.9103 GB, free: 1.367 MB / 0.6856 GB Notification: Performance of preBalanceInitialSystem (initialization): time 0.0005585/0.9074, allocations: 249.9 kB / 0.9106 GB, free: 1.125 MB / 0.6856 GB Notification: Performance of partitionIndependentBlocks (initialization): time 0.0008699/0.9083, allocations: 0.5639 MB / 0.9111 GB, free: 436 kB / 0.6856 GB Notification: Performance of analyzeInitialSystem (initialization): time 0.00148/0.9098, allocations: 0.8641 MB / 0.912 GB, free: 15.43 MB / 0.7012 GB Notification: Performance of solveInitialSystemEqSystem (initialization): time 7.674e-06/0.9098, allocations: 8 kB / 0.912 GB, free: 15.43 MB / 0.7012 GB Notification: Performance of matching and sorting (n=126) (initialization): time 0.001879/0.9117, allocations: 0.9949 MB / 0.9129 GB, free: 14.42 MB / 0.7012 GB Notification: Performance of prepare postOptimizeDAE: time 2.738e-05/0.9117, allocations: 14.19 kB / 0.913 GB, free: 14.41 MB / 0.7012 GB Notification: Performance of postOpt simplifyComplexFunction (initialization): time 1.527e-05/0.9117, allocations: 8 kB / 0.913 GB, free: 14.4 MB / 0.7012 GB Notification: Performance of postOpt tearingSystem (initialization): time 0.0008419/0.9126, allocations: 142.6 kB / 0.9131 GB, free: 14.25 MB / 0.7012 GB Notification: Performance of postOpt solveSimpleEquations (initialization): time 0.0008009/0.9134, allocations: 223.7 kB / 0.9133 GB, free: 14.04 MB / 0.7012 GB Notification: Performance of postOpt calculateStrongComponentJacobians (initialization): time 0.001294/0.9147, allocations: 1.732 MB / 0.915 GB, free: 12.23 MB / 0.7012 GB Notification: Performance of postOpt simplifyAllExpressions (initialization): time 0.0005909/0.9153, allocations: 103.3 kB / 0.9151 GB, free: 12.13 MB / 0.7012 GB Notification: Performance of postOpt collapseArrayExpressions (initialization): time 7.991e-05/0.9153, allocations: 51.94 kB / 0.9152 GB, free: 12.08 MB / 0.7012 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 0.0004652/0.9158, allocations: 265.5 kB / 0.9154 GB, free: 11.81 MB / 0.7012 GB Notification: Performance of postOpt lateInlineFunction (simulation): time 0.0001961/0.916, allocations: 115.2 kB / 0.9155 GB, free: 11.7 MB / 0.7012 GB Notification: Performance of postOpt wrapFunctionCalls (simulation): time 0.00421/0.9202, allocations: 3.069 MB / 0.9185 GB, free: 8.598 MB / 0.7012 GB Notification: Performance of postOpt inlineArrayEqn (simulation): time 4.552e-05/0.9202, allocations: 39.94 kB / 0.9186 GB, free: 8.559 MB / 0.7012 GB Notification: Performance of postOpt constantLinearSystem (simulation): time 7.594e-06/0.9203, allocations: 4 kB / 0.9186 GB, free: 8.555 MB / 0.7012 GB Notification: Performance of postOpt simplifysemiLinear (simulation): time 1.179e-05/0.9203, allocations: 3.984 kB / 0.9186 GB, free: 8.551 MB / 0.7012 GB Notification: Performance of postOpt removeSimpleEquations (simulation): time 0.005887/0.9262, allocations: 4.194 MB / 0.9227 GB, free: 4.312 MB / 0.7012 GB Notification: Performance of postOpt simplifyComplexFunction (simulation): time 6.172e-06/0.9262, allocations: 4 kB / 0.9227 GB, free: 4.309 MB / 0.7012 GB Notification: Performance of postOpt solveSimpleEquations (simulation): time 0.0005731/0.9267, allocations: 135.8 kB / 0.9228 GB, free: 4.176 MB / 0.7012 GB Notification: Performance of postOpt tearingSystem (simulation): time 0.0012/0.9279, allocations: 0.6207 MB / 0.9234 GB, free: 3.551 MB / 0.7012 GB Notification: Performance of postOpt inputDerivativesUsed (simulation): time 6.403e-05/0.928, allocations: 19.98 kB / 0.9234 GB, free: 3.531 MB / 0.7012 GB Notification: Performance of postOpt calculateStrongComponentJacobians (simulation): time 0.001972/0.93, allocations: 2.317 MB / 0.9257 GB, free: 1.141 MB / 0.7012 GB Notification: Performance of postOpt calculateStateSetsJacobians (simulation): time 1.393e-06/0.93, allocations: 8 kB / 0.9257 GB, free: 1.133 MB / 0.7012 GB Notification: Performance of postOpt symbolicJacobian (simulation): time 0.004419/0.9344, allocations: 2.985 MB / 0.9286 GB, free: 14.12 MB / 0.7169 GB Notification: Performance of postOpt removeConstants (simulation): time 0.0005435/0.9349, allocations: 226.4 kB / 0.9288 GB, free: 13.89 MB / 0.7169 GB Notification: Performance of postOpt simplifyTimeIndepFuncCalls (simulation): time 0.0001344/0.9351, allocations: 35.78 kB / 0.9288 GB, free: 13.86 MB / 0.7169 GB Notification: Performance of postOpt simplifyAllExpressions (simulation): time 0.0004471/0.9355, allocations: 31.97 kB / 0.9289 GB, free: 13.83 MB / 0.7169 GB Notification: Performance of postOpt findZeroCrossings (simulation): time 0.0001331/0.9356, allocations: 60.89 kB / 0.9289 GB, free: 13.77 MB / 0.7169 GB Notification: Performance of postOpt collapseArrayExpressions (simulation): time 7.733e-05/0.9357, allocations: 27.98 kB / 0.929 GB, free: 13.74 MB / 0.7169 GB Notification: Performance of sorting global known variables: time 0.001011/0.9367, allocations: 0.6059 MB / 0.9296 GB, free: 13.12 MB / 0.7169 GB Notification: Performance of sort global known variables: time 1.11e-07/0.9367, allocations: 0 / 0.9296 GB, free: 13.12 MB / 0.7169 GB Notification: Performance of remove unused functions: time 0.007357/0.9441, allocations: 1.863 MB / 0.9314 GB, free: 11.26 MB / 0.7169 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 0.01273/0.9568, allocations: 2.074 MB / 0.9334 GB, free: 9.188 MB / 0.7169 GB Notification: Performance of simCode: created initialization part: time 0.003648/0.9605, allocations: 1.001 MB / 0.9344 GB, free: 8.191 MB / 0.7169 GB Notification: Performance of simCode: created event and clocks part: time 6.562e-06/0.9605, allocations: 0 / 0.9344 GB, free: 8.191 MB / 0.7169 GB Notification: Performance of simCode: created simulation system equations: time 0.001696/0.9622, allocations: 0.6123 MB / 0.935 GB, free: 7.586 MB / 0.7169 GB Notification: Performance of simCode: created of all other equations (e.g. parameter, nominal, assert, etc): time 0.004306/0.9665, allocations: 0.5658 MB / 0.9355 GB, free: 7.055 MB / 0.7169 GB [/var/lib/jenkins/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 0.007851/0.9743, allocations: 2.98 MB / 0.9384 GB, free: 4.039 MB / 0.7169 GB Notification: Performance of simCode: some other stuff during SimCode phase: time 0.001315/0.9756, allocations: 0.7145 MB / 0.9391 GB, free: 3.281 MB / 0.7169 GB Notification: Performance of simCode: alias equations: time 0.001347/0.977, allocations: 326.1 kB / 0.9394 GB, free: 2.965 MB / 0.7169 GB Notification: Performance of simCode: all other stuff during SimCode phase: time 0.0003774/0.9774, allocations: 87.42 kB / 0.9395 GB, free: 2.883 MB / 0.7169 GB Notification: Performance of SimCode: time 1.513e-06/0.9774, allocations: 0 / 0.9395 GB, free: 2.883 MB / 0.7169 GB Notification: Performance of Templates: time 0.1296/1.107, allocations: 74.48 MB / 1.012 GB, free: 8.855 MB / 0.795 GB " [Timeout remaining time 659] make -j1 -f ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion.makefile [Timeout 660] (rm -f ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion.pipe ; mkfifo ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion.pipe ; head -c 1048576 < ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion.pipe >> ../files/ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion.sim & ./ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion -abortSlowSimulation -alarm=1200 -emit_protected -lv LOG_STATS > ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion.pipe 2>&1) [Timeout 1200] diffSimulationResults("ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat","/mnt/ReferenceFiles/ThermofluidStream-main-regression/ReferenceData/ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_ref.mat","/var/lib/jenkins/ws/OpenModelicaLibraryTestingWork/OpenModelicaLibraryTesting/files/ThermofluidStream_dev_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_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable CPUtime from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable EventCounter in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable EventCounter from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable NonlinearSystems.initialization[1].Calls in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable NonlinearSystems.initialization[1].Calls from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable NonlinearSystems.initialization[1].Iterations in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable NonlinearSystems.initialization[1].Iterations from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable NonlinearSystems.initialization[1].Jacobians in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable NonlinearSystems.initialization[1].Jacobians from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable NonlinearSystems.initialization[1].Residues in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable NonlinearSystems.initialization[1].Residues from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable NonlinearSystems.simulation[1].Calls in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable NonlinearSystems.simulation[1].Calls from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable NonlinearSystems.simulation[1].Iterations in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable NonlinearSystems.simulation[1].Iterations from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable NonlinearSystems.simulation[1].Jacobians in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable NonlinearSystems.simulation[1].Jacobians from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable NonlinearSystems.simulation[1].Residues in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable NonlinearSystems.simulation[1].Residues from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable NonlinearSystems.simulation[2].Calls in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable NonlinearSystems.simulation[2].Calls from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable NonlinearSystems.simulation[2].Iterations in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable NonlinearSystems.simulation[2].Iterations from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable NonlinearSystems.simulation[2].Jacobians in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable NonlinearSystems.simulation[2].Jacobians from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable NonlinearSystems.simulation[2].Residues in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable NonlinearSystems.simulation[2].Residues from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable boiler.P in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable boiler.P from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable boiler.T_out_fixed in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable boiler.T_out_fixed from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable boiler.assertionLevel in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable boiler.assertionLevel from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable boiler.dh_fixed in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable boiler.dh_fixed from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable boiler.du in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable boiler.du from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable boiler.h_out_fixed in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable boiler.h_out_fixed from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable boiler.p_inf in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable boiler.p_inf from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable boiler.u_in in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable boiler.u_in from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable boiler.u_out in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable boiler.u_out from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable boiler.v_in in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable boiler.v_in from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable boiler.v_out in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable boiler.v_out from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable boiler.w_amb in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable boiler.w_amb from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable boiler.w_exp in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable boiler.w_exp from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable boiler.w_exp_net in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable boiler.w_exp_net from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable condenser.P in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable condenser.P from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable condenser.assertionLevel in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable condenser.assertionLevel from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable condenser.dh_fixed in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable condenser.dh_fixed from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable condenser.du in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable condenser.du from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable condenser.h_out_fixed in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable condenser.h_out_fixed from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable condenser.p_inf in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable condenser.p_inf from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable condenser.u_in in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable condenser.u_in from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable condenser.u_out in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable condenser.u_out from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable condenser.v_in in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable condenser.v_in from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable condenser.v_out in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable condenser.v_out from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable condenser.w_amb in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable condenser.w_amb from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable condenser.w_exp in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable condenser.w_exp from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable condenser.w_exp_net in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable condenser.w_exp_net from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable dropOfCommons.instanceNameColor[1] in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable dropOfCommons.instanceNameColor[1] from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable dropOfCommons.instanceNameColor[2] in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable dropOfCommons.instanceNameColor[2] from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable dropOfCommons.instanceNameColor[3] in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable dropOfCommons.instanceNameColor[3] from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable loopBreaker.h_out_fixed in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable loopBreaker.h_out_fixed from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable loopBreaker.m_flow_in_par in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable loopBreaker.m_flow_in_par from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable preheater.P in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable preheater.P from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable preheater.T_out_fixed in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable preheater.T_out_fixed from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable preheater.assertionLevel in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable preheater.assertionLevel from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable preheater.dh_fixed in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable preheater.dh_fixed from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable preheater.du in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable preheater.du from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable preheater.h_out_fixed in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable preheater.h_out_fixed from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable preheater.p_inf in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable preheater.p_inf from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable preheater.rho_out in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable preheater.rho_out from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable preheater.u_in in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable preheater.u_in from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable preheater.u_out in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable preheater.u_out from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable preheater.v_in in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable preheater.v_in from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable preheater.v_out in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable preheater.v_out from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable preheater.w_amb in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable preheater.w_amb from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable preheater.w_exp in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable preheater.w_exp from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable preheater.w_exp_net in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable preheater.w_exp_net from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable pump.P_nom in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable pump.P_nom from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable pump.TC in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable pump.TC from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable pump.assertionLevel in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable pump.assertionLevel from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable pump.dp_fixed in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable pump.dp_fixed from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable pump.dp_nom in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable pump.dp_nom from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable pump.dp_start in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable pump.dp_start from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable pump.pRatio_fixed in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable pump.pRatio_fixed from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable pump.p_out_fixed in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable pump.p_out_fixed from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable superheater.P in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable superheater.P from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable superheater.T_out_fixed in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable superheater.T_out_fixed from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable superheater.assertionLevel in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable superheater.assertionLevel from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable superheater.dh_fixed in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable superheater.dh_fixed from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable superheater.du in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable superheater.du from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable superheater.h_out_fixed in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable superheater.h_out_fixed from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable superheater.p_inf in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable superheater.p_inf from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable superheater.u_in in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable superheater.u_in from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable superheater.u_out in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable superheater.u_out from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable superheater.v_in in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable superheater.v_in from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable superheater.v_out in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable superheater.v_out from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable superheater.w_amb in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable superheater.w_amb from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable superheater.w_exp in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable superheater.w_exp from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable superheater.w_exp_net in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable superheater.w_exp_net from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable turbine.P_nom in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable turbine.P_nom from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable turbine.TC in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable turbine.TC from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable turbine.assertionLevel in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable turbine.assertionLevel from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable turbine.dp_fixed in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable turbine.dp_fixed from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable turbine.dp_nom in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable turbine.dp_nom from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable turbine.dp_start in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable turbine.dp_start from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable turbine.inlet.der(m_flow) in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable turbine.inlet.der(m_flow) from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable turbine.pRatio_fixed in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable turbine.pRatio_fixed from file ThermofluidStream_dev_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.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.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.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.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.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.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.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.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.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.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: 12.036018881946802]