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]
"[<interactive>:1:22-1:33:writable] Warning: Modelica only supports 32-bit signed integers! Transforming: 13743895347 into a real
[<interactive>:1:1-1:33:writable] Error: Class GC_set_max_heap_size not found in scope <global scope> (looking for a function or record).
Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/ModelicaServices 4.1.0+maint.om/package.mo): time 0.0003554/0.0003554, allocations: 0 / 0, free: 0 / 0
"
[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 0.000478/0.000478, allocations: 0 / 0, free: 0 / 0
"
[Timeout remaining time 180]
loadFile("/home/hudson/saved_omc/libraries/.openmodelica/libraries/Modelica 4.1.0+maint.om/package.mo", uses=false) [Timeout 180]
"Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/Modelica 4.1.0+maint.om/package.mo): time 0.425/0.425, allocations: 0 / 0, free: 0 / 0
"
[Timeout remaining time 179]
loadFile("/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermofluidStream 1.4.0/package.mo", uses=false) [Timeout 180]
"Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermofluidStream 1.4.0/package.mo): time 0.2707/0.2707, allocations: 0 / 0, free: 0 / 0
"
[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: simulate(ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion,startTime=0,stopTime=1,tolerance=1e-06,numberOfIntervals=100,outputFormat="mat",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",simflags="-alarm=1200  -emit_protected -lv LOG_STATS")
simulate(ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion,startTime=0,stopTime=1,tolerance=1e-06,numberOfIntervals=100,outputFormat="mat",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",simflags="-alarm=1200  -emit_protected -lv LOG_STATS") [Timeout 1860]
"Notification: Performance of FrontEnd - loaded program: time 7.61e-07/7.61e-07, allocations: 0 / 0, free: 0 / 0
Notification: Performance of FrontEnd - Absyn->SCode: time 2.405e-05/2.481e-05, allocations: 0 / 0, free: 0 / 0
Notification: Performance of NFInst.instantiate(ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion): time 0.1679/0.1679, allocations: 0 / 0, free: 0 / 0
Notification: Performance of NFInst.instExpressions: time 0.08675/0.2546, allocations: 0 / 0, free: 0 / 0
Notification: Performance of NFInst.updateImplicitVariability: time 0.002884/0.2575, allocations: 0 / 0, free: 0 / 0
Notification: Performance of NFTyping.typeComponents: time 0.005925/0.2634, allocations: 0 / 0, free: 0 / 0
Notification: Performance of NFTyping.typeBindings: time 0.0535/0.3169, allocations: 0 / 0, free: 0 / 0
Notification: Performance of NFTyping.typeClassSections: time 0.01313/0.3301, allocations: 0 / 0, free: 0 / 0
Notification: Performance of NFFlatten.flatten: time 0.004739/0.3348, allocations: 0 / 0, free: 0 / 0
Notification: Performance of NFFlatten.resolveConnections: time 0.001151/0.336, allocations: 0 / 0, free: 0 / 0
Notification: Performance of NFEvalConstants.evaluate: time 0.03976/0.3757, allocations: 0 / 0, free: 0 / 0
Notification: Performance of NFSimplifyModel.simplify: time 0.002111/0.3778, allocations: 0 / 0, free: 0 / 0
Notification: Performance of NFPackage.collectConstants: time 0.0003355/0.3782, allocations: 0 / 0, free: 0 / 0
Notification: Performance of NFFlatten.collectFunctions: time 0.07743/0.4556, allocations: 0 / 0, free: 0 / 0
Notification: Performance of NFScalarize.scalarize: time 0.0009752/0.4566, allocations: 0 / 0, free: 0 / 0
Notification: Performance of NFVerifyModel.verify: time 0.001825/0.4584, allocations: 0 / 0, free: 0 / 0
Notification: Performance of NFConvertDAE.convert: time 0.04473/0.5031, allocations: 0 / 0, free: 0 / 0
Notification: Performance of FrontEnd - DAE generated: time 0.0006628/0.5038, allocations: 0 / 0, free: 0 / 0
Notification: Performance of FrontEnd: time 4.84e-06/0.5038, allocations: 0 / 0, free: 0 / 0
Notification: Performance of Transformations before backend: time 3.03e-05/0.5038, allocations: 0 / 0, free: 0 / 0
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 0.02563/0.5294, allocations: 0 / 0, free: 0 / 0
Notification: Performance of prepare preOptimizeDAE: time 0.0002169/0.5297, allocations: 0 / 0, free: 0 / 0
Notification: Performance of preOpt normalInlineFunction (simulation): time 0.01097/0.5406, allocations: 0 / 0, free: 0 / 0
Notification: Performance of preOpt evaluateParameters (simulation): time 0.005139/0.5458, allocations: 0 / 0, free: 0 / 0
Notification: Performance of preOpt simplifyIfEquations (simulation): time 0.0003834/0.5462, allocations: 0 / 0, free: 0 / 0
Notification: Performance of preOpt expandDerOperator (simulation): time 0.000511/0.5467, allocations: 0 / 0, free: 0 / 0
Notification: Performance of preOpt clockPartitioning (simulation): time 0.01075/0.5574, allocations: 0 / 0, free: 0 / 0
Notification: Performance of preOpt findStateOrder (simulation): time 8.558e-05/0.5575, allocations: 0 / 0, free: 0 / 0
Notification: Performance of preOpt replaceEdgeChange (simulation): time 0.0003791/0.5579, allocations: 0 / 0, free: 0 / 0
Notification: Performance of preOpt inlineArrayEqn (simulation): time 9.092e-05/0.558, allocations: 0 / 0, free: 0 / 0
Notification: Performance of preOpt removeEqualRHS (simulation): time 0.009129/0.5671, allocations: 0 / 0, free: 0 / 0
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 0.02273/0.5898, allocations: 0 / 0, free: 0 / 0
Notification: Performance of preOpt comSubExp (simulation): time 0.007457/0.5973, allocations: 0 / 0, free: 0 / 0
Notification: Performance of preOpt resolveLoops (simulation): time 0.002096/0.5994, allocations: 0 / 0, free: 0 / 0
Notification: Performance of preOpt evalFunc (simulation): time 0.2429/0.8423, allocations: 0 / 0, free: 0 / 0
Notification: Performance of preOpt encapsulateWhenConditions (simulation): time 9.801e-05/0.8424, allocations: 0 / 0, free: 0 / 0
Notification: Performance of pre-optimization done (n=85): time 0.0002966/0.8427, allocations: 0 / 0, free: 0 / 0
Notification: Performance of matching and sorting (n=85): time 0.01514/0.8578, allocations: 0 / 0, free: 0 / 0
Notification: Performance of inlineWhenForInitialization (initialization): time 0.0001263/0.8579, allocations: 0 / 0, free: 0 / 0
Notification: Performance of selectInitializationVariablesDAE (initialization): time 0.003916/0.8618, allocations: 0 / 0, free: 0 / 0
Notification: Performance of collectPreVariables (initialization): time 0.0002723/0.8621, allocations: 0 / 0, free: 0 / 0
Notification: Performance of collectInitialEqns (initialization): time 0.001086/0.8632, allocations: 0 / 0, free: 0 / 0
Notification: Performance of collectInitialBindings (initialization): time 0.0005275/0.8637, allocations: 0 / 0, free: 0 / 0
Notification: Performance of simplifyInitialFunctions (initialization): time 0.001025/0.8648, allocations: 0 / 0, free: 0 / 0
Notification: Performance of setup shared object (initialization): time 0.000299/0.8651, allocations: 0 / 0, free: 0 / 0
Notification: Performance of preBalanceInitialSystem (initialization): time 0.001639/0.8667, allocations: 0 / 0, free: 0 / 0
Notification: Performance of partitionIndependentBlocks (initialization): time 0.002085/0.8688, allocations: 0 / 0, free: 0 / 0
Notification: Performance of analyzeInitialSystem (initialization): time 0.003951/0.8727, allocations: 0 / 0, free: 0 / 0
Notification: Performance of solveInitialSystemEqSystem (initialization): time 2.955e-05/0.8728, allocations: 0 / 0, free: 0 / 0
Notification: Performance of matching and sorting (n=126) (initialization): time 0.006346/0.8791, allocations: 0 / 0, free: 0 / 0
Notification: Performance of prepare postOptimizeDAE: time 6.419e-05/0.8792, allocations: 0 / 0, free: 0 / 0
Notification: Performance of postOpt simplifyComplexFunction (initialization): time 3.997e-05/0.8792, allocations: 0 / 0, free: 0 / 0
Notification: Performance of postOpt tearingSystem (initialization): time 0.002635/0.8818, allocations: 0 / 0, free: 0 / 0
Notification: Performance of postOpt solveSimpleEquations (initialization): time 0.001777/0.8836, allocations: 0 / 0, free: 0 / 0
Notification: Performance of postOpt calculateStrongComponentJacobians (initialization): time 0.003012/0.8866, allocations: 0 / 0, free: 0 / 0
Notification: Performance of postOpt simplifyAllExpressions (initialization): time 0.001175/0.8878, allocations: 0 / 0, free: 0 / 0
Notification: Performance of postOpt collapseArrayExpressions (initialization): time 0.0002604/0.8881, allocations: 0 / 0, free: 0 / 0
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 0.001808/0.8899, allocations: 0 / 0, free: 0 / 0
Notification: Performance of postOpt lateInlineFunction (simulation): time 0.0008761/0.8908, allocations: 0 / 0, free: 0 / 0
Notification: Performance of postOpt wrapFunctionCalls (simulation): time 0.01269/0.9034, allocations: 0 / 0, free: 0 / 0
Notification: Performance of postOpt inlineArrayEqn (simulation): time 9.664e-05/0.9035, allocations: 0 / 0, free: 0 / 0
Notification: Performance of postOpt constantLinearSystem (simulation): time 8.637e-06/0.9036, allocations: 0 / 0, free: 0 / 0
Notification: Performance of postOpt simplifysemiLinear (simulation): time 2.384e-05/0.9036, allocations: 0 / 0, free: 0 / 0
Notification: Performance of postOpt removeSimpleEquations (simulation): time 0.01957/0.9231, allocations: 0 / 0, free: 0 / 0
Notification: Performance of postOpt simplifyComplexFunction (simulation): time 1.511e-05/0.9232, allocations: 0 / 0, free: 0 / 0
Notification: Performance of postOpt solveSimpleEquations (simulation): time 0.001143/0.9243, allocations: 0 / 0, free: 0 / 0
Notification: Performance of postOpt tearingSystem (simulation): time 0.003974/0.9283, allocations: 0 / 0, free: 0 / 0
Notification: Performance of postOpt inputDerivativesUsed (simulation): time 0.0002182/0.9285, allocations: 0 / 0, free: 0 / 0
Notification: Performance of postOpt calculateStrongComponentJacobians (simulation): time 0.005042/0.9335, allocations: 0 / 0, free: 0 / 0
Notification: Performance of postOpt calculateStateSetsJacobians (simulation): time 4.208e-06/0.9335, allocations: 0 / 0, free: 0 / 0
Notification: Performance of postOpt symbolicJacobian (simulation): time 0.01271/0.9463, allocations: 0 / 0, free: 0 / 0
Notification: Performance of postOpt removeConstants (simulation): time 0.002321/0.9486, allocations: 0 / 0, free: 0 / 0
Notification: Performance of postOpt simplifyTimeIndepFuncCalls (simulation): time 0.0007031/0.9493, allocations: 0 / 0, free: 0 / 0
Notification: Performance of postOpt simplifyAllExpressions (simulation): time 0.001077/0.9504, allocations: 0 / 0, free: 0 / 0
Notification: Performance of postOpt findZeroCrossings (simulation): time 0.0006522/0.951, allocations: 0 / 0, free: 0 / 0
Notification: Performance of postOpt collapseArrayExpressions (simulation): time 0.0001996/0.9512, allocations: 0 / 0, free: 0 / 0
Notification: Performance of sorting global known variables: time 0.002785/0.954, allocations: 0 / 0, free: 0 / 0
Notification: Performance of sort global known variables: time 8.383e-05/0.9541, allocations: 0 / 0, free: 0 / 0
Notification: Performance of remove unused functions: time 0.01177/0.9658, allocations: 0 / 0, free: 0 / 0
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 0.02992/0.9958, allocations: 0 / 0, free: 0 / 0
Notification: Performance of simCode: created initialization part: time 0.005356/1.001, allocations: 0 / 0, free: 0 / 0
Notification: Performance of simCode: created event and clocks part: time 7.233e-06/1.001, allocations: 0 / 0, free: 0 / 0
Notification: Performance of simCode: created simulation system equations: time 0.003115/1.004, allocations: 0 / 0, free: 0 / 0
Notification: Performance of simCode: created of all other equations (e.g. parameter, nominal, assert, etc): time 0.007263/1.012, allocations: 0 / 0, free: 0 / 0
[SimCode/SimCodeUtil.mo:0:0-0:0: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 0.01566/1.027, allocations: 0 / 0, free: 0 / 0
Notification: Performance of simCode: some other stuff during SimCode phase: time 0.002718/1.03, allocations: 0 / 0, free: 0 / 0
Notification: Performance of simCode: alias equations: time 0.001644/1.032, allocations: 0 / 0, free: 0 / 0
Notification: Performance of simCode: all other stuff during SimCode phase: time 0.001215/1.033, allocations: 0 / 0, free: 0 / 0
Notification: Performance of SimCode: time 0.00114/1.034, allocations: 0 / 0, free: 0 / 0
Notification: Performance of Templates: time 0.02649/1.06, allocations: 0 / 0, free: 0 / 0
"
[Timeout remaining time 1859]
diffSimulationResults("ThermofluidStream_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_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.dT_fixed in file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat.
Warning: Get data of variable boiler.dT_fixed 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.dT_fixed in file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat.
Warning: Get data of variable condenser.dT_fixed 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 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.dT_fixed in file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat.
Warning: Get data of variable preheater.dT_fixed 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.dT_fixed in file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat.
Warning: Get data of variable superheater.dT_fixed 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:boiler.L,boiler.Q_flow,boiler.T_in,boiler.clip_p_out,boiler.dT,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.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.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.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.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.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: 2.9494698109992896]