Running: ./testmodel.py --libraries=/home/hudson/saved_omc/libraries/.openmodelica/libraries --ompython_omhome=/usr ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion.conf.json loadFile("/home/hudson/saved_omc/libraries/.openmodelica/libraries/ModelicaServices 4.1.0+maint.om/package.mo", uses=false) [Timeout 180] "Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/ModelicaServices 4.1.0+maint.om/package.mo): time 0.0008523/0.0008523, allocations: 100.4 kB / 19.7 MB, free: 452 kB / 13.93 MB " [Timeout remaining time 180] loadFile("/home/hudson/saved_omc/libraries/.openmodelica/libraries/Complex 4.1.0+maint.om/package.mo", uses=false) [Timeout 180] "Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/Complex 4.1.0+maint.om/package.mo): time 0.0008805/0.0008805, allocations: 212.1 kB / 23 MB, free: 2.98 MB / 13.93 MB " [Timeout remaining time 180] loadFile("/home/hudson/saved_omc/libraries/.openmodelica/libraries/Modelica 4.1.0+maint.om/package.mo", uses=false) [Timeout 180] "Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/Modelica 4.1.0+maint.om/package.mo): time 0.9743/0.9743, allocations: 230.6 MB / 256.8 MB, free: 9.605 MB / 202.7 MB " [Timeout remaining time 179] loadFile("/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermofluidStream 1.4.0/package.mo", uses=false) [Timeout 180] "Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermofluidStream 1.4.0/package.mo): time 0.7122/0.7122, allocations: 154.1 MB / 467.3 MB, free: 3.277 MB / 362.7 MB " [Timeout remaining time 179] Using package ThermofluidStream with version 1.4.0 (/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermofluidStream 1.4.0/package.mo) Using package Modelica with version 4.1.0 (/home/hudson/saved_omc/libraries/.openmodelica/libraries/Modelica 4.1.0+maint.om/package.mo) Using package Complex with version 4.1.0 (/home/hudson/saved_omc/libraries/.openmodelica/libraries/Complex 4.1.0+maint.om/package.mo) Using package ModelicaServices with version 4.1.0 (/home/hudson/saved_omc/libraries/.openmodelica/libraries/ModelicaServices 4.1.0+maint.om/package.mo) Running command: translateModel(ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion,tolerance=1e-06,outputFormat="mat",numberOfIntervals=100,variableFilter="CPUtime|EventCounter|NonlinearSystems.initialization.1..Calls|NonlinearSystems.initialization.1..Iterations|NonlinearSystems.initialization.1..Jacobians|NonlinearSystems.initialization.1..Residues|NonlinearSystems.simulation.1..Calls|NonlinearSystems.simulation.1..Iterations|NonlinearSystems.simulation.1..Jacobians|NonlinearSystems.simulation.1..Residues|NonlinearSystems.simulation.2..Calls|NonlinearSystems.simulation.2..Iterations|NonlinearSystems.simulation.2..Jacobians|NonlinearSystems.simulation.2..Residues|Time|boiler.L|boiler.P|boiler.Q_flow|boiler.T_out_fixed|boiler.assertionLevel|boiler.clip_p_out|boiler.dT|boiler.dT_fixed|boiler.dh|boiler.dh_fixed|boiler.dp|boiler.dr_corr|boiler.du|boiler.h_in|boiler.h_out|boiler.h_out_fixed|boiler.initM_flow|der.boiler.inlet.m_flow.|boiler.inlet.m_flow|boiler.inlet.r|boiler.inlet.state.T|boiler.inlet.state.d|boiler.inlet.state.h|boiler.inlet.state.p|boiler.inlet.state.phase|boiler.m_acceleration_0|boiler.m_flow|boiler.m_flowStateSelect|boiler.m_flow_0|boiler.outlet.m_flow|boiler.outlet.r|boiler.outlet.state.T|boiler.outlet.state.d|boiler.outlet.state.h|boiler.outlet.state.p|boiler.outlet.state.phase|boiler.outletSpec|boiler.outletSpec_actual|boiler.outletSpec_prescribed|boiler.outletValueSpec|boiler.p|boiler.p_in|boiler.p_inf|boiler.p_min|boiler.p_out|boiler.q|boiler.rho_in|boiler.rho_out|boiler.singularityRegime|boiler.systemSpec|boiler.u_in|boiler.u_out|boiler.v_in|boiler.v_out|boiler.w_amb|boiler.w_exp|boiler.w_exp_net|condenser.L|condenser.P|condenser.Q_flow|condenser.T_out_fixed|condenser.assertionLevel|condenser.clip_p_out|condenser.dT|condenser.dT_fixed|condenser.dh|condenser.dh_fixed|condenser.dp|condenser.dr_corr|condenser.du|condenser.h_in|condenser.h_out|condenser.h_out_fixed|condenser.initM_flow|der.condenser.inlet.m_flow.|condenser.inlet.m_flow|condenser.inlet.r|condenser.inlet.state.T|condenser.inlet.state.d|condenser.inlet.state.h|condenser.inlet.state.p|condenser.inlet.state.phase|condenser.m_acceleration_0|condenser.m_flow|condenser.m_flowStateSelect|condenser.m_flow_0|condenser.outlet.m_flow|condenser.outlet.r|condenser.outlet.state.T|condenser.outlet.state.d|condenser.outlet.state.h|condenser.outlet.state.p|condenser.outlet.state.phase|condenser.outletSpec|condenser.outletSpec_actual|condenser.outletValueSpec|condenser.p|condenser.p_in|condenser.p_inf|condenser.p_min|condenser.p_out|condenser.q|condenser.rho_in|condenser.rho_out|condenser.singularityRegime|condenser.systemSpec|condenser.u_in|condenser.u_out|condenser.v_in|condenser.v_out|condenser.w_amb|condenser.w_exp|condenser.w_exp_net|dropOfCommons.L|dropOfCommons.assertionLevel|dropOfCommons.g|dropOfCommons.instanceNameColor.1.|dropOfCommons.instanceNameColor.2.|dropOfCommons.instanceNameColor.3.|dropOfCommons.k_volume_damping|dropOfCommons.m_flow_reg|dropOfCommons.omega_reg|dropOfCommons.p_min|dropOfCommons.rho_min|efficiencyExtensive.displayVariablefinal|efficiencyExtensive.showNumber|efficiencyExtensive.significantDigits|efficiencySpecific.displayVariablefinal|efficiencySpecific.showNumber|efficiencySpecific.significantDigits|firstOrder.T|der.firstOrder.y.|firstOrder.initType|firstOrder.k|firstOrder.u|firstOrder.y|firstOrder.y_start|h_bubble.y|h_dew.y|inverseBlockConstraints.u1|inverseBlockConstraints.u2|inverseBlockConstraints.y1|inverseBlockConstraints.y2|loopBreaker.L|loopBreaker.T_out|loopBreaker.T_out_fixed|loopBreaker.XiSpec|loopBreaker.assertionLevel|loopBreaker.dh|loopBreaker.dm_flow|loopBreaker.dp|loopBreaker.h_out|loopBreaker.h_out_fixed|loopBreaker.inlet.m_flow|loopBreaker.inlet.r|loopBreaker.inlet.state.T|loopBreaker.inlet.state.d|loopBreaker.inlet.state.h|loopBreaker.inlet.state.p|loopBreaker.inlet.state.phase|loopBreaker.m_flowSpec|loopBreaker.m_flow_in|loopBreaker.m_flow_in_par|loopBreaker.m_flow_in_prescribed|der.loopBreaker.outlet.m_flow.|loopBreaker.outlet.m_flow|loopBreaker.outlet.r|loopBreaker.outlet.state.T|loopBreaker.outlet.state.d|loopBreaker.outlet.state.h|loopBreaker.outlet.state.p|loopBreaker.outlet.state.phase|loopBreaker.pSpec|loopBreaker.p_out|loopBreaker.p_out_fixed|loopBreaker.thermalSpec|loopBreaker.thermalValueSpec|loopBreaker.tol_Xi|loopBreaker.tol_h|loopBreaker.tol_m_flow|loopBreaker.tol_p|massFlowRate.height|massFlowRate.offset|massFlowRate.startTime|massFlowRate.y|outletPressure.duration|outletPressure.height|outletPressure.offset|outletPressure.startTime|outletPressure.y|preheater.L|preheater.P|preheater.Q_flow|preheater.T_out_fixed|preheater.assertionLevel|preheater.clip_p_out|preheater.dT|preheater.dT_fixed|preheater.dh|preheater.dh_fixed|preheater.dp|preheater.dr_corr|preheater.du|preheater.h_in|preheater.h_out|preheater.h_out_fixed|preheater.initM_flow|der.preheater.inlet.m_flow.|preheater.inlet.m_flow|preheater.inlet.r|preheater.inlet.state.T|preheater.inlet.state.d|preheater.inlet.state.h|preheater.inlet.state.p|preheater.inlet.state.phase|preheater.m_acceleration_0|preheater.m_flow|preheater.m_flowStateSelect|preheater.m_flow_0|preheater.outlet.m_flow|preheater.outlet.r|preheater.outlet.state.T|preheater.outlet.state.d|preheater.outlet.state.h|preheater.outlet.state.p|preheater.outlet.state.phase|preheater.outletSpec|preheater.outletSpec_actual|preheater.outletSpec_prescribed|preheater.outletValueSpec|preheater.p|preheater.p_in|preheater.p_inf|preheater.p_min|preheater.p_out|preheater.q|preheater.rho_in|preheater.rho_out|preheater.singularityRegime|preheater.systemSpec|preheater.u_in|preheater.u_out|preheater.v_in|preheater.v_out|preheater.w_amb|preheater.w_exp|preheater.w_exp_net|pump.L|pump.P|pump.P_nom|pump.TC|pump.adiabaticModel.eta_is|pump.adiabaticModel.h_in|pump.adiabaticModel.h_out|pump.adiabaticModel.h_out_is|pump.adiabaticModel.p_out|pump.adiabaticModel.s_in|pump.adiabaticModel.state_in.T|pump.adiabaticModel.state_in.d|pump.adiabaticModel.state_in.h|pump.adiabaticModel.state_in.p|pump.adiabaticModel.state_in.phase|pump.adiabaticModel.w_t|pump.adiabaticModel.w_t_is|pump.assertionLevel|pump.clip_p_out|pump.dh|pump.dp|pump.dp_fixed|pump.dp_nom|pump.dp_start|pump.dr_corr|pump.etaSpec|pump.eta_actual|pump.eta_fixed|pump.eta_is|pump.h_in|pump.h_out|pump.initM_flow|der.pump.inlet.m_flow.|pump.inlet.m_flow|pump.inlet.r|pump.inlet.state.T|pump.inlet.state.d|pump.inlet.state.h|pump.inlet.state.p|pump.inlet.state.phase|pump.m_acceleration_0|pump.m_flow|pump.m_flowStateSelect|pump.m_flow_0|pump.outlet.m_flow|pump.outlet.r|pump.outlet.state.T|pump.outlet.state.d|pump.outlet.state.h|pump.outlet.state.p|pump.outlet.state.phase|pump.outletSpec|pump.outletSpec_actual|pump.outletSpec_prescribed|pump.outletValueSpec|pump.pRatio|pump.pRatio_fixed|pump.p_in|pump.p_min|pump.p_out|pump.p_out_fixed|pump.singularityRegime|superheater.L|superheater.P|superheater.Q_flow|superheater.T_out_fixed|superheater.assertionLevel|superheater.clip_p_out|superheater.dT|superheater.dT_fixed|superheater.dh|superheater.dh_fixed|superheater.dp|superheater.dr_corr|superheater.du|superheater.h_in|superheater.h_out|superheater.h_out_fixed|superheater.initM_flow|der.superheater.inlet.m_flow.|superheater.inlet.m_flow|superheater.inlet.r|superheater.inlet.state.T|superheater.inlet.state.d|superheater.inlet.state.h|superheater.inlet.state.p|superheater.inlet.state.phase|superheater.m_acceleration_0|superheater.m_flow|superheater.m_flowStateSelect|superheater.m_flow_0|superheater.outlet.m_flow|superheater.outlet.r|superheater.outlet.state.T|superheater.outlet.state.d|superheater.outlet.state.h|superheater.outlet.state.p|superheater.outlet.state.phase|superheater.outletSpec|superheater.outletSpec_actual|superheater.outletSpec_prescribed|superheater.outletValueSpec|superheater.p|superheater.p_in|superheater.p_inf|superheater.p_min|superheater.p_out|superheater.q|superheater.rho_in|superheater.rho_out|superheater.singularityRegime|superheater.systemSpec|superheater.u_in|superheater.u_out|superheater.v_in|superheater.v_out|superheater.w_amb|superheater.w_exp|superheater.w_exp_net|turbine.L|turbine.P|turbine.P_nom|turbine.TC|turbine.adiabaticModel.eta_is|turbine.adiabaticModel.h_in|turbine.adiabaticModel.h_out|turbine.adiabaticModel.h_out_is|turbine.adiabaticModel.p_out|turbine.adiabaticModel.s_in|turbine.adiabaticModel.state_in.T|turbine.adiabaticModel.state_in.d|turbine.adiabaticModel.state_in.h|turbine.adiabaticModel.state_in.p|turbine.adiabaticModel.state_in.phase|turbine.adiabaticModel.w_t|turbine.adiabaticModel.w_t_is|turbine.assertionLevel|turbine.clip_p_out|turbine.dh|turbine.dp|turbine.dp_fixed|turbine.dp_nom|turbine.dp_start|turbine.dr_corr|turbine.etaSpec|turbine.eta_actual|turbine.eta_fixed|turbine.eta_is|turbine.h_in|turbine.h_out|turbine.initM_flow|der.turbine.inlet.m_flow.|turbine.inlet.m_flow|turbine.inlet.r|turbine.inlet.state.T|turbine.inlet.state.d|turbine.inlet.state.h|turbine.inlet.state.p|turbine.inlet.state.phase|turbine.m_acceleration_0|turbine.m_flow|turbine.m_flowStateSelect|turbine.m_flow_0|turbine.outlet.m_flow|turbine.outlet.r|turbine.outlet.state.T|turbine.outlet.state.d|turbine.outlet.state.h|turbine.outlet.state.p|turbine.outlet.state.phase|turbine.outletSpec|turbine.outletSpec_actual|turbine.outletValueSpec|turbine.pRatio|turbine.pRatio_fixed|turbine.p_in|turbine.p_min|turbine.p_out|turbine.p_out_fixed|turbine.singularityRegime|vaporQualitySensor.TC|vaporQualitySensor.digits|vaporQualitySensor.direct_value|vaporQualitySensor.init|vaporQualitySensor.inlet.m_flow|vaporQualitySensor.inlet.r|vaporQualitySensor.inlet.state.T|vaporQualitySensor.inlet.state.d|vaporQualitySensor.inlet.state.h|vaporQualitySensor.inlet.state.p|vaporQualitySensor.inlet.state.phase|vaporQualitySensor.quantity|vaporQualitySensor.value|vaporQualitySensor.value_0|vaporQualitySensor.value_out|vaporQualitySetpoint.y",fileNamePrefix="ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion") translateModel(ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion,tolerance=1e-06,outputFormat="mat",numberOfIntervals=100,variableFilter="CPUtime|EventCounter|NonlinearSystems.initialization.1..Calls|NonlinearSystems.initialization.1..Iterations|NonlinearSystems.initialization.1..Jacobians|NonlinearSystems.initialization.1..Residues|NonlinearSystems.simulation.1..Calls|NonlinearSystems.simulation.1..Iterations|NonlinearSystems.simulation.1..Jacobians|NonlinearSystems.simulation.1..Residues|NonlinearSystems.simulation.2..Calls|NonlinearSystems.simulation.2..Iterations|NonlinearSystems.simulation.2..Jacobians|NonlinearSystems.simulation.2..Residues|Time|boiler.L|boiler.P|boiler.Q_flow|boiler.T_out_fixed|boiler.assertionLevel|boiler.clip_p_out|boiler.dT|boiler.dT_fixed|boiler.dh|boiler.dh_fixed|boiler.dp|boiler.dr_corr|boiler.du|boiler.h_in|boiler.h_out|boiler.h_out_fixed|boiler.initM_flow|der.boiler.inlet.m_flow.|boiler.inlet.m_flow|boiler.inlet.r|boiler.inlet.state.T|boiler.inlet.state.d|boiler.inlet.state.h|boiler.inlet.state.p|boiler.inlet.state.phase|boiler.m_acceleration_0|boiler.m_flow|boiler.m_flowStateSelect|boiler.m_flow_0|boiler.outlet.m_flow|boiler.outlet.r|boiler.outlet.state.T|boiler.outlet.state.d|boiler.outlet.state.h|boiler.outlet.state.p|boiler.outlet.state.phase|boiler.outletSpec|boiler.outletSpec_actual|boiler.outletSpec_prescribed|boiler.outletValueSpec|boiler.p|boiler.p_in|boiler.p_inf|boiler.p_min|boiler.p_out|boiler.q|boiler.rho_in|boiler.rho_out|boiler.singularityRegime|boiler.systemSpec|boiler.u_in|boiler.u_out|boiler.v_in|boiler.v_out|boiler.w_amb|boiler.w_exp|boiler.w_exp_net|condenser.L|condenser.P|condenser.Q_flow|condenser.T_out_fixed|condenser.assertionLevel|condenser.clip_p_out|condenser.dT|condenser.dT_fixed|condenser.dh|condenser.dh_fixed|condenser.dp|condenser.dr_corr|condenser.du|condenser.h_in|condenser.h_out|condenser.h_out_fixed|condenser.initM_flow|der.condenser.inlet.m_flow.|condenser.inlet.m_flow|condenser.inlet.r|condenser.inlet.state.T|condenser.inlet.state.d|condenser.inlet.state.h|condenser.inlet.state.p|condenser.inlet.state.phase|condenser.m_acceleration_0|condenser.m_flow|condenser.m_flowStateSelect|condenser.m_flow_0|condenser.outlet.m_flow|condenser.outlet.r|condenser.outlet.state.T|condenser.outlet.state.d|condenser.outlet.state.h|condenser.outlet.state.p|condenser.outlet.state.phase|condenser.outletSpec|condenser.outletSpec_actual|condenser.outletValueSpec|condenser.p|condenser.p_in|condenser.p_inf|condenser.p_min|condenser.p_out|condenser.q|condenser.rho_in|condenser.rho_out|condenser.singularityRegime|condenser.systemSpec|condenser.u_in|condenser.u_out|condenser.v_in|condenser.v_out|condenser.w_amb|condenser.w_exp|condenser.w_exp_net|dropOfCommons.L|dropOfCommons.assertionLevel|dropOfCommons.g|dropOfCommons.instanceNameColor.1.|dropOfCommons.instanceNameColor.2.|dropOfCommons.instanceNameColor.3.|dropOfCommons.k_volume_damping|dropOfCommons.m_flow_reg|dropOfCommons.omega_reg|dropOfCommons.p_min|dropOfCommons.rho_min|efficiencyExtensive.displayVariablefinal|efficiencyExtensive.showNumber|efficiencyExtensive.significantDigits|efficiencySpecific.displayVariablefinal|efficiencySpecific.showNumber|efficiencySpecific.significantDigits|firstOrder.T|der.firstOrder.y.|firstOrder.initType|firstOrder.k|firstOrder.u|firstOrder.y|firstOrder.y_start|h_bubble.y|h_dew.y|inverseBlockConstraints.u1|inverseBlockConstraints.u2|inverseBlockConstraints.y1|inverseBlockConstraints.y2|loopBreaker.L|loopBreaker.T_out|loopBreaker.T_out_fixed|loopBreaker.XiSpec|loopBreaker.assertionLevel|loopBreaker.dh|loopBreaker.dm_flow|loopBreaker.dp|loopBreaker.h_out|loopBreaker.h_out_fixed|loopBreaker.inlet.m_flow|loopBreaker.inlet.r|loopBreaker.inlet.state.T|loopBreaker.inlet.state.d|loopBreaker.inlet.state.h|loopBreaker.inlet.state.p|loopBreaker.inlet.state.phase|loopBreaker.m_flowSpec|loopBreaker.m_flow_in|loopBreaker.m_flow_in_par|loopBreaker.m_flow_in_prescribed|der.loopBreaker.outlet.m_flow.|loopBreaker.outlet.m_flow|loopBreaker.outlet.r|loopBreaker.outlet.state.T|loopBreaker.outlet.state.d|loopBreaker.outlet.state.h|loopBreaker.outlet.state.p|loopBreaker.outlet.state.phase|loopBreaker.pSpec|loopBreaker.p_out|loopBreaker.p_out_fixed|loopBreaker.thermalSpec|loopBreaker.thermalValueSpec|loopBreaker.tol_Xi|loopBreaker.tol_h|loopBreaker.tol_m_flow|loopBreaker.tol_p|massFlowRate.height|massFlowRate.offset|massFlowRate.startTime|massFlowRate.y|outletPressure.duration|outletPressure.height|outletPressure.offset|outletPressure.startTime|outletPressure.y|preheater.L|preheater.P|preheater.Q_flow|preheater.T_out_fixed|preheater.assertionLevel|preheater.clip_p_out|preheater.dT|preheater.dT_fixed|preheater.dh|preheater.dh_fixed|preheater.dp|preheater.dr_corr|preheater.du|preheater.h_in|preheater.h_out|preheater.h_out_fixed|preheater.initM_flow|der.preheater.inlet.m_flow.|preheater.inlet.m_flow|preheater.inlet.r|preheater.inlet.state.T|preheater.inlet.state.d|preheater.inlet.state.h|preheater.inlet.state.p|preheater.inlet.state.phase|preheater.m_acceleration_0|preheater.m_flow|preheater.m_flowStateSelect|preheater.m_flow_0|preheater.outlet.m_flow|preheater.outlet.r|preheater.outlet.state.T|preheater.outlet.state.d|preheater.outlet.state.h|preheater.outlet.state.p|preheater.outlet.state.phase|preheater.outletSpec|preheater.outletSpec_actual|preheater.outletSpec_prescribed|preheater.outletValueSpec|preheater.p|preheater.p_in|preheater.p_inf|preheater.p_min|preheater.p_out|preheater.q|preheater.rho_in|preheater.rho_out|preheater.singularityRegime|preheater.systemSpec|preheater.u_in|preheater.u_out|preheater.v_in|preheater.v_out|preheater.w_amb|preheater.w_exp|preheater.w_exp_net|pump.L|pump.P|pump.P_nom|pump.TC|pump.adiabaticModel.eta_is|pump.adiabaticModel.h_in|pump.adiabaticModel.h_out|pump.adiabaticModel.h_out_is|pump.adiabaticModel.p_out|pump.adiabaticModel.s_in|pump.adiabaticModel.state_in.T|pump.adiabaticModel.state_in.d|pump.adiabaticModel.state_in.h|pump.adiabaticModel.state_in.p|pump.adiabaticModel.state_in.phase|pump.adiabaticModel.w_t|pump.adiabaticModel.w_t_is|pump.assertionLevel|pump.clip_p_out|pump.dh|pump.dp|pump.dp_fixed|pump.dp_nom|pump.dp_start|pump.dr_corr|pump.etaSpec|pump.eta_actual|pump.eta_fixed|pump.eta_is|pump.h_in|pump.h_out|pump.initM_flow|der.pump.inlet.m_flow.|pump.inlet.m_flow|pump.inlet.r|pump.inlet.state.T|pump.inlet.state.d|pump.inlet.state.h|pump.inlet.state.p|pump.inlet.state.phase|pump.m_acceleration_0|pump.m_flow|pump.m_flowStateSelect|pump.m_flow_0|pump.outlet.m_flow|pump.outlet.r|pump.outlet.state.T|pump.outlet.state.d|pump.outlet.state.h|pump.outlet.state.p|pump.outlet.state.phase|pump.outletSpec|pump.outletSpec_actual|pump.outletSpec_prescribed|pump.outletValueSpec|pump.pRatio|pump.pRatio_fixed|pump.p_in|pump.p_min|pump.p_out|pump.p_out_fixed|pump.singularityRegime|superheater.L|superheater.P|superheater.Q_flow|superheater.T_out_fixed|superheater.assertionLevel|superheater.clip_p_out|superheater.dT|superheater.dT_fixed|superheater.dh|superheater.dh_fixed|superheater.dp|superheater.dr_corr|superheater.du|superheater.h_in|superheater.h_out|superheater.h_out_fixed|superheater.initM_flow|der.superheater.inlet.m_flow.|superheater.inlet.m_flow|superheater.inlet.r|superheater.inlet.state.T|superheater.inlet.state.d|superheater.inlet.state.h|superheater.inlet.state.p|superheater.inlet.state.phase|superheater.m_acceleration_0|superheater.m_flow|superheater.m_flowStateSelect|superheater.m_flow_0|superheater.outlet.m_flow|superheater.outlet.r|superheater.outlet.state.T|superheater.outlet.state.d|superheater.outlet.state.h|superheater.outlet.state.p|superheater.outlet.state.phase|superheater.outletSpec|superheater.outletSpec_actual|superheater.outletSpec_prescribed|superheater.outletValueSpec|superheater.p|superheater.p_in|superheater.p_inf|superheater.p_min|superheater.p_out|superheater.q|superheater.rho_in|superheater.rho_out|superheater.singularityRegime|superheater.systemSpec|superheater.u_in|superheater.u_out|superheater.v_in|superheater.v_out|superheater.w_amb|superheater.w_exp|superheater.w_exp_net|turbine.L|turbine.P|turbine.P_nom|turbine.TC|turbine.adiabaticModel.eta_is|turbine.adiabaticModel.h_in|turbine.adiabaticModel.h_out|turbine.adiabaticModel.h_out_is|turbine.adiabaticModel.p_out|turbine.adiabaticModel.s_in|turbine.adiabaticModel.state_in.T|turbine.adiabaticModel.state_in.d|turbine.adiabaticModel.state_in.h|turbine.adiabaticModel.state_in.p|turbine.adiabaticModel.state_in.phase|turbine.adiabaticModel.w_t|turbine.adiabaticModel.w_t_is|turbine.assertionLevel|turbine.clip_p_out|turbine.dh|turbine.dp|turbine.dp_fixed|turbine.dp_nom|turbine.dp_start|turbine.dr_corr|turbine.etaSpec|turbine.eta_actual|turbine.eta_fixed|turbine.eta_is|turbine.h_in|turbine.h_out|turbine.initM_flow|der.turbine.inlet.m_flow.|turbine.inlet.m_flow|turbine.inlet.r|turbine.inlet.state.T|turbine.inlet.state.d|turbine.inlet.state.h|turbine.inlet.state.p|turbine.inlet.state.phase|turbine.m_acceleration_0|turbine.m_flow|turbine.m_flowStateSelect|turbine.m_flow_0|turbine.outlet.m_flow|turbine.outlet.r|turbine.outlet.state.T|turbine.outlet.state.d|turbine.outlet.state.h|turbine.outlet.state.p|turbine.outlet.state.phase|turbine.outletSpec|turbine.outletSpec_actual|turbine.outletValueSpec|turbine.pRatio|turbine.pRatio_fixed|turbine.p_in|turbine.p_min|turbine.p_out|turbine.p_out_fixed|turbine.singularityRegime|vaporQualitySensor.TC|vaporQualitySensor.digits|vaporQualitySensor.direct_value|vaporQualitySensor.init|vaporQualitySensor.inlet.m_flow|vaporQualitySensor.inlet.r|vaporQualitySensor.inlet.state.T|vaporQualitySensor.inlet.state.d|vaporQualitySensor.inlet.state.h|vaporQualitySensor.inlet.state.p|vaporQualitySensor.inlet.state.phase|vaporQualitySensor.quantity|vaporQualitySensor.value|vaporQualitySensor.value_0|vaporQualitySensor.value_out|vaporQualitySetpoint.y",fileNamePrefix="ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion") [Timeout 660] "Notification: Performance of FrontEnd - loaded program: time 0.001031/0.001031, allocations: 91.86 kB / 0.6443 GB, free: 28.55 MB / 490.7 MB Notification: Performance of FrontEnd - Absyn->SCode: time 0.1374/0.1384, allocations: 88.77 MB / 0.731 GB, free: 3.59 MB / 0.5417 GB Notification: Performance of NFInst.instantiate(ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion): time 0.04285/0.1813, allocations: 66.29 MB / 0.7957 GB, free: 1.082 MB / 0.6042 GB Notification: Performance of NFInst.instExpressions: time 0.02317/0.2045, allocations: 27.49 MB / 0.8225 GB, free: 5.5 MB / 0.6355 GB Notification: Performance of NFInst.updateImplicitVariability: time 0.0009497/0.2054, allocations: 63.38 kB / 0.8226 GB, free: 5.438 MB / 0.6355 GB Notification: Performance of NFTyping.typeComponents: time 0.001459/0.2069, allocations: 0.6905 MB / 0.8233 GB, free: 4.742 MB / 0.6355 GB Notification: Performance of NFTyping.typeBindings: time 0.3444/0.5513, allocations: 7.671 MB / 0.8308 GB, free: 6.578 MB / 0.6355 GB Notification: Performance of NFTyping.typeClassSections: time 0.004258/0.5556, allocations: 2.048 MB / 0.8328 GB, free: 6.574 MB / 0.6355 GB Notification: Performance of NFFlatten.flatten: time 0.002029/0.5576, allocations: 2.125 MB / 0.8348 GB, free: 6.57 MB / 0.6355 GB Notification: Performance of NFFlatten.resolveConnections: time 0.0003595/0.558, allocations: 237.6 kB / 0.8351 GB, free: 6.5 MB / 0.6355 GB Notification: Performance of NFEvalConstants.evaluate: time 0.01275/0.5707, allocations: 8.854 MB / 0.8437 GB, free: 4.129 MB / 0.6355 GB Notification: Performance of NFSimplifyModel.simplify: time 0.001163/0.5719, allocations: 0.6939 MB / 0.8444 GB, free: 4.129 MB / 0.6355 GB Notification: Performance of NFPackage.collectConstants: time 0.0001116/0.572, allocations: 94.47 kB / 0.8445 GB, free: 4.129 MB / 0.6355 GB Notification: Performance of NFFlatten.collectFunctions: time 0.01713/0.5891, allocations: 10.76 MB / 0.855 GB, free: 4.098 MB / 0.6355 GB Notification: Performance of NFScalarize.scalarize: time 0.0002005/0.5893, allocations: 259.5 kB / 0.8552 GB, free: 4.074 MB / 0.6355 GB Notification: Performance of NFVerifyModel.verify: time 0.0005737/0.5899, allocations: 0.6065 MB / 0.8558 GB, free: 3.891 MB / 0.6355 GB Notification: Performance of NFConvertDAE.convert: time 0.01166/0.6016, allocations: 8.259 MB / 0.8639 GB, free: 3.285 MB / 0.6355 GB Notification: Performance of FrontEnd - DAE generated: time 4.518e-06/0.6016, allocations: 0 / 0.8639 GB, free: 3.285 MB / 0.6355 GB Notification: Performance of FrontEnd: time 1.844e-06/0.6016, allocations: 0 / 0.8639 GB, free: 3.285 MB / 0.6355 GB Notification: Performance of Transformations before backend: time 1.742e-05/0.6016, allocations: 0 / 0.8639 GB, free: 3.285 MB / 0.6355 GB Notification: Model statistics after passing the front-end and creating the data structures used by the back-end: * Number of equations: 304 * Number of variables: 304 Notification: Performance of Generate backend data structure: time 0.003888/0.6055, allocations: 2.798 MB / 0.8666 GB, free: 1.93 MB / 0.6355 GB Notification: Performance of prepare preOptimizeDAE: time 3.776e-05/0.6055, allocations: 10.44 kB / 0.8666 GB, free: 1.93 MB / 0.6355 GB Notification: Performance of preOpt normalInlineFunction (simulation): time 0.001091/0.6066, allocations: 375.2 kB / 0.867 GB, free: 1.832 MB / 0.6355 GB Notification: Performance of preOpt evaluateParameters (simulation): time 0.001/0.6076, allocations: 0.8567 MB / 0.8678 GB, free: 1.48 MB / 0.6355 GB Notification: Performance of preOpt simplifyIfEquations (simulation): time 0.0001215/0.6077, allocations: 199.2 kB / 0.868 GB, free: 1.352 MB / 0.6355 GB Notification: Performance of preOpt expandDerOperator (simulation): time 0.0001041/0.6078, allocations: 120.9 kB / 0.8681 GB, free: 1.348 MB / 0.6355 GB Notification: Performance of preOpt clockPartitioning (simulation): time 0.001652/0.6095, allocations: 1.49 MB / 0.8696 GB, free: 0.9141 MB / 0.6355 GB Notification: Performance of preOpt findStateOrder (simulation): time 2.221e-05/0.6095, allocations: 6.969 kB / 0.8696 GB, free: 0.9141 MB / 0.6355 GB Notification: Performance of preOpt replaceEdgeChange (simulation): time 6.261e-05/0.6096, allocations: 50.97 kB / 0.8696 GB, free: 0.9141 MB / 0.6355 GB Notification: Performance of preOpt inlineArrayEqn (simulation): time 1.689e-05/0.6096, allocations: 28.94 kB / 0.8697 GB, free: 0.9141 MB / 0.6355 GB Notification: Performance of preOpt removeEqualRHS (simulation): time 0.001411/0.611, allocations: 1.018 MB / 0.8707 GB, free: 0.8945 MB / 0.6355 GB Warning: The model contains alias variables with redundant start and/or conflicting nominal values. It is recommended to resolve the conflicts, because otherwise the system could be hard to solve. To print the conflicting alias sets and the chosen candidates please use -d=aliasConflicts. Notification: Performance of preOpt removeSimpleEquations (simulation): time 0.003607/0.6146, allocations: 4.832 MB / 0.8754 GB, free: 13.87 MB / 0.6511 GB Notification: Performance of preOpt comSubExp (simulation): time 0.001252/0.6158, allocations: 0.8389 MB / 0.8762 GB, free: 13.71 MB / 0.6511 GB Notification: Performance of preOpt resolveLoops (simulation): time 0.0004165/0.6163, allocations: 374.3 kB / 0.8766 GB, free: 13.66 MB / 0.6511 GB Notification: Performance of preOpt evalFunc (simulation): time 0.06365/0.6799, allocations: 36.47 MB / 0.9122 GB, free: 3.809 MB / 0.6667 GB Notification: Performance of preOpt encapsulateWhenConditions (simulation): time 5.071e-05/0.68, allocations: 41.12 kB / 0.9122 GB, free: 3.766 MB / 0.6667 GB Notification: Performance of pre-optimization done (n=85): time 3.166e-06/0.68, allocations: 0 / 0.9122 GB, free: 3.766 MB / 0.6667 GB Notification: Performance of matching and sorting (n=85): time 0.003107/0.6831, allocations: 1.386 MB / 0.9136 GB, free: 2.695 MB / 0.6667 GB Notification: Performance of inlineWhenForInitialization (initialization): time 4.896e-05/0.6831, allocations: 95.7 kB / 0.9137 GB, free: 2.59 MB / 0.6667 GB Notification: Performance of selectInitializationVariablesDAE (initialization): time 0.0007819/0.6839, allocations: 0.8413 MB / 0.9145 GB, free: 1.914 MB / 0.6667 GB Notification: Performance of collectPreVariables (initialization): time 3.618e-05/0.6839, allocations: 44.42 kB / 0.9145 GB, free: 1.879 MB / 0.6667 GB Notification: Performance of collectInitialEqns (initialization): time 0.0003174/0.6843, allocations: 0.6464 MB / 0.9152 GB, free: 1.434 MB / 0.6667 GB Notification: Performance of collectInitialBindings (initialization): time 0.0001568/0.6844, allocations: 313.4 kB / 0.9155 GB, free: 1.172 MB / 0.6667 GB Notification: Performance of simplifyInitialFunctions (initialization): time 0.0001692/0.6846, allocations: 194 kB / 0.9156 GB, free: 1.047 MB / 0.6667 GB Notification: Performance of setup shared object (initialization): time 0.0001027/0.6847, allocations: 341.9 kB / 0.916 GB, free: 0.707 MB / 0.6667 GB Notification: Performance of preBalanceInitialSystem (initialization): time 0.0003225/0.685, allocations: 249.9 kB / 0.9162 GB, free: 472 kB / 0.6667 GB Notification: Performance of partitionIndependentBlocks (initialization): time 0.0004899/0.6855, allocations: 0.573 MB / 0.9168 GB, free: 15.75 MB / 0.6823 GB Notification: Performance of analyzeInitialSystem (initialization): time 0.0008355/0.6863, allocations: 0.8592 MB / 0.9176 GB, free: 14.81 MB / 0.6823 GB Notification: Performance of solveInitialSystemEqSystem (initialization): time 5.239e-06/0.6863, allocations: 4 kB / 0.9176 GB, free: 14.8 MB / 0.6823 GB Notification: Performance of matching and sorting (n=126) (initialization): time 0.001065/0.6874, allocations: 1.002 MB / 0.9186 GB, free: 13.84 MB / 0.6823 GB Notification: Performance of prepare postOptimizeDAE: time 1.989e-05/0.6874, allocations: 8.188 kB / 0.9186 GB, free: 13.84 MB / 0.6823 GB Notification: Performance of postOpt simplifyComplexFunction (initialization): time 1.222e-05/0.6874, allocations: 16 kB / 0.9186 GB, free: 13.82 MB / 0.6823 GB Notification: Performance of postOpt tearingSystem (initialization): time 0.0005554/0.688, allocations: 147.1 kB / 0.9187 GB, free: 13.68 MB / 0.6823 GB Notification: Performance of postOpt solveSimpleEquations (initialization): time 0.0004188/0.6884, allocations: 216.8 kB / 0.919 GB, free: 13.48 MB / 0.6823 GB Notification: Performance of postOpt calculateStrongComponentJacobians (initialization): time 0.00101/0.6894, allocations: 1.72 MB / 0.9206 GB, free: 11.69 MB / 0.6823 GB Notification: Performance of postOpt simplifyAllExpressions (initialization): time 0.0004082/0.6898, allocations: 115.5 kB / 0.9207 GB, free: 11.58 MB / 0.6823 GB Notification: Performance of postOpt collapseArrayExpressions (initialization): time 4.626e-05/0.6899, allocations: 47.94 kB / 0.9208 GB, free: 11.53 MB / 0.6823 GB Notification: Model statistics after passing the back-end for initialization: * Number of independent subsystems: 42 * Number of states: 0 () * Number of discrete variables: 7 (superheater.outlet.state.phase,loopBreaker.outlet.state.phase,turbine.outlet.state.phase,condenser.outlet.state.phase,preheater.outlet.state.phase,boiler.outlet.state.phase,pump.outlet.state.phase) * Number of discrete states: 0 () * Number of clocked states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for initialization (120): * Single equations (assignments): 117 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 0 * When equations: 0 * If-equations: 0 * Equation systems (not torn): 1 * Torn equation systems: 2 * Mixed (continuous/discrete) equation systems: 0 Notification: Equation system details (not torn): * Constant Jacobian (size): 0 systems * Linear Jacobian (size,density): 0 systems * Non-linear Jacobian (size): 1 system {1} * Without analytic Jacobian (size): 0 systems Notification: Torn system details for strict tearing set: * Linear torn systems (#iteration vars, #inner vars, density): 0 systems * Non-linear torn systems (#iteration vars, #inner vars): 2 systems {(1,4), (1,2)} Notification: Performance of prepare postOptimizeDAE: time 0.0003404/0.6902, allocations: 271.5 kB / 0.9211 GB, free: 11.27 MB / 0.6823 GB Notification: Performance of postOpt lateInlineFunction (simulation): time 9.929e-05/0.6903, allocations: 123.1 kB / 0.9212 GB, free: 11.15 MB / 0.6823 GB Notification: Performance of postOpt wrapFunctionCalls (simulation): time 0.00228/0.6926, allocations: 3.074 MB / 0.9242 GB, free: 8.105 MB / 0.6823 GB Notification: Performance of postOpt inlineArrayEqn (simulation): time 2.367e-05/0.6926, allocations: 31.95 kB / 0.9242 GB, free: 8.074 MB / 0.6823 GB Notification: Performance of postOpt constantLinearSystem (simulation): time 7.384e-06/0.6926, allocations: 7.938 kB / 0.9242 GB, free: 8.066 MB / 0.6823 GB Notification: Performance of postOpt simplifysemiLinear (simulation): time 9.167e-06/0.6926, allocations: 7.969 kB / 0.9242 GB, free: 8.059 MB / 0.6823 GB Notification: Performance of postOpt removeSimpleEquations (simulation): time 0.003571/0.6962, allocations: 4.205 MB / 0.9283 GB, free: 3.867 MB / 0.6823 GB Notification: Performance of postOpt simplifyComplexFunction (simulation): time 7.364e-06/0.6962, allocations: 3.078 kB / 0.9283 GB, free: 3.867 MB / 0.6823 GB Notification: Performance of postOpt solveSimpleEquations (simulation): time 0.0002812/0.6965, allocations: 134.6 kB / 0.9285 GB, free: 3.742 MB / 0.6823 GB Notification: Performance of postOpt tearingSystem (simulation): time 0.0006603/0.6972, allocations: 0.63 MB / 0.9291 GB, free: 3.113 MB / 0.6823 GB Notification: Performance of postOpt inputDerivativesUsed (simulation): time 3.209e-05/0.6972, allocations: 20 kB / 0.9291 GB, free: 3.094 MB / 0.6823 GB Notification: Performance of postOpt calculateStrongComponentJacobians (simulation): time 0.0009817/0.6982, allocations: 2.313 MB / 0.9313 GB, free: 0.7031 MB / 0.6823 GB Notification: Performance of postOpt calculateStateSetsJacobians (simulation): time 2.244e-06/0.6982, allocations: 3.984 kB / 0.9314 GB, free: 0.6992 MB / 0.6823 GB Notification: Performance of postOpt symbolicJacobian (simulation): time 0.002328/0.7005, allocations: 2.984 MB / 0.9343 GB, free: 13.73 MB / 0.698 GB Notification: Performance of postOpt removeConstants (simulation): time 0.0002525/0.7008, allocations: 234.3 kB / 0.9345 GB, free: 13.5 MB / 0.698 GB Notification: Performance of postOpt simplifyTimeIndepFuncCalls (simulation): time 7.542e-05/0.7008, allocations: 43.89 kB / 0.9345 GB, free: 13.46 MB / 0.698 GB Notification: Performance of postOpt simplifyAllExpressions (simulation): time 0.000211/0.701, allocations: 31.98 kB / 0.9346 GB, free: 13.43 MB / 0.698 GB Notification: Performance of postOpt findZeroCrossings (simulation): time 7.842e-05/0.7011, allocations: 60.88 kB / 0.9346 GB, free: 13.37 MB / 0.698 GB Notification: Performance of postOpt collapseArrayExpressions (simulation): time 2.63e-05/0.7011, allocations: 23.98 kB / 0.9346 GB, free: 13.35 MB / 0.698 GB Notification: Performance of sorting global known variables: time 0.0008005/0.7019, allocations: 0.6272 MB / 0.9353 GB, free: 12.71 MB / 0.698 GB Notification: Performance of sort global known variables: time 8e-08/0.7019, allocations: 0 / 0.9353 GB, free: 12.71 MB / 0.698 GB Notification: Performance of remove unused functions: time 0.004833/0.7068, allocations: 1.874 MB / 0.9371 GB, free: 10.84 MB / 0.698 GB Notification: Model statistics after passing the back-end for simulation: * Number of independent subsystems: 1 * Number of states: 1 (firstOrder.y) * Number of discrete variables: 18 ($cse1.phase,$cse1.region,$cse2.phase,$cse2.region,$cse3.phase,$cse3.region,$cse4.phase,$cse4.region,$cse5.phase,$cse5.region,$cse6.phase,$cse6.region,$cse9.phase,$cse9.region,$cse10.phase,$cse10.region,$cse11.region3boundary,$cse13.region3boundary) * Number of discrete states: 0 () * Number of clocked states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for simulation (87): * Single equations (assignments): 76 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 8 * When equations: 0 * If-equations: 0 * Equation systems (not torn): 0 * Torn equation systems: 3 * Mixed (continuous/discrete) equation systems: 0 Notification: Torn system details for strict tearing set: * Linear torn systems (#iteration vars, #inner vars, density): 0 systems * Non-linear torn systems (#iteration vars, #inner vars): 3 systems {(1,1), (1,5), (1,3)} Notification: Performance of Backend phase and start with SimCode phase: time 0.004124/0.7109, allocations: 2.06 MB / 0.9391 GB, free: 8.961 MB / 0.698 GB Notification: Performance of simCode: created initialization part: time 0.001142/0.712, allocations: 1.006 MB / 0.9401 GB, free: 7.992 MB / 0.698 GB Notification: Performance of simCode: created event and clocks part: time 2.545e-06/0.712, allocations: 0 / 0.9401 GB, free: 7.992 MB / 0.698 GB Notification: Performance of simCode: created simulation system equations: time 0.0005509/0.7126, allocations: 0.6131 MB / 0.9407 GB, free: 7.398 MB / 0.698 GB Notification: Performance of simCode: created of all other equations (e.g. parameter, nominal, assert, etc): time 0.001443/0.714, allocations: 0.6178 MB / 0.9413 GB, free: 6.832 MB / 0.698 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 0.003417/0.7175, allocations: 3.087 MB / 0.9443 GB, free: 3.723 MB / 0.698 GB Notification: Performance of simCode: some other stuff during SimCode phase: time 0.0004472/0.7179, allocations: 0.7313 MB / 0.945 GB, free: 2.949 MB / 0.698 GB Notification: Performance of simCode: all other stuff during SimCode phase: time 0.0001556/0.7181, allocations: 106.4 kB / 0.9451 GB, free: 2.848 MB / 0.698 GB Notification: Performance of SimCode: time 4.91e-07/0.7181, allocations: 0 / 0.9451 GB, free: 2.848 MB / 0.698 GB Notification: Performance of Templates: time 0.05991/0.778, allocations: 67.47 MB / 1.011 GB, free: 15.53 MB / 0.7761 GB " [Timeout remaining time 659] make -j1 -f ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion.makefile [Timeout 660] (rm -f ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion.pipe ; mkfifo ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion.pipe ; head -c 1048576 < ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion.pipe >> ../files/ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion.sim & ./ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion -emit_protected > ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion.pipe 2>&1) [Timeout 1200] diffSimulationResults("ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat","/mnt/ReferenceFiles/ThermofluidStream-main-regression/ReferenceData/ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_ref.mat","/var/lib/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.dh_fixed in file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable boiler.dh_fixed from file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable boiler.du in file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable boiler.du from file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable boiler.h_out_fixed in file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable boiler.h_out_fixed from file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable boiler.p_inf in file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable boiler.p_inf from file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable boiler.u_in in file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable boiler.u_in from file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable boiler.u_out in file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable boiler.u_out from file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable boiler.v_in in file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable boiler.v_in from file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable boiler.v_out in file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable boiler.v_out from file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable boiler.w_amb in file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable boiler.w_amb from file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable boiler.w_exp in file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable boiler.w_exp from file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable boiler.w_exp_net in file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable boiler.w_exp_net from file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable condenser.P in file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable condenser.P from file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable condenser.assertionLevel in file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable condenser.assertionLevel from file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable condenser.dh_fixed in file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable condenser.dh_fixed from file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable condenser.du in file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable condenser.du from file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable condenser.h_out_fixed in file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable condenser.h_out_fixed from file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable condenser.p_inf in file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable condenser.p_inf from file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable condenser.u_in in file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable condenser.u_in from file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable condenser.u_out in file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable condenser.u_out from file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable condenser.v_in in file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable condenser.v_in from file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable condenser.v_out in file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable condenser.v_out from file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable condenser.w_amb in file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable condenser.w_amb from file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable condenser.w_exp in file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable condenser.w_exp from file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable condenser.w_exp_net in file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable condenser.w_exp_net from file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable dropOfCommons.instanceNameColor[1] in file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable dropOfCommons.instanceNameColor[1] from file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable dropOfCommons.instanceNameColor[2] in file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable dropOfCommons.instanceNameColor[2] from file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable dropOfCommons.instanceNameColor[3] in file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable dropOfCommons.instanceNameColor[3] from file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable loopBreaker.h_out_fixed in file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable loopBreaker.h_out_fixed from file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable loopBreaker.m_flow_in_par in file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable loopBreaker.m_flow_in_par from file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable preheater.P in file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable preheater.P from file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable preheater.T_out_fixed in file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable preheater.T_out_fixed from file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable preheater.assertionLevel in file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable preheater.assertionLevel from file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable preheater.dh_fixed in file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable preheater.dh_fixed from file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable preheater.du in file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable preheater.du from file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable preheater.h_out_fixed in file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable preheater.h_out_fixed from file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable preheater.p_inf in file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable preheater.p_inf from file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable preheater.rho_out in file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable preheater.rho_out from file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable preheater.u_in in file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable preheater.u_in from file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable preheater.u_out in file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable preheater.u_out from file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable preheater.v_in in file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable preheater.v_in from file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable preheater.v_out in file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable preheater.v_out from file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable preheater.w_amb in file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable preheater.w_amb from file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable preheater.w_exp in file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable preheater.w_exp from file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable preheater.w_exp_net in file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable preheater.w_exp_net from file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable pump.P_nom in file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable pump.P_nom from file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable pump.TC in file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable pump.TC from file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable pump.assertionLevel in file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable pump.assertionLevel from file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable pump.dp_fixed in file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable pump.dp_fixed from file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable pump.dp_nom in file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable pump.dp_nom from file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable pump.dp_start in file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable pump.dp_start from file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable pump.pRatio_fixed in file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable pump.pRatio_fixed from file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable pump.p_out_fixed in file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable pump.p_out_fixed from file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable superheater.P in file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable superheater.P from file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable superheater.T_out_fixed in file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable superheater.T_out_fixed from file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable superheater.assertionLevel in file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable superheater.assertionLevel from file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable superheater.dh_fixed in file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable superheater.dh_fixed from file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable superheater.du in file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable superheater.du from file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable superheater.h_out_fixed in file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable superheater.h_out_fixed from file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable superheater.p_inf in file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable superheater.p_inf from file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable superheater.rho_in in file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable superheater.rho_in 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.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.singularityRegime,boiler.systemSpec,condenser.L,condenser.Q_flow,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.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.showNumber,efficiencyExtensive.significantDigits,efficiencySpecific.displayVariablefinal,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_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.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.singularityRegime,preheater.systemSpec,pump.L,pump.P,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.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.singularityRegime,superheater.systemSpec,time,turbine.L,turbine.P,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: 11.429141515865922]