Running: ./testmodel.py --libraries=/home/hudson/saved_omc/libraries/.openmodelica/libraries --ompython_omhome=/usr ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion.conf.json loadFile("/home/hudson/saved_omc/libraries/.openmodelica/libraries/ModelicaServices 4.1.0+maint.om/package.mo", uses=false) [Timeout 180] "Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/ModelicaServices 4.1.0+maint.om/package.mo): time 0.0008274/0.0008274, allocations: 76.5 kB / 19.93 MB, free: 4.633 MB / 18.57 MB " [Timeout remaining time 180] loadFile("/home/hudson/saved_omc/libraries/.openmodelica/libraries/Complex 4.1.0+maint.om/package.mo", uses=false) [Timeout 180] "Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/Complex 4.1.0+maint.om/package.mo): time 0.0008556/0.0008556, allocations: 173.9 kB / 23.21 MB, free: 1.352 MB / 18.57 MB " [Timeout remaining time 180] loadFile("/home/hudson/saved_omc/libraries/.openmodelica/libraries/Modelica 4.1.0+maint.om/package.mo", uses=false) [Timeout 180] "Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/Modelica 4.1.0+maint.om/package.mo): time 0.851/0.851, allocations: 177.1 MB / 203.5 MB, free: 5.742 MB / 186.7 MB " [Timeout remaining time 179] loadFile("/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermofluidStream main/package.mo", uses=false) [Timeout 180] "Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermofluidStream main/package.mo): time 0.5981/0.5981, allocations: 116 MB / 376 MB, free: 4.176 MB / 346.7 MB " [Timeout remaining time 179] Using package ThermofluidStream with version 1.3.0 (/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermofluidStream main/package.mo) Using package Modelica with version 4.1.0 (/home/hudson/saved_omc/libraries/.openmodelica/libraries/Modelica 4.1.0+maint.om/package.mo) Using package Complex with version 4.1.0 (/home/hudson/saved_omc/libraries/.openmodelica/libraries/Complex 4.1.0+maint.om/package.mo) Using package ModelicaServices with version 4.1.0 (/home/hudson/saved_omc/libraries/.openmodelica/libraries/ModelicaServices 4.1.0+maint.om/package.mo) Running command: translateModel(ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion,tolerance=1e-06,outputFormat="mat",numberOfIntervals=100,variableFilter="CPUtime|EventCounter|NonlinearSystems.initialization.1..Calls|NonlinearSystems.initialization.1..Iterations|NonlinearSystems.initialization.1..Jacobians|NonlinearSystems.initialization.1..Residues|NonlinearSystems.simulation.1..Calls|NonlinearSystems.simulation.1..Iterations|NonlinearSystems.simulation.1..Jacobians|NonlinearSystems.simulation.1..Residues|NonlinearSystems.simulation.2..Calls|NonlinearSystems.simulation.2..Iterations|NonlinearSystems.simulation.2..Jacobians|NonlinearSystems.simulation.2..Residues|Time|boiler.L|boiler.P|boiler.Q_flow|boiler.T_out_fixed|boiler.assertionLevel|boiler.clip_p_out|boiler.dT|boiler.dT_fixed|boiler.dh|boiler.dh_fixed|boiler.dp|boiler.dr_corr|boiler.du|boiler.h_in|boiler.h_out|boiler.h_out_fixed|boiler.initM_flow|der.boiler.inlet.m_flow.|boiler.inlet.m_flow|boiler.inlet.r|boiler.inlet.state.T|boiler.inlet.state.d|boiler.inlet.state.h|boiler.inlet.state.p|boiler.inlet.state.phase|boiler.m_acceleration_0|boiler.m_flow|boiler.m_flowStateSelect|boiler.m_flow_0|boiler.outlet.m_flow|boiler.outlet.r|boiler.outlet.state.T|boiler.outlet.state.d|boiler.outlet.state.h|boiler.outlet.state.p|boiler.outlet.state.phase|boiler.outletSpec|boiler.outletSpec_actual|boiler.outletSpec_prescribed|boiler.outletValueSpec|boiler.p|boiler.p_in|boiler.p_inf|boiler.p_min|boiler.p_out|boiler.q|boiler.rho_in|boiler.rho_out|boiler.singularityRegime|boiler.systemSpec|boiler.u_in|boiler.u_out|boiler.v_in|boiler.v_out|boiler.w_amb|boiler.w_exp|boiler.w_exp_net|condenser.L|condenser.P|condenser.Q_flow|condenser.T_out_fixed|condenser.assertionLevel|condenser.clip_p_out|condenser.dT|condenser.dT_fixed|condenser.dh|condenser.dh_fixed|condenser.dp|condenser.dr_corr|condenser.du|condenser.h_in|condenser.h_out|condenser.h_out_fixed|condenser.initM_flow|der.condenser.inlet.m_flow.|condenser.inlet.m_flow|condenser.inlet.r|condenser.inlet.state.T|condenser.inlet.state.d|condenser.inlet.state.h|condenser.inlet.state.p|condenser.inlet.state.phase|condenser.m_acceleration_0|condenser.m_flow|condenser.m_flowStateSelect|condenser.m_flow_0|condenser.outlet.m_flow|condenser.outlet.r|condenser.outlet.state.T|condenser.outlet.state.d|condenser.outlet.state.h|condenser.outlet.state.p|condenser.outlet.state.phase|condenser.outletSpec|condenser.outletSpec_actual|condenser.outletValueSpec|condenser.p|condenser.p_in|condenser.p_inf|condenser.p_min|condenser.p_out|condenser.q|condenser.rho_in|condenser.rho_out|condenser.singularityRegime|condenser.systemSpec|condenser.u_in|condenser.u_out|condenser.v_in|condenser.v_out|condenser.w_amb|condenser.w_exp|condenser.w_exp_net|dropOfCommons.L|dropOfCommons.assertionLevel|dropOfCommons.g|dropOfCommons.instanceNameColor.1.|dropOfCommons.instanceNameColor.2.|dropOfCommons.instanceNameColor.3.|dropOfCommons.k_volume_damping|dropOfCommons.m_flow_reg|dropOfCommons.omega_reg|dropOfCommons.p_min|dropOfCommons.rho_min|efficiencyExtensive.displayVariablefinal|efficiencyExtensive.showNumber|efficiencyExtensive.significantDigits|efficiencySpecific.displayVariablefinal|efficiencySpecific.showNumber|efficiencySpecific.significantDigits|firstOrder.T|der.firstOrder.y.|firstOrder.initType|firstOrder.k|firstOrder.u|firstOrder.y|firstOrder.y_start|h_bubble.y|h_dew.y|inverseBlockConstraints.u1|inverseBlockConstraints.u2|inverseBlockConstraints.y1|inverseBlockConstraints.y2|loopBreaker.L|loopBreaker.T_out|loopBreaker.T_out_fixed|loopBreaker.XiSpec|loopBreaker.assertionLevel|loopBreaker.dh|loopBreaker.dm_flow|loopBreaker.dp|loopBreaker.h_out|loopBreaker.h_out_fixed|loopBreaker.inlet.m_flow|loopBreaker.inlet.r|loopBreaker.inlet.state.T|loopBreaker.inlet.state.d|loopBreaker.inlet.state.h|loopBreaker.inlet.state.p|loopBreaker.inlet.state.phase|loopBreaker.m_flowSpec|loopBreaker.m_flow_in|loopBreaker.m_flow_in_par|loopBreaker.m_flow_in_prescribed|der.loopBreaker.outlet.m_flow.|loopBreaker.outlet.m_flow|loopBreaker.outlet.r|loopBreaker.outlet.state.T|loopBreaker.outlet.state.d|loopBreaker.outlet.state.h|loopBreaker.outlet.state.p|loopBreaker.outlet.state.phase|loopBreaker.pSpec|loopBreaker.p_out|loopBreaker.p_out_fixed|loopBreaker.thermalSpec|loopBreaker.thermalValueSpec|loopBreaker.tol_Xi|loopBreaker.tol_h|loopBreaker.tol_m_flow|loopBreaker.tol_p|massFlowRate.height|massFlowRate.offset|massFlowRate.startTime|massFlowRate.y|outletPressure.duration|outletPressure.height|outletPressure.offset|outletPressure.startTime|outletPressure.y|preheater.L|preheater.P|preheater.Q_flow|preheater.T_out_fixed|preheater.assertionLevel|preheater.clip_p_out|preheater.dT|preheater.dT_fixed|preheater.dh|preheater.dh_fixed|preheater.dp|preheater.dr_corr|preheater.du|preheater.h_in|preheater.h_out|preheater.h_out_fixed|preheater.initM_flow|der.preheater.inlet.m_flow.|preheater.inlet.m_flow|preheater.inlet.r|preheater.inlet.state.T|preheater.inlet.state.d|preheater.inlet.state.h|preheater.inlet.state.p|preheater.inlet.state.phase|preheater.m_acceleration_0|preheater.m_flow|preheater.m_flowStateSelect|preheater.m_flow_0|preheater.outlet.m_flow|preheater.outlet.r|preheater.outlet.state.T|preheater.outlet.state.d|preheater.outlet.state.h|preheater.outlet.state.p|preheater.outlet.state.phase|preheater.outletSpec|preheater.outletSpec_actual|preheater.outletSpec_prescribed|preheater.outletValueSpec|preheater.p|preheater.p_in|preheater.p_inf|preheater.p_min|preheater.p_out|preheater.q|preheater.rho_in|preheater.rho_out|preheater.singularityRegime|preheater.systemSpec|preheater.u_in|preheater.u_out|preheater.v_in|preheater.v_out|preheater.w_amb|preheater.w_exp|preheater.w_exp_net|pump.L|pump.P|pump.P_nom|pump.TC|pump.adiabaticModel.eta_is|pump.adiabaticModel.h_in|pump.adiabaticModel.h_out|pump.adiabaticModel.h_out_is|pump.adiabaticModel.p_out|pump.adiabaticModel.s_in|pump.adiabaticModel.state_in.T|pump.adiabaticModel.state_in.d|pump.adiabaticModel.state_in.h|pump.adiabaticModel.state_in.p|pump.adiabaticModel.state_in.phase|pump.adiabaticModel.w_t|pump.adiabaticModel.w_t_is|pump.assertionLevel|pump.clip_p_out|pump.dh|pump.dp|pump.dp_fixed|pump.dp_nom|pump.dp_start|pump.dr_corr|pump.etaSpec|pump.eta_actual|pump.eta_fixed|pump.eta_is|pump.h_in|pump.h_out|pump.initM_flow|der.pump.inlet.m_flow.|pump.inlet.m_flow|pump.inlet.r|pump.inlet.state.T|pump.inlet.state.d|pump.inlet.state.h|pump.inlet.state.p|pump.inlet.state.phase|pump.m_acceleration_0|pump.m_flow|pump.m_flowStateSelect|pump.m_flow_0|pump.outlet.m_flow|pump.outlet.r|pump.outlet.state.T|pump.outlet.state.d|pump.outlet.state.h|pump.outlet.state.p|pump.outlet.state.phase|pump.outletSpec|pump.outletSpec_actual|pump.outletSpec_prescribed|pump.outletValueSpec|pump.pRatio|pump.pRatio_fixed|pump.p_in|pump.p_min|pump.p_out|pump.p_out_fixed|pump.singularityRegime|superheater.L|superheater.P|superheater.Q_flow|superheater.T_out_fixed|superheater.assertionLevel|superheater.clip_p_out|superheater.dT|superheater.dT_fixed|superheater.dh|superheater.dh_fixed|superheater.dp|superheater.dr_corr|superheater.du|superheater.h_in|superheater.h_out|superheater.h_out_fixed|superheater.initM_flow|der.superheater.inlet.m_flow.|superheater.inlet.m_flow|superheater.inlet.r|superheater.inlet.state.T|superheater.inlet.state.d|superheater.inlet.state.h|superheater.inlet.state.p|superheater.inlet.state.phase|superheater.m_acceleration_0|superheater.m_flow|superheater.m_flowStateSelect|superheater.m_flow_0|superheater.outlet.m_flow|superheater.outlet.r|superheater.outlet.state.T|superheater.outlet.state.d|superheater.outlet.state.h|superheater.outlet.state.p|superheater.outlet.state.phase|superheater.outletSpec|superheater.outletSpec_actual|superheater.outletSpec_prescribed|superheater.outletValueSpec|superheater.p|superheater.p_in|superheater.p_inf|superheater.p_min|superheater.p_out|superheater.q|superheater.rho_in|superheater.rho_out|superheater.singularityRegime|superheater.systemSpec|superheater.u_in|superheater.u_out|superheater.v_in|superheater.v_out|superheater.w_amb|superheater.w_exp|superheater.w_exp_net|turbine.L|turbine.P|turbine.P_nom|turbine.TC|turbine.adiabaticModel.eta_is|turbine.adiabaticModel.h_in|turbine.adiabaticModel.h_out|turbine.adiabaticModel.h_out_is|turbine.adiabaticModel.p_out|turbine.adiabaticModel.s_in|turbine.adiabaticModel.state_in.T|turbine.adiabaticModel.state_in.d|turbine.adiabaticModel.state_in.h|turbine.adiabaticModel.state_in.p|turbine.adiabaticModel.state_in.phase|turbine.adiabaticModel.w_t|turbine.adiabaticModel.w_t_is|turbine.assertionLevel|turbine.clip_p_out|turbine.dh|turbine.dp|turbine.dp_fixed|turbine.dp_nom|turbine.dp_start|turbine.dr_corr|turbine.etaSpec|turbine.eta_actual|turbine.eta_fixed|turbine.eta_is|turbine.h_in|turbine.h_out|turbine.initM_flow|der.turbine.inlet.m_flow.|turbine.inlet.m_flow|turbine.inlet.r|turbine.inlet.state.T|turbine.inlet.state.d|turbine.inlet.state.h|turbine.inlet.state.p|turbine.inlet.state.phase|turbine.m_acceleration_0|turbine.m_flow|turbine.m_flowStateSelect|turbine.m_flow_0|turbine.outlet.m_flow|turbine.outlet.r|turbine.outlet.state.T|turbine.outlet.state.d|turbine.outlet.state.h|turbine.outlet.state.p|turbine.outlet.state.phase|turbine.outletSpec|turbine.outletSpec_actual|turbine.outletValueSpec|turbine.pRatio|turbine.pRatio_fixed|turbine.p_in|turbine.p_min|turbine.p_out|turbine.p_out_fixed|turbine.singularityRegime|vaporQualitySensor.TC|vaporQualitySensor.digits|vaporQualitySensor.direct_value|vaporQualitySensor.init|vaporQualitySensor.inlet.m_flow|vaporQualitySensor.inlet.r|vaporQualitySensor.inlet.state.T|vaporQualitySensor.inlet.state.d|vaporQualitySensor.inlet.state.h|vaporQualitySensor.inlet.state.p|vaporQualitySensor.inlet.state.phase|vaporQualitySensor.quantity|vaporQualitySensor.value|vaporQualitySensor.value_0|vaporQualitySensor.value_out|vaporQualitySetpoint.y",fileNamePrefix="ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion") translateModel(ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion,tolerance=1e-06,outputFormat="mat",numberOfIntervals=100,variableFilter="CPUtime|EventCounter|NonlinearSystems.initialization.1..Calls|NonlinearSystems.initialization.1..Iterations|NonlinearSystems.initialization.1..Jacobians|NonlinearSystems.initialization.1..Residues|NonlinearSystems.simulation.1..Calls|NonlinearSystems.simulation.1..Iterations|NonlinearSystems.simulation.1..Jacobians|NonlinearSystems.simulation.1..Residues|NonlinearSystems.simulation.2..Calls|NonlinearSystems.simulation.2..Iterations|NonlinearSystems.simulation.2..Jacobians|NonlinearSystems.simulation.2..Residues|Time|boiler.L|boiler.P|boiler.Q_flow|boiler.T_out_fixed|boiler.assertionLevel|boiler.clip_p_out|boiler.dT|boiler.dT_fixed|boiler.dh|boiler.dh_fixed|boiler.dp|boiler.dr_corr|boiler.du|boiler.h_in|boiler.h_out|boiler.h_out_fixed|boiler.initM_flow|der.boiler.inlet.m_flow.|boiler.inlet.m_flow|boiler.inlet.r|boiler.inlet.state.T|boiler.inlet.state.d|boiler.inlet.state.h|boiler.inlet.state.p|boiler.inlet.state.phase|boiler.m_acceleration_0|boiler.m_flow|boiler.m_flowStateSelect|boiler.m_flow_0|boiler.outlet.m_flow|boiler.outlet.r|boiler.outlet.state.T|boiler.outlet.state.d|boiler.outlet.state.h|boiler.outlet.state.p|boiler.outlet.state.phase|boiler.outletSpec|boiler.outletSpec_actual|boiler.outletSpec_prescribed|boiler.outletValueSpec|boiler.p|boiler.p_in|boiler.p_inf|boiler.p_min|boiler.p_out|boiler.q|boiler.rho_in|boiler.rho_out|boiler.singularityRegime|boiler.systemSpec|boiler.u_in|boiler.u_out|boiler.v_in|boiler.v_out|boiler.w_amb|boiler.w_exp|boiler.w_exp_net|condenser.L|condenser.P|condenser.Q_flow|condenser.T_out_fixed|condenser.assertionLevel|condenser.clip_p_out|condenser.dT|condenser.dT_fixed|condenser.dh|condenser.dh_fixed|condenser.dp|condenser.dr_corr|condenser.du|condenser.h_in|condenser.h_out|condenser.h_out_fixed|condenser.initM_flow|der.condenser.inlet.m_flow.|condenser.inlet.m_flow|condenser.inlet.r|condenser.inlet.state.T|condenser.inlet.state.d|condenser.inlet.state.h|condenser.inlet.state.p|condenser.inlet.state.phase|condenser.m_acceleration_0|condenser.m_flow|condenser.m_flowStateSelect|condenser.m_flow_0|condenser.outlet.m_flow|condenser.outlet.r|condenser.outlet.state.T|condenser.outlet.state.d|condenser.outlet.state.h|condenser.outlet.state.p|condenser.outlet.state.phase|condenser.outletSpec|condenser.outletSpec_actual|condenser.outletValueSpec|condenser.p|condenser.p_in|condenser.p_inf|condenser.p_min|condenser.p_out|condenser.q|condenser.rho_in|condenser.rho_out|condenser.singularityRegime|condenser.systemSpec|condenser.u_in|condenser.u_out|condenser.v_in|condenser.v_out|condenser.w_amb|condenser.w_exp|condenser.w_exp_net|dropOfCommons.L|dropOfCommons.assertionLevel|dropOfCommons.g|dropOfCommons.instanceNameColor.1.|dropOfCommons.instanceNameColor.2.|dropOfCommons.instanceNameColor.3.|dropOfCommons.k_volume_damping|dropOfCommons.m_flow_reg|dropOfCommons.omega_reg|dropOfCommons.p_min|dropOfCommons.rho_min|efficiencyExtensive.displayVariablefinal|efficiencyExtensive.showNumber|efficiencyExtensive.significantDigits|efficiencySpecific.displayVariablefinal|efficiencySpecific.showNumber|efficiencySpecific.significantDigits|firstOrder.T|der.firstOrder.y.|firstOrder.initType|firstOrder.k|firstOrder.u|firstOrder.y|firstOrder.y_start|h_bubble.y|h_dew.y|inverseBlockConstraints.u1|inverseBlockConstraints.u2|inverseBlockConstraints.y1|inverseBlockConstraints.y2|loopBreaker.L|loopBreaker.T_out|loopBreaker.T_out_fixed|loopBreaker.XiSpec|loopBreaker.assertionLevel|loopBreaker.dh|loopBreaker.dm_flow|loopBreaker.dp|loopBreaker.h_out|loopBreaker.h_out_fixed|loopBreaker.inlet.m_flow|loopBreaker.inlet.r|loopBreaker.inlet.state.T|loopBreaker.inlet.state.d|loopBreaker.inlet.state.h|loopBreaker.inlet.state.p|loopBreaker.inlet.state.phase|loopBreaker.m_flowSpec|loopBreaker.m_flow_in|loopBreaker.m_flow_in_par|loopBreaker.m_flow_in_prescribed|der.loopBreaker.outlet.m_flow.|loopBreaker.outlet.m_flow|loopBreaker.outlet.r|loopBreaker.outlet.state.T|loopBreaker.outlet.state.d|loopBreaker.outlet.state.h|loopBreaker.outlet.state.p|loopBreaker.outlet.state.phase|loopBreaker.pSpec|loopBreaker.p_out|loopBreaker.p_out_fixed|loopBreaker.thermalSpec|loopBreaker.thermalValueSpec|loopBreaker.tol_Xi|loopBreaker.tol_h|loopBreaker.tol_m_flow|loopBreaker.tol_p|massFlowRate.height|massFlowRate.offset|massFlowRate.startTime|massFlowRate.y|outletPressure.duration|outletPressure.height|outletPressure.offset|outletPressure.startTime|outletPressure.y|preheater.L|preheater.P|preheater.Q_flow|preheater.T_out_fixed|preheater.assertionLevel|preheater.clip_p_out|preheater.dT|preheater.dT_fixed|preheater.dh|preheater.dh_fixed|preheater.dp|preheater.dr_corr|preheater.du|preheater.h_in|preheater.h_out|preheater.h_out_fixed|preheater.initM_flow|der.preheater.inlet.m_flow.|preheater.inlet.m_flow|preheater.inlet.r|preheater.inlet.state.T|preheater.inlet.state.d|preheater.inlet.state.h|preheater.inlet.state.p|preheater.inlet.state.phase|preheater.m_acceleration_0|preheater.m_flow|preheater.m_flowStateSelect|preheater.m_flow_0|preheater.outlet.m_flow|preheater.outlet.r|preheater.outlet.state.T|preheater.outlet.state.d|preheater.outlet.state.h|preheater.outlet.state.p|preheater.outlet.state.phase|preheater.outletSpec|preheater.outletSpec_actual|preheater.outletSpec_prescribed|preheater.outletValueSpec|preheater.p|preheater.p_in|preheater.p_inf|preheater.p_min|preheater.p_out|preheater.q|preheater.rho_in|preheater.rho_out|preheater.singularityRegime|preheater.systemSpec|preheater.u_in|preheater.u_out|preheater.v_in|preheater.v_out|preheater.w_amb|preheater.w_exp|preheater.w_exp_net|pump.L|pump.P|pump.P_nom|pump.TC|pump.adiabaticModel.eta_is|pump.adiabaticModel.h_in|pump.adiabaticModel.h_out|pump.adiabaticModel.h_out_is|pump.adiabaticModel.p_out|pump.adiabaticModel.s_in|pump.adiabaticModel.state_in.T|pump.adiabaticModel.state_in.d|pump.adiabaticModel.state_in.h|pump.adiabaticModel.state_in.p|pump.adiabaticModel.state_in.phase|pump.adiabaticModel.w_t|pump.adiabaticModel.w_t_is|pump.assertionLevel|pump.clip_p_out|pump.dh|pump.dp|pump.dp_fixed|pump.dp_nom|pump.dp_start|pump.dr_corr|pump.etaSpec|pump.eta_actual|pump.eta_fixed|pump.eta_is|pump.h_in|pump.h_out|pump.initM_flow|der.pump.inlet.m_flow.|pump.inlet.m_flow|pump.inlet.r|pump.inlet.state.T|pump.inlet.state.d|pump.inlet.state.h|pump.inlet.state.p|pump.inlet.state.phase|pump.m_acceleration_0|pump.m_flow|pump.m_flowStateSelect|pump.m_flow_0|pump.outlet.m_flow|pump.outlet.r|pump.outlet.state.T|pump.outlet.state.d|pump.outlet.state.h|pump.outlet.state.p|pump.outlet.state.phase|pump.outletSpec|pump.outletSpec_actual|pump.outletSpec_prescribed|pump.outletValueSpec|pump.pRatio|pump.pRatio_fixed|pump.p_in|pump.p_min|pump.p_out|pump.p_out_fixed|pump.singularityRegime|superheater.L|superheater.P|superheater.Q_flow|superheater.T_out_fixed|superheater.assertionLevel|superheater.clip_p_out|superheater.dT|superheater.dT_fixed|superheater.dh|superheater.dh_fixed|superheater.dp|superheater.dr_corr|superheater.du|superheater.h_in|superheater.h_out|superheater.h_out_fixed|superheater.initM_flow|der.superheater.inlet.m_flow.|superheater.inlet.m_flow|superheater.inlet.r|superheater.inlet.state.T|superheater.inlet.state.d|superheater.inlet.state.h|superheater.inlet.state.p|superheater.inlet.state.phase|superheater.m_acceleration_0|superheater.m_flow|superheater.m_flowStateSelect|superheater.m_flow_0|superheater.outlet.m_flow|superheater.outlet.r|superheater.outlet.state.T|superheater.outlet.state.d|superheater.outlet.state.h|superheater.outlet.state.p|superheater.outlet.state.phase|superheater.outletSpec|superheater.outletSpec_actual|superheater.outletSpec_prescribed|superheater.outletValueSpec|superheater.p|superheater.p_in|superheater.p_inf|superheater.p_min|superheater.p_out|superheater.q|superheater.rho_in|superheater.rho_out|superheater.singularityRegime|superheater.systemSpec|superheater.u_in|superheater.u_out|superheater.v_in|superheater.v_out|superheater.w_amb|superheater.w_exp|superheater.w_exp_net|turbine.L|turbine.P|turbine.P_nom|turbine.TC|turbine.adiabaticModel.eta_is|turbine.adiabaticModel.h_in|turbine.adiabaticModel.h_out|turbine.adiabaticModel.h_out_is|turbine.adiabaticModel.p_out|turbine.adiabaticModel.s_in|turbine.adiabaticModel.state_in.T|turbine.adiabaticModel.state_in.d|turbine.adiabaticModel.state_in.h|turbine.adiabaticModel.state_in.p|turbine.adiabaticModel.state_in.phase|turbine.adiabaticModel.w_t|turbine.adiabaticModel.w_t_is|turbine.assertionLevel|turbine.clip_p_out|turbine.dh|turbine.dp|turbine.dp_fixed|turbine.dp_nom|turbine.dp_start|turbine.dr_corr|turbine.etaSpec|turbine.eta_actual|turbine.eta_fixed|turbine.eta_is|turbine.h_in|turbine.h_out|turbine.initM_flow|der.turbine.inlet.m_flow.|turbine.inlet.m_flow|turbine.inlet.r|turbine.inlet.state.T|turbine.inlet.state.d|turbine.inlet.state.h|turbine.inlet.state.p|turbine.inlet.state.phase|turbine.m_acceleration_0|turbine.m_flow|turbine.m_flowStateSelect|turbine.m_flow_0|turbine.outlet.m_flow|turbine.outlet.r|turbine.outlet.state.T|turbine.outlet.state.d|turbine.outlet.state.h|turbine.outlet.state.p|turbine.outlet.state.phase|turbine.outletSpec|turbine.outletSpec_actual|turbine.outletValueSpec|turbine.pRatio|turbine.pRatio_fixed|turbine.p_in|turbine.p_min|turbine.p_out|turbine.p_out_fixed|turbine.singularityRegime|vaporQualitySensor.TC|vaporQualitySensor.digits|vaporQualitySensor.direct_value|vaporQualitySensor.init|vaporQualitySensor.inlet.m_flow|vaporQualitySensor.inlet.r|vaporQualitySensor.inlet.state.T|vaporQualitySensor.inlet.state.d|vaporQualitySensor.inlet.state.h|vaporQualitySensor.inlet.state.p|vaporQualitySensor.inlet.state.phase|vaporQualitySensor.quantity|vaporQualitySensor.value|vaporQualitySensor.value_0|vaporQualitySensor.value_out|vaporQualitySetpoint.y",fileNamePrefix="ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion") [Timeout 660] "Notification: Performance of FrontEnd - loaded program: time 1.463e-06/1.463e-06, allocations: 0 / 0.5545 GB, free: 12.78 MB / 490.7 MB Notification: Performance of FrontEnd - Absyn->SCode: time 2.226e-05/2.373e-05, allocations: 2.281 kB / 0.5545 GB, free: 12.78 MB / 490.7 MB Notification: Performance of NFInst.instantiate(ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion): time 0.0412/0.04122, allocations: 65.7 MB / 0.6187 GB, free: 10.85 MB / 0.5417 GB Notification: Performance of NFInst.instExpressions: time 0.297/0.3382, allocations: 27.42 MB / 0.6455 GB, free: 11.27 MB / 0.5573 GB Notification: Performance of NFInst.updateImplicitVariability: time 0.001644/0.3398, allocations: 55.22 kB / 0.6455 GB, free: 11.27 MB / 0.5573 GB Notification: Performance of NFTyping.typeComponents: time 0.001638/0.3415, allocations: 0.7003 MB / 0.6462 GB, free: 11.27 MB / 0.5573 GB Notification: Performance of NFTyping.typeBindings: time 0.01767/0.3591, allocations: 7.799 MB / 0.6538 GB, free: 10.74 MB / 0.5573 GB Notification: Performance of NFTyping.typeClassSections: time 0.004413/0.3636, allocations: 2.094 MB / 0.6559 GB, free: 10.47 MB / 0.5573 GB Notification: Performance of NFFlatten.flatten: time 0.002068/0.3656, allocations: 2.195 MB / 0.658 GB, free: 9.758 MB / 0.5573 GB Notification: Performance of NFFlatten.resolveConnections: time 0.0003731/0.366, allocations: 239 kB / 0.6582 GB, free: 9.684 MB / 0.5573 GB Notification: Performance of NFEvalConstants.evaluate: time 0.0106/0.3766, allocations: 9.175 MB / 0.6672 GB, free: 7.164 MB / 0.5573 GB Notification: Performance of NFSimplifyModel.simplify: time 0.0008925/0.3775, allocations: 0.5755 MB / 0.6678 GB, free: 7.078 MB / 0.5573 GB Notification: Performance of NFPackage.collectConstants: time 0.0001256/0.3776, allocations: 92.84 kB / 0.6679 GB, free: 7.078 MB / 0.5573 GB Notification: Performance of NFFlatten.collectFunctions: time 0.02014/0.3978, allocations: 10.78 MB / 0.6784 GB, free: 6.898 MB / 0.5573 GB Notification: Performance of NFScalarize.scalarize: time 0.0002397/0.398, allocations: 262 kB / 0.6786 GB, free: 6.828 MB / 0.5573 GB Notification: Performance of NFVerifyModel.verify: time 0.0006622/0.3987, allocations: 498.3 kB / 0.6791 GB, free: 6.758 MB / 0.5573 GB Notification: Performance of NFConvertDAE.convert: time 0.01549/0.4141, allocations: 9.871 MB / 0.6887 GB, free: 3.668 MB / 0.5573 GB Notification: Performance of FrontEnd - DAE generated: time 5.63e-06/0.4141, allocations: 7.25 kB / 0.6888 GB, free: 3.664 MB / 0.5573 GB Notification: Performance of FrontEnd: time 1.704e-06/0.4141, allocations: 0 / 0.6888 GB, free: 3.664 MB / 0.5573 GB Notification: Performance of Transformations before backend: time 1.312e-05/0.4142, allocations: 0 / 0.6888 GB, free: 3.664 MB / 0.5573 GB Notification: Model statistics after passing the front-end and creating the data structures used by the back-end: * Number of equations: 304 * Number of variables: 304 Notification: Performance of Generate backend data structure: time 0.003526/0.4177, allocations: 2.731 MB / 0.6914 GB, free: 2.062 MB / 0.5573 GB Notification: Performance of prepare preOptimizeDAE: time 3.835e-05/0.4177, allocations: 7.781 kB / 0.6914 GB, free: 2.062 MB / 0.5573 GB Notification: Performance of preOpt normalInlineFunction (simulation): time 0.0008916/0.4186, allocations: 375 kB / 0.6918 GB, free: 1.914 MB / 0.5573 GB Notification: Performance of preOpt evaluateParameters (simulation): time 0.0008916/0.4195, allocations: 0.7929 MB / 0.6926 GB, free: 1.492 MB / 0.5573 GB Notification: Performance of preOpt simplifyIfEquations (simulation): time 0.0001259/0.4196, allocations: 205.3 kB / 0.6928 GB, free: 1.355 MB / 0.5573 GB Notification: Performance of preOpt expandDerOperator (simulation): time 9.493e-05/0.4197, allocations: 122.9 kB / 0.6929 GB, free: 1.352 MB / 0.5573 GB Notification: Performance of preOpt clockPartitioning (simulation): time 0.001407/0.4211, allocations: 1.487 MB / 0.6943 GB, free: 0.6758 MB / 0.5573 GB Notification: Performance of preOpt findStateOrder (simulation): time 1.884e-05/0.4212, allocations: 0 / 0.6943 GB, free: 0.6758 MB / 0.5573 GB Notification: Performance of preOpt replaceEdgeChange (simulation): time 5.991e-05/0.4212, allocations: 51.09 kB / 0.6944 GB, free: 0.6758 MB / 0.5573 GB Notification: Performance of preOpt inlineArrayEqn (simulation): time 1.605e-05/0.4212, allocations: 35.94 kB / 0.6944 GB, free: 0.6719 MB / 0.5573 GB Notification: Performance of preOpt removeEqualRHS (simulation): time 0.001247/0.4225, allocations: 1.02 MB / 0.6954 GB, free: 0.4922 MB / 0.5573 GB Warning: The model contains alias variables with redundant start and/or conflicting nominal values. It is recommended to resolve the conflicts, because otherwise the system could be hard to solve. To print the conflicting alias sets and the chosen candidates please use -d=aliasConflicts. Notification: Performance of preOpt removeSimpleEquations (simulation): time 0.003766/0.4262, allocations: 4.803 MB / 0.7001 GB, free: 13.18 MB / 0.573 GB Notification: Performance of preOpt comSubExp (simulation): time 0.001216/0.4275, allocations: 0.8316 MB / 0.7009 GB, free: 12.74 MB / 0.573 GB Notification: Performance of preOpt resolveLoops (simulation): time 0.0004122/0.4279, allocations: 369.4 kB / 0.7013 GB, free: 12.57 MB / 0.573 GB Notification: Performance of preOpt evalFunc (simulation): time 0.05945/0.4873, allocations: 36.47 MB / 0.7369 GB, free: 14.19 MB / 0.6042 GB Notification: Performance of preOpt encapsulateWhenConditions (simulation): time 4.762e-05/0.4874, allocations: 46.64 kB / 0.7369 GB, free: 14.14 MB / 0.6042 GB Notification: Performance of pre-optimization done (n=85): time 2.776e-06/0.4874, allocations: 0 / 0.7369 GB, free: 14.14 MB / 0.6042 GB Notification: Performance of matching and sorting (n=85): time 0.002775/0.4901, allocations: 1.384 MB / 0.7383 GB, free: 12.77 MB / 0.6042 GB Notification: Performance of inlineWhenForInitialization (initialization): time 5.393e-05/0.4902, allocations: 86.11 kB / 0.7384 GB, free: 12.66 MB / 0.6042 GB Notification: Performance of selectInitializationVariablesDAE (initialization): time 0.001075/0.4913, allocations: 0.7952 MB / 0.7391 GB, free: 11.85 MB / 0.6042 GB Notification: Performance of collectPreVariables (initialization): time 3.774e-05/0.4913, allocations: 41.7 kB / 0.7392 GB, free: 11.8 MB / 0.6042 GB Notification: Performance of collectInitialEqns (initialization): time 0.0003371/0.4916, allocations: 0.6383 MB / 0.7398 GB, free: 11.16 MB / 0.6042 GB Notification: Performance of collectInitialBindings (initialization): time 0.0001588/0.4918, allocations: 303.9 kB / 0.7401 GB, free: 10.86 MB / 0.6042 GB Notification: Performance of simplifyInitialFunctions (initialization): time 0.0001631/0.492, allocations: 186.5 kB / 0.7403 GB, free: 10.68 MB / 0.6042 GB Notification: Performance of setup shared object (initialization): time 9.97e-05/0.4921, allocations: 349.9 kB / 0.7406 GB, free: 10.33 MB / 0.6042 GB Notification: Performance of preBalanceInitialSystem (initialization): time 0.0003126/0.4924, allocations: 249.8 kB / 0.7408 GB, free: 10.08 MB / 0.6042 GB Notification: Performance of partitionIndependentBlocks (initialization): time 0.0004648/0.4928, allocations: 0.5778 MB / 0.7414 GB, free: 9.371 MB / 0.6042 GB Notification: Performance of analyzeInitialSystem (initialization): time 0.0008087/0.4937, allocations: 0.8666 MB / 0.7422 GB, free: 8.414 MB / 0.6042 GB Notification: Performance of solveInitialSystemEqSystem (initialization): time 5.56e-06/0.4937, allocations: 4 kB / 0.7422 GB, free: 8.41 MB / 0.6042 GB Notification: Performance of matching and sorting (n=126) (initialization): time 0.001042/0.4947, allocations: 0.9947 MB / 0.7432 GB, free: 7.461 MB / 0.6042 GB Notification: Performance of prepare postOptimizeDAE: time 2.263e-05/0.4947, allocations: 12.88 kB / 0.7432 GB, free: 7.449 MB / 0.6042 GB Notification: Performance of postOpt simplifyComplexFunction (initialization): time 1.238e-05/0.4947, allocations: 12 kB / 0.7432 GB, free: 7.438 MB / 0.6042 GB Notification: Performance of postOpt tearingSystem (initialization): time 0.0005416/0.4953, allocations: 137.6 kB / 0.7434 GB, free: 7.297 MB / 0.6042 GB Notification: Performance of postOpt solveSimpleEquations (initialization): time 0.0004428/0.4957, allocations: 227.1 kB / 0.7436 GB, free: 7.09 MB / 0.6042 GB Notification: Performance of postOpt calculateStrongComponentJacobians (initialization): time 0.0007603/0.4965, allocations: 1.72 MB / 0.7453 GB, free: 5.305 MB / 0.6042 GB Notification: Performance of postOpt simplifyAllExpressions (initialization): time 0.0004093/0.4969, allocations: 99.34 kB / 0.7454 GB, free: 5.207 MB / 0.6042 GB Notification: Performance of postOpt collapseArrayExpressions (initialization): time 4.831e-05/0.4969, allocations: 49.08 kB / 0.7454 GB, free: 5.16 MB / 0.6042 GB Notification: Model statistics after passing the back-end for initialization: * Number of independent subsystems: 42 * Number of states: 0 () * Number of discrete variables: 7 (superheater.outlet.state.phase,loopBreaker.outlet.state.phase,turbine.outlet.state.phase,condenser.outlet.state.phase,preheater.outlet.state.phase,boiler.outlet.state.phase,pump.outlet.state.phase) * Number of discrete states: 0 () * Number of clocked states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for initialization (120): * Single equations (assignments): 117 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 0 * When equations: 0 * If-equations: 0 * Equation systems (not torn): 1 * Torn equation systems: 2 * Mixed (continuous/discrete) equation systems: 0 Notification: Equation system details (not torn): * Constant Jacobian (size): 0 systems * Linear Jacobian (size,density): 0 systems * Non-linear Jacobian (size): 1 system {1} * Without analytic Jacobian (size): 0 systems Notification: Torn system details for strict tearing set: * Linear torn systems (#iteration vars, #inner vars, density): 0 systems * Non-linear torn systems (#iteration vars, #inner vars): 2 systems {(1,4), (1,2)} Notification: Performance of prepare postOptimizeDAE: time 0.0003702/0.4973, allocations: 273.7 kB / 0.7457 GB, free: 4.898 MB / 0.6042 GB Notification: Performance of postOpt lateInlineFunction (simulation): time 0.0004128/0.4977, allocations: 119.2 kB / 0.7458 GB, free: 4.781 MB / 0.6042 GB Notification: Performance of postOpt wrapFunctionCalls (simulation): time 0.002336/0.5001, allocations: 3.076 MB / 0.7488 GB, free: 1.723 MB / 0.6042 GB Notification: Performance of postOpt inlineArrayEqn (simulation): time 3.219e-05/0.5001, allocations: 47.88 kB / 0.7488 GB, free: 1.676 MB / 0.6042 GB Notification: Performance of postOpt constantLinearSystem (simulation): time 9.999e-06/0.5001, allocations: 0 / 0.7488 GB, free: 1.676 MB / 0.6042 GB Notification: Performance of postOpt simplifysemiLinear (simulation): time 8.005e-06/0.5001, allocations: 3.984 kB / 0.7488 GB, free: 1.672 MB / 0.6042 GB Notification: Performance of postOpt removeSimpleEquations (simulation): time 0.00387/0.504, allocations: 4.197 MB / 0.7529 GB, free: 13.5 MB / 0.6198 GB Notification: Performance of postOpt simplifyComplexFunction (simulation): time 7.394e-06/0.504, allocations: 11.86 kB / 0.7529 GB, free: 13.48 MB / 0.6198 GB Notification: Performance of postOpt solveSimpleEquations (simulation): time 0.0002715/0.5043, allocations: 127.8 kB / 0.7531 GB, free: 13.37 MB / 0.6198 GB Notification: Performance of postOpt tearingSystem (simulation): time 0.0006562/0.5049, allocations: 0.6341 MB / 0.7537 GB, free: 12.73 MB / 0.6198 GB Notification: Performance of postOpt inputDerivativesUsed (simulation): time 3.137e-05/0.5049, allocations: 23.94 kB / 0.7537 GB, free: 12.71 MB / 0.6198 GB Notification: Performance of postOpt calculateStrongComponentJacobians (simulation): time 0.001049/0.506, allocations: 2.315 MB / 0.756 GB, free: 10.32 MB / 0.6198 GB Notification: Performance of postOpt calculateStateSetsJacobians (simulation): time 2.094e-06/0.506, allocations: 0 / 0.756 GB, free: 10.32 MB / 0.6198 GB Notification: Performance of postOpt symbolicJacobian (simulation): time 0.00234/0.5083, allocations: 2.992 MB / 0.7589 GB, free: 7.348 MB / 0.6198 GB Notification: Performance of postOpt removeConstants (simulation): time 0.0002739/0.5086, allocations: 230.3 kB / 0.7591 GB, free: 7.121 MB / 0.6198 GB Notification: Performance of postOpt simplifyTimeIndepFuncCalls (simulation): time 7.684e-05/0.5087, allocations: 31.84 kB / 0.7591 GB, free: 7.09 MB / 0.6198 GB Notification: Performance of postOpt simplifyAllExpressions (simulation): time 0.0002083/0.5089, allocations: 31.97 kB / 0.7592 GB, free: 7.059 MB / 0.6198 GB Notification: Performance of postOpt findZeroCrossings (simulation): time 8.916e-05/0.509, allocations: 64.94 kB / 0.7592 GB, free: 6.996 MB / 0.6198 GB Notification: Performance of postOpt collapseArrayExpressions (simulation): time 2.84e-05/0.509, allocations: 28 kB / 0.7593 GB, free: 6.969 MB / 0.6198 GB Notification: Performance of sorting global known variables: time 0.000515/0.5095, allocations: 0.606 MB / 0.7599 GB, free: 6.355 MB / 0.6198 GB Notification: Performance of sort global known variables: time 7e-08/0.5095, allocations: 0 / 0.7599 GB, free: 6.355 MB / 0.6198 GB Notification: Performance of remove unused functions: time 0.004768/0.5143, allocations: 1.859 MB / 0.7617 GB, free: 4.492 MB / 0.6198 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 0.004454/0.5188, allocations: 2.277 MB / 0.7639 GB, free: 2.395 MB / 0.6198 GB Notification: Performance of simCode: created initialization part: time 0.0012/0.52, allocations: 1.001 MB / 0.7649 GB, free: 1.426 MB / 0.6198 GB Notification: Performance of simCode: created event and clocks part: time 3.497e-06/0.52, allocations: 4.438 kB / 0.7649 GB, free: 1.422 MB / 0.6198 GB Notification: Performance of simCode: created simulation system equations: time 0.0005417/0.5205, allocations: 0.6246 MB / 0.7655 GB, free: 0.8164 MB / 0.6198 GB Notification: Performance of simCode: created of all other equations (e.g. parameter, nominal, assert, etc): time 0.001311/0.5218, allocations: 0.5614 MB / 0.766 GB, free: 304 kB / 0.6198 GB [/var/lib/jenkins/ws/OpenModelicaLibraryTestingWork/OpenModelica/OMCompiler/Compiler/SimCode/SimCodeUtil.mo:10414:11-10414:222: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 0.00328/0.5251, allocations: 3.009 MB / 0.769 GB, free: 13.26 MB / 0.6355 GB Notification: Performance of simCode: some other stuff during SimCode phase: time 0.0004287/0.5255, allocations: 0.7262 MB / 0.7697 GB, free: 12.49 MB / 0.6355 GB Notification: Performance of simCode: all other stuff during SimCode phase: time 0.0001482/0.5257, allocations: 92.48 kB / 0.7698 GB, free: 12.4 MB / 0.6355 GB Notification: Performance of SimCode: time 9.22e-07/0.5257, allocations: 0 / 0.7698 GB, free: 12.4 MB / 0.6355 GB Notification: Performance of Templates: time 0.0661/0.5918, allocations: 66.8 MB / 0.835 GB, free: 9.715 MB / 0.698 GB " [Timeout remaining time 659] make -j1 -f ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion.makefile [Timeout 660] (rm -f ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion.pipe ; mkfifo ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion.pipe ; head -c 1048576 < ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion.pipe >> ../files/ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion.sim & ./ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion -abortSlowSimulation -alarm=1200 -emit_protected -lv LOG_STATS > ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion.pipe 2>&1) [Timeout 1200] diffSimulationResults("ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat","/mnt/ReferenceFiles/ThermofluidStream-main-regression/ReferenceData/ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_ref.mat","/var/lib/jenkins/ws/OpenModelicaLibraryTestingWork/OpenModelicaLibraryTesting/files/ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion.diff",relTol=0.003,relTolDiffMinMax=0.003,rangeDelta=0.001) [Timeout 660] "Error: Could not read variable CPUtime in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable CPUtime from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable EventCounter in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable EventCounter from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable NonlinearSystems.initialization[1].Calls in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable NonlinearSystems.initialization[1].Calls from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable NonlinearSystems.initialization[1].Iterations in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable NonlinearSystems.initialization[1].Iterations from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable NonlinearSystems.initialization[1].Jacobians in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable NonlinearSystems.initialization[1].Jacobians from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable NonlinearSystems.initialization[1].Residues in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable NonlinearSystems.initialization[1].Residues from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable NonlinearSystems.simulation[1].Calls in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable NonlinearSystems.simulation[1].Calls from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable NonlinearSystems.simulation[1].Iterations in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable NonlinearSystems.simulation[1].Iterations from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable NonlinearSystems.simulation[1].Jacobians in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable NonlinearSystems.simulation[1].Jacobians from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable NonlinearSystems.simulation[1].Residues in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable NonlinearSystems.simulation[1].Residues from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable NonlinearSystems.simulation[2].Calls in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable NonlinearSystems.simulation[2].Calls from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable NonlinearSystems.simulation[2].Iterations in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable NonlinearSystems.simulation[2].Iterations from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable NonlinearSystems.simulation[2].Jacobians in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable NonlinearSystems.simulation[2].Jacobians from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable NonlinearSystems.simulation[2].Residues in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable NonlinearSystems.simulation[2].Residues from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable boiler.P in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable boiler.P from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable boiler.T_out_fixed in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable boiler.T_out_fixed from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable boiler.assertionLevel in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable boiler.assertionLevel from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable boiler.dT_fixed in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable boiler.dT_fixed from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable boiler.dh_fixed in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable boiler.dh_fixed from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable boiler.du in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable boiler.du from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable boiler.h_out_fixed in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable boiler.h_out_fixed from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable boiler.p_inf in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable boiler.p_inf from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable boiler.u_in in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable boiler.u_in from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable boiler.u_out in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable boiler.u_out from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable boiler.v_in in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable boiler.v_in from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable boiler.v_out in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable boiler.v_out from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable boiler.w_amb in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable boiler.w_amb from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable boiler.w_exp in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable boiler.w_exp from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable boiler.w_exp_net in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable boiler.w_exp_net from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable condenser.P in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable condenser.P from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable condenser.assertionLevel in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable condenser.assertionLevel from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable condenser.dT_fixed in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable condenser.dT_fixed from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable condenser.dh_fixed in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable condenser.dh_fixed from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable condenser.du in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable condenser.du from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable condenser.h_out_fixed in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable condenser.h_out_fixed from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable condenser.p_inf in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable condenser.p_inf from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable condenser.u_in in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable condenser.u_in from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable condenser.u_out in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable condenser.u_out from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable condenser.v_in in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable condenser.v_in from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable condenser.v_out in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable condenser.v_out from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable condenser.w_amb in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable condenser.w_amb from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable condenser.w_exp in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable condenser.w_exp from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable condenser.w_exp_net in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable condenser.w_exp_net from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable dropOfCommons.instanceNameColor[1] in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable dropOfCommons.instanceNameColor[1] from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable dropOfCommons.instanceNameColor[2] in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable dropOfCommons.instanceNameColor[2] from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable dropOfCommons.instanceNameColor[3] in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable dropOfCommons.instanceNameColor[3] from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable loopBreaker.h_out_fixed in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable loopBreaker.h_out_fixed from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable loopBreaker.m_flow_in_par in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable loopBreaker.m_flow_in_par from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable preheater.P in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable preheater.P from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable preheater.T_out_fixed in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable preheater.T_out_fixed from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable preheater.assertionLevel in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable preheater.assertionLevel from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable preheater.dT_fixed in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable preheater.dT_fixed from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable preheater.dh_fixed in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable preheater.dh_fixed from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable preheater.du in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable preheater.du from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable preheater.h_out_fixed in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable preheater.h_out_fixed from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable preheater.p_inf in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable preheater.p_inf from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable preheater.rho_out in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable preheater.rho_out from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable preheater.u_in in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable preheater.u_in from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable preheater.u_out in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable preheater.u_out from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable preheater.v_in in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable preheater.v_in from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable preheater.v_out in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable preheater.v_out from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable preheater.w_amb in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable preheater.w_amb from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable preheater.w_exp in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable preheater.w_exp from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable preheater.w_exp_net in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable preheater.w_exp_net from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable pump.P_nom in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable pump.P_nom from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable pump.TC in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable pump.TC from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable pump.assertionLevel in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable pump.assertionLevel from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable pump.dp_fixed in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable pump.dp_fixed from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable pump.dp_nom in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable pump.dp_nom from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable pump.dp_start in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable pump.dp_start from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable pump.pRatio_fixed in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable pump.pRatio_fixed from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable pump.p_out_fixed in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable pump.p_out_fixed from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable superheater.P in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable superheater.P from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable superheater.T_out_fixed in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable superheater.T_out_fixed from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable superheater.assertionLevel in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable superheater.assertionLevel from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable superheater.dT_fixed in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable superheater.dT_fixed from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable superheater.dh_fixed in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable superheater.dh_fixed from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable superheater.du in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable superheater.du from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable superheater.h_out_fixed in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable superheater.h_out_fixed from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable superheater.p_inf in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable superheater.p_inf from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable superheater.rho_in in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable superheater.rho_in from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable superheater.u_in in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable superheater.u_in from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable superheater.u_out in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable superheater.u_out from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable superheater.v_in in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable superheater.v_in from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable superheater.v_out in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable superheater.v_out from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable superheater.w_amb in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable superheater.w_amb from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable superheater.w_exp in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable superheater.w_exp from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable superheater.w_exp_net in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable superheater.w_exp_net from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable turbine.P_nom in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable turbine.P_nom from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable turbine.TC in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable turbine.TC from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable turbine.assertionLevel in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable turbine.assertionLevel from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable turbine.dp_fixed in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable turbine.dp_fixed from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable turbine.dp_nom in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable turbine.dp_nom from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable turbine.dp_start in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable turbine.dp_start from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable turbine.inlet.der(m_flow) in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable turbine.inlet.der(m_flow) from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! Error: Could not read variable turbine.pRatio_fixed in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat. Warning: Get data of variable turbine.pRatio_fixed from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step9VaporQualityInversion_res.mat failed! " [Timeout remaining time 660] "" Variables in the reference:CPUtime,EventCounter,NonlinearSystems.initialization[1].Calls,NonlinearSystems.initialization[1].Iterations,NonlinearSystems.initialization[1].Jacobians,NonlinearSystems.initialization[1].Residues,NonlinearSystems.simulation[1].Calls,NonlinearSystems.simulation[1].Iterations,NonlinearSystems.simulation[1].Jacobians,NonlinearSystems.simulation[1].Residues,NonlinearSystems.simulation[2].Calls,NonlinearSystems.simulation[2].Iterations,NonlinearSystems.simulation[2].Jacobians,NonlinearSystems.simulation[2].Residues,Time,boiler.L,boiler.P,boiler.Q_flow,boiler.T_out_fixed,boiler.assertionLevel,boiler.clip_p_out,boiler.dT,boiler.dT_fixed,boiler.dh,boiler.dh_fixed,boiler.dp,boiler.dr_corr,boiler.du,boiler.h_in,boiler.h_out,boiler.h_out_fixed,boiler.initM_flow,der(boiler.inlet.m_flow),boiler.inlet.m_flow,boiler.inlet.r,boiler.inlet.state.T,boiler.inlet.state.d,boiler.inlet.state.h,boiler.inlet.state.p,boiler.inlet.state.phase,boiler.m_acceleration_0,boiler.m_flow,boiler.m_flowStateSelect,boiler.m_flow_0,boiler.outlet.m_flow,boiler.outlet.r,boiler.outlet.state.T,boiler.outlet.state.d,boiler.outlet.state.h,boiler.outlet.state.p,boiler.outlet.state.phase,boiler.outletSpec,boiler.outletSpec_actual,boiler.outletSpec_prescribed,boiler.outletValueSpec,boiler.p,boiler.p_in,boiler.p_inf,boiler.p_min,boiler.p_out,boiler.q,boiler.rho_in,boiler.rho_out,boiler.singularityRegime,boiler.systemSpec,boiler.u_in,boiler.u_out,boiler.v_in,boiler.v_out,boiler.w_amb,boiler.w_exp,boiler.w_exp_net,condenser.L,condenser.P,condenser.Q_flow,condenser.T_out_fixed,condenser.assertionLevel,condenser.clip_p_out,condenser.dT,condenser.dT_fixed,condenser.dh,condenser.dh_fixed,condenser.dp,condenser.dr_corr,condenser.du,condenser.h_in,condenser.h_out,condenser.h_out_fixed,condenser.initM_flow,der(condenser.inlet.m_flow),condenser.inlet.m_flow,condenser.inlet.r,condenser.inlet.state.T,condenser.inlet.state.d,condenser.inlet.state.h,condenser.inlet.state.p,condenser.inlet.state.phase,condenser.m_acceleration_0,condenser.m_flow,condenser.m_flowStateSelect,condenser.m_flow_0,condenser.outlet.m_flow,condenser.outlet.r,condenser.outlet.state.T,condenser.outlet.state.d,condenser.outlet.state.h,condenser.outlet.state.p,condenser.outlet.state.phase,condenser.outletSpec,condenser.outletSpec_actual,condenser.outletValueSpec,condenser.p,condenser.p_in,condenser.p_inf,condenser.p_min,condenser.p_out,condenser.q,condenser.rho_in,condenser.rho_out,condenser.singularityRegime,condenser.systemSpec,condenser.u_in,condenser.u_out,condenser.v_in,condenser.v_out,condenser.w_amb,condenser.w_exp,condenser.w_exp_net,dropOfCommons.L,dropOfCommons.assertionLevel,dropOfCommons.g,dropOfCommons.instanceNameColor[1],dropOfCommons.instanceNameColor[2],dropOfCommons.instanceNameColor[3],dropOfCommons.k_volume_damping,dropOfCommons.m_flow_reg,dropOfCommons.omega_reg,dropOfCommons.p_min,dropOfCommons.rho_min,efficiencyExtensive.displayVariablefinal,efficiencyExtensive.showNumber,efficiencyExtensive.significantDigits,efficiencySpecific.displayVariablefinal,efficiencySpecific.showNumber,efficiencySpecific.significantDigits,firstOrder.T,der(firstOrder.y),firstOrder.initType,firstOrder.k,firstOrder.u,firstOrder.y,firstOrder.y_start,h_bubble.y,h_dew.y,inverseBlockConstraints.u1,inverseBlockConstraints.u2,inverseBlockConstraints.y1,inverseBlockConstraints.y2,loopBreaker.L,loopBreaker.T_out,loopBreaker.T_out_fixed,loopBreaker.XiSpec,loopBreaker.assertionLevel,loopBreaker.dh,loopBreaker.dm_flow,loopBreaker.dp,loopBreaker.h_out,loopBreaker.h_out_fixed,loopBreaker.inlet.m_flow,loopBreaker.inlet.r,loopBreaker.inlet.state.T,loopBreaker.inlet.state.d,loopBreaker.inlet.state.h,loopBreaker.inlet.state.p,loopBreaker.inlet.state.phase,loopBreaker.m_flowSpec,loopBreaker.m_flow_in,loopBreaker.m_flow_in_par,loopBreaker.m_flow_in_prescribed,der(loopBreaker.outlet.m_flow),loopBreaker.outlet.m_flow,loopBreaker.outlet.r,loopBreaker.outlet.state.T,loopBreaker.outlet.state.d,loopBreaker.outlet.state.h,loopBreaker.outlet.state.p,loopBreaker.outlet.state.phase,loopBreaker.pSpec,loopBreaker.p_out,loopBreaker.p_out_fixed,loopBreaker.thermalSpec,loopBreaker.thermalValueSpec,loopBreaker.tol_Xi,loopBreaker.tol_h,loopBreaker.tol_m_flow,loopBreaker.tol_p,massFlowRate.height,massFlowRate.offset,massFlowRate.startTime,massFlowRate.y,outletPressure.duration,outletPressure.height,outletPressure.offset,outletPressure.startTime,outletPressure.y,preheater.L,preheater.P,preheater.Q_flow,preheater.T_out_fixed,preheater.assertionLevel,preheater.clip_p_out,preheater.dT,preheater.dT_fixed,preheater.dh,preheater.dh_fixed,preheater.dp,preheater.dr_corr,preheater.du,preheater.h_in,preheater.h_out,preheater.h_out_fixed,preheater.initM_flow,der(preheater.inlet.m_flow),preheater.inlet.m_flow,preheater.inlet.r,preheater.inlet.state.T,preheater.inlet.state.d,preheater.inlet.state.h,preheater.inlet.state.p,preheater.inlet.state.phase,preheater.m_acceleration_0,preheater.m_flow,preheater.m_flowStateSelect,preheater.m_flow_0,preheater.outlet.m_flow,preheater.outlet.r,preheater.outlet.state.T,preheater.outlet.state.d,preheater.outlet.state.h,preheater.outlet.state.p,preheater.outlet.state.phase,preheater.outletSpec,preheater.outletSpec_actual,preheater.outletSpec_prescribed,preheater.outletValueSpec,preheater.p,preheater.p_in,preheater.p_inf,preheater.p_min,preheater.p_out,preheater.q,preheater.rho_in,preheater.rho_out,preheater.singularityRegime,preheater.systemSpec,preheater.u_in,preheater.u_out,preheater.v_in,preheater.v_out,preheater.w_amb,preheater.w_exp,preheater.w_exp_net,pump.L,pump.P,pump.P_nom,pump.TC,pump.adiabaticModel.eta_is,pump.adiabaticModel.h_in,pump.adiabaticModel.h_out,pump.adiabaticModel.h_out_is,pump.adiabaticModel.p_out,pump.adiabaticModel.s_in,pump.adiabaticModel.state_in.T,pump.adiabaticModel.state_in.d,pump.adiabaticModel.state_in.h,pump.adiabaticModel.state_in.p,pump.adiabaticModel.state_in.phase,pump.adiabaticModel.w_t,pump.adiabaticModel.w_t_is,pump.assertionLevel,pump.clip_p_out,pump.dh,pump.dp,pump.dp_fixed,pump.dp_nom,pump.dp_start,pump.dr_corr,pump.etaSpec,pump.eta_actual,pump.eta_fixed,pump.eta_is,pump.h_in,pump.h_out,pump.initM_flow,der(pump.inlet.m_flow),pump.inlet.m_flow,pump.inlet.r,pump.inlet.state.T,pump.inlet.state.d,pump.inlet.state.h,pump.inlet.state.p,pump.inlet.state.phase,pump.m_acceleration_0,pump.m_flow,pump.m_flowStateSelect,pump.m_flow_0,pump.outlet.m_flow,pump.outlet.r,pump.outlet.state.T,pump.outlet.state.d,pump.outlet.state.h,pump.outlet.state.p,pump.outlet.state.phase,pump.outletSpec,pump.outletSpec_actual,pump.outletSpec_prescribed,pump.outletValueSpec,pump.pRatio,pump.pRatio_fixed,pump.p_in,pump.p_min,pump.p_out,pump.p_out_fixed,pump.singularityRegime,superheater.L,superheater.P,superheater.Q_flow,superheater.T_out_fixed,superheater.assertionLevel,superheater.clip_p_out,superheater.dT,superheater.dT_fixed,superheater.dh,superheater.dh_fixed,superheater.dp,superheater.dr_corr,superheater.du,superheater.h_in,superheater.h_out,superheater.h_out_fixed,superheater.initM_flow,der(superheater.inlet.m_flow),superheater.inlet.m_flow,superheater.inlet.r,superheater.inlet.state.T,superheater.inlet.state.d,superheater.inlet.state.h,superheater.inlet.state.p,superheater.inlet.state.phase,superheater.m_acceleration_0,superheater.m_flow,superheater.m_flowStateSelect,superheater.m_flow_0,superheater.outlet.m_flow,superheater.outlet.r,superheater.outlet.state.T,superheater.outlet.state.d,superheater.outlet.state.h,superheater.outlet.state.p,superheater.outlet.state.phase,superheater.outletSpec,superheater.outletSpec_actual,superheater.outletSpec_prescribed,superheater.outletValueSpec,superheater.p,superheater.p_in,superheater.p_inf,superheater.p_min,superheater.p_out,superheater.q,superheater.rho_in,superheater.rho_out,superheater.singularityRegime,superheater.systemSpec,superheater.u_in,superheater.u_out,superheater.v_in,superheater.v_out,superheater.w_amb,superheater.w_exp,superheater.w_exp_net,turbine.L,turbine.P,turbine.P_nom,turbine.TC,turbine.adiabaticModel.eta_is,turbine.adiabaticModel.h_in,turbine.adiabaticModel.h_out,turbine.adiabaticModel.h_out_is,turbine.adiabaticModel.p_out,turbine.adiabaticModel.s_in,turbine.adiabaticModel.state_in.T,turbine.adiabaticModel.state_in.d,turbine.adiabaticModel.state_in.h,turbine.adiabaticModel.state_in.p,turbine.adiabaticModel.state_in.phase,turbine.adiabaticModel.w_t,turbine.adiabaticModel.w_t_is,turbine.assertionLevel,turbine.clip_p_out,turbine.dh,turbine.dp,turbine.dp_fixed,turbine.dp_nom,turbine.dp_start,turbine.dr_corr,turbine.etaSpec,turbine.eta_actual,turbine.eta_fixed,turbine.eta_is,turbine.h_in,turbine.h_out,turbine.initM_flow,der(turbine.inlet.m_flow),turbine.inlet.m_flow,turbine.inlet.r,turbine.inlet.state.T,turbine.inlet.state.d,turbine.inlet.state.h,turbine.inlet.state.p,turbine.inlet.state.phase,turbine.m_acceleration_0,turbine.m_flow,turbine.m_flowStateSelect,turbine.m_flow_0,turbine.outlet.m_flow,turbine.outlet.r,turbine.outlet.state.T,turbine.outlet.state.d,turbine.outlet.state.h,turbine.outlet.state.p,turbine.outlet.state.phase,turbine.outletSpec,turbine.outletSpec_actual,turbine.outletValueSpec,turbine.pRatio,turbine.pRatio_fixed,turbine.p_in,turbine.p_min,turbine.p_out,turbine.p_out_fixed,turbine.singularityRegime,vaporQualitySensor.TC,vaporQualitySensor.digits,vaporQualitySensor.direct_value,vaporQualitySensor.init,vaporQualitySensor.inlet.m_flow,vaporQualitySensor.inlet.r,vaporQualitySensor.inlet.state.T,vaporQualitySensor.inlet.state.d,vaporQualitySensor.inlet.state.h,vaporQualitySensor.inlet.state.p,vaporQualitySensor.inlet.state.phase,vaporQualitySensor.quantity,vaporQualitySensor.value,vaporQualitySensor.value_0,vaporQualitySensor.value_out,vaporQualitySetpoint.y Variables in the result:boiler.L,boiler.Q_flow,boiler.clip_p_out,boiler.dT,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.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.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.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: 9.374318431131542]