Running: ./testmodel.py --libraries=/home/hudson/saved_omc/libraries/.openmodelica/libraries --ompython_omhome=/usr ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.Volumes.Volume.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 0.001697/0.001697, allocations: 85.77 kB / 20.05 MB, free: 1.453 MB / 14.72 MB " [Timeout remaining time 180] loadFile("/home/hudson/saved_omc/libraries/.openmodelica/libraries/Complex 4.1.0+maint.om/package.mo", uses=false) [Timeout 180] "Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/Complex 4.1.0+maint.om/package.mo): time 0.001824/0.001824, allocations: 167.1 kB / 23.34 MB, free: 4.43 MB / 14.72 MB " [Timeout remaining time 180] loadFile("/home/hudson/saved_omc/libraries/.openmodelica/libraries/Modelica 4.1.0+maint.om/package.mo", uses=false) [Timeout 180] "Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/Modelica 4.1.0+maint.om/package.mo): time 1.545/1.545, allocations: 177.1 MB / 203.7 MB, free: 9.129 MB / 190.1 MB " [Timeout remaining time 178] loadFile("/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermofluidStream main/package.mo", uses=false) [Timeout 180] "Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermofluidStream main/package.mo): time 1.098/1.098, allocations: 116.1 MB / 376.1 MB, free: 7.504 MB / 350.1 MB " [Timeout remaining time 179] Using package ThermofluidStream with version 1.3.0 (/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermofluidStream main/package.mo) Using package Modelica with version 4.1.0 (/home/hudson/saved_omc/libraries/.openmodelica/libraries/Modelica 4.1.0+maint.om/package.mo) Using package Complex with version 4.1.0 (/home/hudson/saved_omc/libraries/.openmodelica/libraries/Complex 4.1.0+maint.om/package.mo) Using package ModelicaServices with version 4.1.0 (/home/hudson/saved_omc/libraries/.openmodelica/libraries/ModelicaServices 4.1.0+maint.om/package.mo) Running command: translateModel(ThermofluidStream.Idealized.Examples.Volumes.Volume,tolerance=1e-06,outputFormat="mat",numberOfIntervals=1000,variableFilter="A|CPUtime|EventCounter|NonlinearSystems.simulation.1..Calls|NonlinearSystems.simulation.1..Iterations|NonlinearSystems.simulation.1..Jacobians|NonlinearSystems.simulation.1..Residues|Time|V|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.CO2.H0|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.CO2.Hf|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.CO2.MM|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.CO2.R_s|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.CO2.Tlimit|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.CO2.ahigh.1.|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.CO2.ahigh.2.|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.CO2.ahigh.3.|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.CO2.ahigh.4.|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.CO2.ahigh.5.|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.CO2.ahigh.6.|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.CO2.ahigh.7.|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.CO2.alow.1.|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.CO2.alow.2.|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.CO2.alow.3.|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.CO2.alow.4.|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.CO2.alow.5.|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.CO2.alow.6.|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.CO2.alow.7.|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.CO2.bhigh.1.|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.CO2.bhigh.2.|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.CO2.blow.1.|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.CO2.blow.2.|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.SingleGases.CO2.data.H0|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.SingleGases.CO2.data.Hf|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.SingleGases.CO2.data.MM|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.SingleGases.CO2.data.R_s|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.SingleGases.CO2.data.Tlimit|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.SingleGases.CO2.data.ahigh.1.|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.SingleGases.CO2.data.ahigh.2.|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.SingleGases.CO2.data.ahigh.3.|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.SingleGases.CO2.data.ahigh.4.|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.SingleGases.CO2.data.ahigh.5.|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.SingleGases.CO2.data.ahigh.6.|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.SingleGases.CO2.data.ahigh.7.|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.SingleGases.CO2.data.alow.1.|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.SingleGases.CO2.data.alow.2.|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.SingleGases.CO2.data.alow.3.|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.SingleGases.CO2.data.alow.4.|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.SingleGases.CO2.data.alow.5.|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.SingleGases.CO2.data.alow.6.|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.SingleGases.CO2.data.alow.7.|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.SingleGases.CO2.data.bhigh.1.|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.SingleGases.CO2.data.bhigh.2.|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.SingleGases.CO2.data.blow.1.|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.SingleGases.CO2.data.blow.2.|compressor.L|compressor.P|compressor.P_nom|compressor.TC|compressor.adiabaticModel.eta_is|compressor.adiabaticModel.h_in|compressor.adiabaticModel.h_out|compressor.adiabaticModel.h_out_is|compressor.adiabaticModel.p_out|compressor.adiabaticModel.s_in|compressor.adiabaticModel.state_in.T|compressor.adiabaticModel.state_in.p|compressor.adiabaticModel.w_t|compressor.adiabaticModel.w_t_is|compressor.assertionLevel|compressor.clip_p_out|compressor.dh|compressor.dp|compressor.dp_fixed|compressor.dp_nom|compressor.dp_start|compressor.dr_corr|compressor.etaSpec|compressor.eta_actual|compressor.eta_fixed|compressor.eta_is|compressor.h_in|compressor.h_out|compressor.initM_flow|der.compressor.inlet.m_flow.|compressor.inlet.m_flow|compressor.inlet.r|compressor.inlet.state.T|compressor.inlet.state.p|compressor.m_acceleration_0|compressor.m_flow|compressor.m_flowStateSelect|compressor.m_flow_0|compressor.outlet.m_flow|compressor.outlet.r|compressor.outlet.state.T|compressor.outlet.state.p|compressor.outletSpec|compressor.outletSpec_actual|compressor.outletSpec_prescribed|compressor.outletValueSpec|compressor.pRatio|compressor.pRatio_fixed|compressor.p_in|compressor.p_min|compressor.p_out|compressor.p_out_fixed|compressor.singularityRegime|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|fixedTemperature.T|fixedTemperature.port.Q_flow|fixedTemperature.port.T|massFlowRate.L|massFlowRate.clip_p_out|massFlowRate.dp|massFlowRate.dr_corr|massFlowRate.h_in|massFlowRate.h_out|massFlowRate.initM_flow|der.massFlowRate.inlet.m_flow.|massFlowRate.inlet.m_flow|massFlowRate.inlet.r|massFlowRate.inlet.state.T|massFlowRate.inlet.state.p|massFlowRate.m_acceleration_0|massFlowRate.m_flow|massFlowRate.m_flowSpec|massFlowRate.m_flowStateSelect|massFlowRate.m_flow_0|massFlowRate.m_flow_actual|massFlowRate.m_flow_fixed|massFlowRate.outlet.m_flow|massFlowRate.outlet.r|massFlowRate.outlet.state.T|massFlowRate.outlet.state.p|massFlowRate.p_in|massFlowRate.p_min|massFlowRate.p_out|pressureTank.A|pressureTank.L|pressureTank.M|pressureTank.Q_flow|pressureTank.T_heatPort|pressureTank.T_start|pressureTank.U|pressureTank.U_med|pressureTank.V|pressureTank.V_par|pressureTank.W_v|pressureTank.d|pressureTank.density_derp_h|pressureTank.density_derp_h_set|der.pressureTank.M.|der.pressureTank.U_med.|der.pressureTank.m_flow_in.|der.pressureTank.m_flow_out.|pressureTank.h_in|pressureTank.h_out|pressureTank.h_start|pressureTank.heatPort.Q_flow|pressureTank.heatPort.T|pressureTank.inlet.m_flow|pressureTank.inlet.r|pressureTank.inlet.state.T|pressureTank.inlet.state.p|pressureTank.k_volume_damping|pressureTank.m_flow_assert|pressureTank.m_flow_in|pressureTank.m_flow_out|pressureTank.medium.MM|pressureTank.medium.R_s|pressureTank.medium.T|pressureTank.medium.T_degC|pressureTank.medium.X.1.|pressureTank.medium.d|pressureTank.medium.h|pressureTank.medium.p|pressureTank.medium.p_bar|pressureTank.medium.preferredMediumStates|pressureTank.medium.standardOrderComponents|pressureTank.medium.state.T|pressureTank.medium.state.p|pressureTank.medium.u|pressureTank.p_in|pressureTank.p_start|pressureTank.r|pressureTank.r_damping|pressureTank.r_in|pressureTank.r_out|pressureTank.state_in.T|pressureTank.state_in.p|pressureTank.state_out.T|pressureTank.state_out.p|r|source.L|source.T0|source.T0_par|source.h0|source.h0_par|der.source.outlet.m_flow.|source.outlet.m_flow|source.outlet.r|source.outlet.state.T|source.outlet.state.p|source.p0|source.p0_par|tankPressure.y",fileNamePrefix="ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.Volumes.Volume") translateModel(ThermofluidStream.Idealized.Examples.Volumes.Volume,tolerance=1e-06,outputFormat="mat",numberOfIntervals=1000,variableFilter="A|CPUtime|EventCounter|NonlinearSystems.simulation.1..Calls|NonlinearSystems.simulation.1..Iterations|NonlinearSystems.simulation.1..Jacobians|NonlinearSystems.simulation.1..Residues|Time|V|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.CO2.H0|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.CO2.Hf|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.CO2.MM|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.CO2.R_s|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.CO2.Tlimit|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.CO2.ahigh.1.|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.CO2.ahigh.2.|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.CO2.ahigh.3.|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.CO2.ahigh.4.|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.CO2.ahigh.5.|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.CO2.ahigh.6.|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.CO2.ahigh.7.|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.CO2.alow.1.|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.CO2.alow.2.|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.CO2.alow.3.|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.CO2.alow.4.|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.CO2.alow.5.|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.CO2.alow.6.|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.CO2.alow.7.|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.CO2.bhigh.1.|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.CO2.bhigh.2.|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.CO2.blow.1.|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.CO2.blow.2.|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.SingleGases.CO2.data.H0|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.SingleGases.CO2.data.Hf|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.SingleGases.CO2.data.MM|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.SingleGases.CO2.data.R_s|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.SingleGases.CO2.data.Tlimit|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.SingleGases.CO2.data.ahigh.1.|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.SingleGases.CO2.data.ahigh.2.|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.SingleGases.CO2.data.ahigh.3.|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.SingleGases.CO2.data.ahigh.4.|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.SingleGases.CO2.data.ahigh.5.|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.SingleGases.CO2.data.ahigh.6.|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.SingleGases.CO2.data.ahigh.7.|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.SingleGases.CO2.data.alow.1.|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.SingleGases.CO2.data.alow.2.|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.SingleGases.CO2.data.alow.3.|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.SingleGases.CO2.data.alow.4.|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.SingleGases.CO2.data.alow.5.|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.SingleGases.CO2.data.alow.6.|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.SingleGases.CO2.data.alow.7.|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.SingleGases.CO2.data.bhigh.1.|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.SingleGases.CO2.data.bhigh.2.|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.SingleGases.CO2.data.blow.1.|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.SingleGases.CO2.data.blow.2.|compressor.L|compressor.P|compressor.P_nom|compressor.TC|compressor.adiabaticModel.eta_is|compressor.adiabaticModel.h_in|compressor.adiabaticModel.h_out|compressor.adiabaticModel.h_out_is|compressor.adiabaticModel.p_out|compressor.adiabaticModel.s_in|compressor.adiabaticModel.state_in.T|compressor.adiabaticModel.state_in.p|compressor.adiabaticModel.w_t|compressor.adiabaticModel.w_t_is|compressor.assertionLevel|compressor.clip_p_out|compressor.dh|compressor.dp|compressor.dp_fixed|compressor.dp_nom|compressor.dp_start|compressor.dr_corr|compressor.etaSpec|compressor.eta_actual|compressor.eta_fixed|compressor.eta_is|compressor.h_in|compressor.h_out|compressor.initM_flow|der.compressor.inlet.m_flow.|compressor.inlet.m_flow|compressor.inlet.r|compressor.inlet.state.T|compressor.inlet.state.p|compressor.m_acceleration_0|compressor.m_flow|compressor.m_flowStateSelect|compressor.m_flow_0|compressor.outlet.m_flow|compressor.outlet.r|compressor.outlet.state.T|compressor.outlet.state.p|compressor.outletSpec|compressor.outletSpec_actual|compressor.outletSpec_prescribed|compressor.outletValueSpec|compressor.pRatio|compressor.pRatio_fixed|compressor.p_in|compressor.p_min|compressor.p_out|compressor.p_out_fixed|compressor.singularityRegime|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|fixedTemperature.T|fixedTemperature.port.Q_flow|fixedTemperature.port.T|massFlowRate.L|massFlowRate.clip_p_out|massFlowRate.dp|massFlowRate.dr_corr|massFlowRate.h_in|massFlowRate.h_out|massFlowRate.initM_flow|der.massFlowRate.inlet.m_flow.|massFlowRate.inlet.m_flow|massFlowRate.inlet.r|massFlowRate.inlet.state.T|massFlowRate.inlet.state.p|massFlowRate.m_acceleration_0|massFlowRate.m_flow|massFlowRate.m_flowSpec|massFlowRate.m_flowStateSelect|massFlowRate.m_flow_0|massFlowRate.m_flow_actual|massFlowRate.m_flow_fixed|massFlowRate.outlet.m_flow|massFlowRate.outlet.r|massFlowRate.outlet.state.T|massFlowRate.outlet.state.p|massFlowRate.p_in|massFlowRate.p_min|massFlowRate.p_out|pressureTank.A|pressureTank.L|pressureTank.M|pressureTank.Q_flow|pressureTank.T_heatPort|pressureTank.T_start|pressureTank.U|pressureTank.U_med|pressureTank.V|pressureTank.V_par|pressureTank.W_v|pressureTank.d|pressureTank.density_derp_h|pressureTank.density_derp_h_set|der.pressureTank.M.|der.pressureTank.U_med.|der.pressureTank.m_flow_in.|der.pressureTank.m_flow_out.|pressureTank.h_in|pressureTank.h_out|pressureTank.h_start|pressureTank.heatPort.Q_flow|pressureTank.heatPort.T|pressureTank.inlet.m_flow|pressureTank.inlet.r|pressureTank.inlet.state.T|pressureTank.inlet.state.p|pressureTank.k_volume_damping|pressureTank.m_flow_assert|pressureTank.m_flow_in|pressureTank.m_flow_out|pressureTank.medium.MM|pressureTank.medium.R_s|pressureTank.medium.T|pressureTank.medium.T_degC|pressureTank.medium.X.1.|pressureTank.medium.d|pressureTank.medium.h|pressureTank.medium.p|pressureTank.medium.p_bar|pressureTank.medium.preferredMediumStates|pressureTank.medium.standardOrderComponents|pressureTank.medium.state.T|pressureTank.medium.state.p|pressureTank.medium.u|pressureTank.p_in|pressureTank.p_start|pressureTank.r|pressureTank.r_damping|pressureTank.r_in|pressureTank.r_out|pressureTank.state_in.T|pressureTank.state_in.p|pressureTank.state_out.T|pressureTank.state_out.p|r|source.L|source.T0|source.T0_par|source.h0|source.h0_par|der.source.outlet.m_flow.|source.outlet.m_flow|source.outlet.r|source.outlet.state.T|source.outlet.state.p|source.p0|source.p0_par|tankPressure.y",fileNamePrefix="ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.Volumes.Volume") [Timeout 660] "Notification: Performance of FrontEnd - Absyn->SCode: time 2.257e-05/2.257e-05, allocations: 2.281 kB / 0.5547 GB, free: 13.67 MB / 478.1 MB Notification: Performance of NFInst.instantiate(ThermofluidStream.Idealized.Examples.Volumes.Volume): time 0.5801/0.5801, allocations: 152.6 MB / 0.7037 GB, free: 6.449 MB / 0.5919 GB Notification: Performance of NFInst.instExpressions: time 0.004289/0.5844, allocations: 2.475 MB / 0.7062 GB, free: 6.434 MB / 0.5919 GB Notification: Performance of NFInst.updateImplicitVariability: time 0.0006566/0.5851, allocations: 35.84 kB / 0.7062 GB, free: 6.434 MB / 0.5919 GB Notification: Performance of NFTyping.typeComponents: time 0.0008384/0.5859, allocations: 243.4 kB / 0.7064 GB, free: 6.426 MB / 0.5919 GB Notification: Performance of NFTyping.typeBindings: time 0.003486/0.5894, allocations: 1.051 MB / 0.7075 GB, free: 6.387 MB / 0.5919 GB Notification: Performance of NFTyping.typeClassSections: time 0.002067/0.5915, allocations: 0.6554 MB / 0.7081 GB, free: 6.371 MB / 0.5919 GB Notification: Performance of NFFlatten.flatten: time 0.002098/0.5936, allocations: 1.302 MB / 0.7094 GB, free: 6.371 MB / 0.5919 GB Notification: Performance of NFFlatten.resolveConnections: time 0.000273/0.5938, allocations: 68.41 kB / 0.7094 GB, free: 6.359 MB / 0.5919 GB Notification: Performance of NFEvalConstants.evaluate: time 0.00238/0.5962, allocations: 1.001 MB / 0.7104 GB, free: 6.34 MB / 0.5919 GB Notification: Performance of NFSimplifyModel.simplify: time 0.0004321/0.5966, allocations: 253.8 kB / 0.7106 GB, free: 6.305 MB / 0.5919 GB Notification: Performance of NFPackage.collectConstants: time 8.628e-05/0.5967, allocations: 40.47 kB / 0.7107 GB, free: 6.305 MB / 0.5919 GB Notification: Performance of NFFlatten.collectFunctions: time 0.002237/0.599, allocations: 0.7671 MB / 0.7114 GB, free: 6.262 MB / 0.5919 GB Notification: Performance of combineBinaries: time 0.0008496/0.5998, allocations: 1.043 MB / 0.7125 GB, free: 5.816 MB / 0.5919 GB Notification: Performance of replaceArrayConstructors: time 0.0003782/0.6002, allocations: 0.6899 MB / 0.7131 GB, free: 5.445 MB / 0.5919 GB Notification: Performance of NFVerifyModel.verify: time 0.000137/0.6003, allocations: 60.03 kB / 0.7132 GB, free: 5.445 MB / 0.5919 GB Notification: Performance of FrontEnd: time 0.0003458/0.6007, allocations: 114.7 kB / 0.7133 GB, free: 5.434 MB / 0.5919 GB Notification: Model statistics after passing the front-end and creating the data structures used by the back-end: * Number of equations: 98 (92) * Number of variables: 100 (100) Notification: Performance of [SIM] Bindings: time 0.002667/0.6033, allocations: 2.699 MB / 0.7159 GB, free: 4.363 MB / 0.5919 GB Notification: Performance of [SIM] FunctionAlias: time 0.0005694/0.6039, allocations: 452.5 kB / 0.7164 GB, free: 4.262 MB / 0.5919 GB Notification: Performance of [SIM] Early Inline: time 0.001776/0.6057, allocations: 1.826 MB / 0.7181 GB, free: 4.145 MB / 0.5919 GB Notification: Performance of [SIM] Simplify 1: time 0.0003333/0.606, allocations: 239 kB / 0.7184 GB, free: 4.07 MB / 0.5919 GB Notification: Performance of [SIM] Alias: time 0.002858/0.6089, allocations: 2.297 MB / 0.7206 GB, free: 3.238 MB / 0.5919 GB Notification: Performance of [SIM] Simplify 2: time 0.0002547/0.6091, allocations: 191.4 kB / 0.7208 GB, free: 3.168 MB / 0.5919 GB Notification: Performance of [SIM] Remove Stream: time 0.0001397/0.6093, allocations: 147.9 kB / 0.7209 GB, free: 3.105 MB / 0.5919 GB Notification: Performance of [SIM] Detect States: time 0.0004219/0.6097, allocations: 432.4 kB / 0.7214 GB, free: 2.934 MB / 0.5919 GB Notification: Performance of [SIM] Events: time 8.598e-05/0.6098, allocations: 58.69 kB / 0.7214 GB, free: 2.93 MB / 0.5919 GB Notification: Performance of [SIM] Partitioning: time 0.0006093/0.6104, allocations: 0.5655 MB / 0.722 GB, free: 2.793 MB / 0.5919 GB Error: Internal error NBSorting.tarjan failed to sort system: System Variables (66/66) ************************** (1|1) [ALGB] (1) final Real compressor.adiabaticModel.s_in = ThermofluidStream.Idealized.Examples.Volumes.Volume.compressor.adiabaticModel.Medium.specificEntropy(compressor.adiabaticModel.state_in) (min = -1e7, max = 1e7, nominal = 1000.0) (2|2) [ALGB] (1) final input Real compressor.adiabaticModel.state_in.p = compressor.inlet.state.p (start = 1e6, min = 0.0, max = 1e8, nominal = 1e6) (3|3) [ALGB] (1) output Real source.outlet.state.p (start = 1e6, min = 0.0, max = 1e8, nominal = 1e6) (4|4) [ALGB] (1) Real $FUN_17 (5|5) [ALGB] (1) protected Real pressureTank.d = pressureTank.k_volume_damping * sqrt(abs((2.0 * pressureTank.L) / (pressureTank.V_par * max(pressureTank.density_derp_h_set, 1e-10)))) (6|6) [ALGB] (1) Real $FUN_16 (7|7) [ALGB] (1) protected Real pressureTank.p_in = ThermofluidStream.Idealized.Examples.Volumes.Volume.pressureTank.Medium.pressure(pressureTank.state_in) (start = 1e6, min = 0.0, max = 1e8, nominal = 1e6) (8|8) [ALGB] (1) input Real pressureTank.inlet.state.p = pressureTank.state_in.p (start = 1e6, min = 0.0, max = 1e8, nominal = 1e6) (9|9) [ALGB] (1) Real compressor.outlet.r (10|10) [ALGB] (1) Real $FUN_14 (11|11) [ALGB] (1) Real $FUN_13 (12|12) [ALGB] (1) protected Real pressureTank.r_out (13|13) [ALGB] (1) Real compressor.h_out (start = 212805.6215135368, min = -1e10, max = 1e10, nominal = 1e5) (14|14) [ALGB] (1) Real compressor.p_in = ThermofluidStream.Idealized.Examples.Volumes.Volume.compressor.Medium.pressure(compressor.inlet.state) (start = 1e6, min = 0.0, max = 1e8, nominal = 1e6) (15|15) [ALGB] (1) Real massFlowRate.dr_corr (16|16) [ALGB] (1) Real compressor.dp (17|17) [ALGB] (1) input Real pressureTank.inlet.state.T = pressureTank.state_in.T (start = 500.0, min = 200.0, max = 6000.0, nominal = 500.0) (18|18) [ALGB] (1) protected Real pressureTank.h_out = if noEvent((-0.0) >= 0.0) then ThermofluidStream.Idealized.Examples.Volumes.Volume.pressureTank.Medium.specificEnthalpy(pressureTank.state_out) else pressureTank.medium.h (start = 212805.6215135368, min = -1e10, max = 1e10, nominal = 1e5) (19|19) [DER-] (1) Real $DER.pressureTank.U_med (20|20) [ALGB] (1) Real compressor.dh (21|21) [ALGB] (1) protected Real pressureTank.state_out.p (start = 1e6, min = 0.0, max = 1e8, nominal = 1e6) (22|22) [ALGB] (1) final Real compressor.adiabaticModel.h_out_is = ThermofluidStream.Idealized.Examples.Volumes.Volume.compressor.adiabaticModel.Medium.specificEnthalpy_psX(compressor.p_out, compressor.adiabaticModel.s_in, {}) (start = 212805.6215135368, min = -1e10, max = 1e10, nominal = 1e5) (23|23) [ALGB] (1) Real pressureTank.medium.u (min = -1e8, max = 1e8, nominal = 1e6) (24|24) [ALGB] (1) Real $FUN_4.T (25|25) [ALGB] (1) Real $FUN_3.T (26|26) [ALGB] (1) Real compressor.pRatio = compressor.p_out / compressor.p_in (27|27) [ALGB] (1) protected Real pressureTank.state_in.T (start = 500.0, min = 200.0, max = 6000.0, nominal = 500.0) (28|28) [ALGB] (1) Real $FUN_1.T (29|29) [ALGB] (1) Real pressureTank.medium.state.p (start = 1e6, min = 0.0, max = 1e8, nominal = 1e6) (30|30) [ALGB] (1) input Real compressor.inlet.state.T (start = 500.0, min = 200.0, max = 6000.0, nominal = 500.0) (31|31) [ALGB] (1) output Real massFlowRate.outlet.state.T (start = 500.0, min = 200.0, max = 6000.0, nominal = 500.0) (32|32) [ALGB] (1) protected Real pressureTank.state_out.T (start = 500.0, min = 200.0, max = 6000.0, nominal = 500.0) (33|33) [ALGB] (1) final Real compressor.adiabaticModel.p_in = ThermofluidStream.Idealized.Examples.Volumes.Volume.compressor.adiabaticModel.Medium.pressure(compressor.adiabaticModel.state_in) (start = 1e6, min = 0.0, max = 1e8, nominal = 1e6) (34|34) [ALGB] (1) input Real compressor.inlet.state.p (start = 1e6, min = 0.0, max = 1e8, nominal = 1e6) (35|35) [ALGB] (1) Real pressureTank.Q_flow (36|36) [ALGB] (1) protected Real pressureTank.r_in (37|37) [ALGB] (1) Real massFlowRate.p_in = ThermofluidStream.Idealized.Examples.Volumes.Volume.massFlowRate.Medium.pressure(massFlowRate.inlet.state) (start = 1e6, min = 0.0, max = 1e8, nominal = 1e6) (38|38) [ALGB] (1) final Real compressor.adiabaticModel.w_t_is (39|39) [ALGB] (1) Real pressureTank.medium.h (40|40) [ALGB] (1) input Real massFlowRate.inlet.state.p (start = 1e6, min = 0.0, max = 1e8, nominal = 1e6) (41|41) [ALGB] (1) Real massFlowRate.h_out (start = 212805.6215135368, min = -1e10, max = 1e10, nominal = 1e5) (42|42) [DER-] (1) Real $DER.pressureTank.M (43|43) [ALGB] (1) final Real compressor.adiabaticModel.w_t (44|44) [ALGB] (1) Real pressureTank.medium.d (start = 10.0, min = 0.0, max = 1e5, nominal = 10.0) (45|45) [ALGB] (1) input Real massFlowRate.inlet.state.T (start = 500.0, min = 200.0, max = 6000.0, nominal = 500.0) (46|46) [ALGB] (1) protected Real pressureTank.r (47|47) [ALGB] (1) output Real source.outlet.state.T (start = 500.0, min = 200.0, max = 6000.0, nominal = 500.0) (48|48) [ALGB] (1) Real $FUN_4.p (49|49) [ALGB] (1) output Real compressor.outlet.state.T (start = 500.0, min = 200.0, max = 6000.0, nominal = 500.0) (50|50) [ALGB] (1) Real $FUN_3.p (51|51) [ALGB] (1) protected Real pressureTank.state_in.p (start = 1e6, min = 0.0, max = 1e8, nominal = 1e6) (52|52) [ALGB] (1) final Real compressor.adiabaticModel.h_in = ThermofluidStream.Idealized.Examples.Volumes.Volume.compressor.adiabaticModel.Medium.specificEnthalpy(compressor.adiabaticModel.state_in) (start = 212805.6215135368, min = -1e10, max = 1e10, nominal = 1e5) (53|53) [ALGB] (1) Real $FUN_1.p (54|54) [DISC] (1) Boolean $SEV_0 (55|55) [ALGB] (1) protected Real pressureTank.r_damping = pressureTank.d * der(pressureTank.M) (56|56) [ALGB] (1) final input Real compressor.adiabaticModel.state_in.T = compressor.inlet.state.T (start = 500.0, min = 200.0, max = 6000.0, nominal = 500.0) (57|57) [ALGB] (1) output Real massFlowRate.outlet.state.p (start = 1e6, min = 0.0, max = 1e8, nominal = 1e6) (58|58) [ALGB] (1) Real pressureTank.medium.T (start = 500.0, min = 200.0, max = 6000.0, nominal = 500.0, StateSelect = default) (59|59) [ALGB] (1) Real massFlowRate.p_out (start = 1e6, min = 0.0, max = 1e8, nominal = 1e6) (60|60) [ALGB] (1) Real compressor.h_in = ThermofluidStream.Idealized.Examples.Volumes.Volume.compressor.Medium.specificEnthalpy(compressor.inlet.state) (start = 212805.6215135368, min = -1e10, max = 1e10, nominal = 1e5) (61|61) [ALGB] (1) Real compressor.p_out (start = 1e6, min = 0.0, max = 1e8, nominal = 1e6) (62|62) [ALGB] (1) protected Real pressureTank.h_in = if noEvent(massFlowRate.m_flow_fixed >= 0.0) then ThermofluidStream.Idealized.Examples.Volumes.Volume.pressureTank.Medium.specificEnthalpy(pressureTank.state_in) else pressureTank.medium.h (start = 212805.6215135368, min = -1e10, max = 1e10, nominal = 1e5) (63|63) [ALGB] (1) Real compressor.P_in_internal (64|64) [ALGB] (1) output Real compressor.outlet.state.p (start = 1e6, min = 0.0, max = 1e8, nominal = 1e6) (65|65) [ALGB] (1) Real source.outlet.r (66|66) [ALGB] (1) Real pressureTank.medium.state.T (start = 500.0, min = 200.0, max = 6000.0, nominal = 500.0) System Equations (58/64) ************************** (1|1) [RECD] (2) compressor.outlet.state = $FUN_3 ($RES_SIM_12) (2|3) [SCAL] (1) compressor.p_out = compressor.p_in + compressor.dp ($RES_SIM_14) (3|4) [SCAL] (1) compressor.outlet.r = source.outlet.r - 0.0 * compressor.L ($RES_SIM_15) (4|5) [SCAL] (1) pressureTank.Q_flow = pressureTank.A * pressureTank.U * (fixedTemperature.T - pressureTank.medium.T) ($RES_SIM_31) (5|6) [SCAL] (1) $DER.pressureTank.U_med = pressureTank.h_in * massFlowRate.m_flow_fixed + pressureTank.Q_flow ($RES_SIM_32) (6|7) [SCAL] (1) $DER.pressureTank.M = massFlowRate.m_flow_fixed ($RES_SIM_33) (7|8) [SCAL] (1) compressor.P_in_internal = massFlowRate.m_flow_fixed * compressor.dh ($RES_SIM_18) (8|9) [SCAL] (1) 0.0 = pressureTank.r_out - pressureTank.r_damping ($RES_SIM_34) (9|10) [SCAL] (1) $SEV_0 = compressor.p_out >= compressor.adiabaticModel.p_in ($RES_EVT_133) (10|11) [SCAL] (1) 0.0 * pressureTank.L = pressureTank.r_in - (pressureTank.r_damping + pressureTank.r) ($RES_SIM_35) (11|12) [SCAL] (1) pressureTank.medium.u = pressureTank.medium.h - 188.9244822140674 * pressureTank.medium.T ($RES_SIM_50) (12|13) [RECD] (2) pressureTank.state_out = pressureTank.medium.state ($RES_SIM_39) (13|15) [SCAL] (1) pressureTank.inlet.state.p = massFlowRate.outlet.state.p ($RES_SIM_70) (14|16) [RECD] (2) source.outlet.state = $FUN_1 ($RES_SIM_55) (15|18) [SCAL] (1) source.L * 0.0 = source.outlet.r ($RES_SIM_56) (16|19) [SCAL] (1) source.outlet.state.T = compressor.inlet.state.T ($RES_SIM_72) (17|20) [SCAL] (1) source.outlet.state.p = compressor.inlet.state.p ($RES_SIM_73) (18|21) [SCAL] (1) compressor.p_in = compressor.inlet.state.p ($RES_AUX_110) (19|22) [SCAL] (1) compressor.h_in = ThermofluidStream.Media.myMedia.IdealGases.Common.Functions.h_T(ThermofluidStream.Media.myMedia.IdealGases.Common.DataRecord(\"CO2\", 0.0440095, -8.941478544405185e6, 212805.6215135368, 1000.0, {49436.5054, -626.411601, 5.30172524, 0.002503813816, -2.127308728e-7, -7.68998878e-10, 2.849677801e-13}, {-45281.9846, -7.04827944}, {117696.2419, -1788.791477, 8.29152319, -9.22315678e-5, 4.86367688e-9, -1.891053312e-12, 6.330036589999999e-16}, {-39083.5059, -26.52669281}, 188.9244822140674), compressor.inlet.state.T, true, ThermofluidStream.Media.myMedia.Interfaces.Choices.ReferenceEnthalpy.ZeroAt0K, 0.0) ($RES_AUX_111) (20|23) [SCAL] (1) pressureTank.d = pressureTank.k_volume_damping * $FUN_17 ($RES_BND_82) (21|24) [SCAL] (1) compressor.adiabaticModel.p_in = compressor.adiabaticModel.state_in.p ($RES_AUX_112) (22|25) [SCAL] (1) $FUN_1.p = source.p0_par ($RES_SIM_123) (23|26) [SCAL] (1) pressureTank.r_damping = pressureTank.d * $DER.pressureTank.M ($RES_BND_83) (24|27) [SCAL] (1) compressor.adiabaticModel.s_in = (if noEvent(compressor.adiabaticModel.state_in.T < 1000.0) then 188.9244822140674 * (((-7.04827944) + 626.411601 / compressor.adiabaticModel.state_in.T + 5.30172524 * log(compressor.adiabaticModel.state_in.T) + compressor.adiabaticModel.state_in.T * (0.002503813816 + compressor.adiabaticModel.state_in.T * ((-1.063654364e-7) + compressor.adiabaticModel.state_in.T * ((-2.563329593333333e-10) + 7.1241945025e-14 * compressor.adiabaticModel.state_in.T)))) - 24718.2527 / (compressor.adiabaticModel.state_in.T * compressor.adiabaticModel.state_in.T)) else 188.9244822140674 * (((-26.52669281) + 1788.791477 / compressor.adiabaticModel.state_in.T + 8.29152319 * log(compressor.adiabaticModel.state_in.T) + compressor.adiabaticModel.state_in.T * ((-9.22315678e-5) + compressor.adiabaticModel.state_in.T * (2.43183844e-9 + compressor.adiabaticModel.state_in.T * ((-6.303511039999999e-13) + 1.5825091474999999e-16 * compressor.adiabaticModel.state_in.T)))) - 58848.12095 / (compressor.adiabaticModel.state_in.T * compressor.adiabaticModel.state_in.T))) - 188.9244822140674 * log(9.869232667160129e-6 * compressor.adiabaticModel.state_in.p) ($RES_AUX_113) (25|28) [SCAL] (1) $FUN_1.T = source.T0_par ($RES_SIM_124) (26|29) [SCAL] (1) compressor.adiabaticModel.h_in = ThermofluidStream.Media.myMedia.IdealGases.Common.Functions.h_T(ThermofluidStream.Media.myMedia.IdealGases.Common.DataRecord(\"CO2\", 0.0440095, -8.941478544405185e6, 212805.6215135368, 1000.0, {49436.5054, -626.411601, 5.30172524, 0.002503813816, -2.127308728e-7, -7.68998878e-10, 2.849677801e-13}, {-45281.9846, -7.04827944}, {117696.2419, -1788.791477, 8.29152319, -9.22315678e-5, 4.86367688e-9, -1.891053312e-12, 6.330036589999999e-16}, {-39083.5059, -26.52669281}, 188.9244822140674), compressor.adiabaticModel.state_in.T, true, ThermofluidStream.Media.myMedia.Interfaces.Choices.ReferenceEnthalpy.ZeroAt0K, 0.0) ($RES_AUX_114) (27|30) [SCAL] (1) $FUN_3.p = compressor.p_out ($RES_SIM_125) (28|31) [SCAL] (1) pressureTank.h_in = if noEvent(massFlowRate.m_flow_fixed >= 0.0) then $FUN_14 else pressureTank.medium.h ($RES_BND_85) (29|32) [SCAL] (1) compressor.adiabaticModel.h_out_is = ThermofluidStream.Media.myMedia.IdealGases.Common.Functions.h_T(ThermofluidStream.Media.myMedia.IdealGases.Common.DataRecord(\"CO2\", 0.0440095, -8.941478544405185e6, 212805.6215135368, 1000.0, {49436.5054, -626.411601, 5.30172524, 0.002503813816, -2.127308728e-7, -7.68998878e-10, 2.849677801e-13}, {-45281.9846, -7.04827944}, {117696.2419, -1788.791477, 8.29152319, -9.22315678e-5, 4.86367688e-9, -1.891053312e-12, 6.330036589999999e-16}, {-39083.5059, -26.52669281}, 188.9244822140674), ThermofluidStream.Idealized.Examples.Volumes.Volume.compressor.adiabaticModel.Medium.T_ps(compressor.p_out, compressor.adiabaticModel.s_in), true, ThermofluidStream.Media.myMedia.Interfaces.Choices.ReferenceEnthalpy.ZeroAt0K, 0.0) ($RES_AUX_115) (30|33) [SCAL] (1) $FUN_3.T = ThermofluidStream.Idealized.Examples.Volumes.Volume.compressor.Medium.T_h(compressor.h_out) ($RES_SIM_126) (31|34) [SCAL] (1) pressureTank.h_out = $FUN_13 ($RES_BND_86) (32|35) [SCAL] (1) massFlowRate.p_in = massFlowRate.inlet.state.p ($RES_AUX_116) (33|36) [SCAL] (1) $FUN_4.p = massFlowRate.p_out ($RES_SIM_127) (34|37) [SCAL] (1) massFlowRate.h_out = ThermofluidStream.Media.myMedia.IdealGases.Common.Functions.h_T(ThermofluidStream.Media.myMedia.IdealGases.Common.DataRecord(\"CO2\", 0.0440095, -8.941478544405185e6, 212805.6215135368, 1000.0, {49436.5054, -626.411601, 5.30172524, 0.002503813816, -2.127308728e-7, -7.68998878e-10, 2.849677801e-13}, {-45281.9846, -7.04827944}, {117696.2419, -1788.791477, 8.29152319, -9.22315678e-5, 4.86367688e-9, -1.891053312e-12, 6.330036589999999e-16}, {-39083.5059, -26.52669281}, 188.9244822140674), massFlowRate.inlet.state.T, true, ThermofluidStream.Media.myMedia.Interfaces.Choices.ReferenceEnthalpy.ZeroAt0K, 0.0) ($RES_AUX_117) (35|38) [SCAL] (1) $FUN_4.T = ThermofluidStream.Idealized.Examples.Volumes.Volume.massFlowRate.Medium.T_h(massFlowRate.h_out) ($RES_SIM_128) (36|39) [SCAL] (1) compressor.dh = compressor.h_out - compressor.h_in ($RES_SIM_20) (37|40) [RECD] (2) pressureTank.inlet.state = pressureTank.state_in ($RES_BND_101) (38|42) [RECD] (2) compressor.adiabaticModel.state_in = compressor.inlet.state ($RES_BND_102) (39|44) [SCAL] (1) compressor.adiabaticModel.w_t = if $SEV_0 then compressor.adiabaticModel.w_t_is / compressor.eta_fixed else compressor.adiabaticModel.w_t_is * compressor.eta_fixed ($RES_SIM_25) (40|45) [SCAL] (1) compressor.adiabaticModel.w_t = compressor.h_out - compressor.adiabaticModel.h_in ($RES_SIM_28) (41|46) [SCAL] (1) compressor.adiabaticModel.w_t_is = compressor.adiabaticModel.h_out_is - compressor.adiabaticModel.h_in ($RES_SIM_29) (42|47) [SCAL] (1) pressureTank.medium.state.p = compressor.p_out ($RES_SIM_47) (43|48) [SCAL] (1) pressureTank.medium.state.T = pressureTank.medium.T ($RES_SIM_48) (44|49) [SCAL] (1) pressureTank.medium.d = (0.005293120236618753 * compressor.p_out) / pressureTank.medium.T ($RES_SIM_49) (45|50) [SCAL] (1) compressor.outlet.state.T = massFlowRate.inlet.state.T ($RES_SIM_66) (46|51) [SCAL] (1) pressureTank.r_in = (massFlowRate.dr_corr + compressor.outlet.r) - 0.0 * massFlowRate.L ($RES_SIM_6) (47|52) [SCAL] (1) compressor.outlet.state.p = massFlowRate.inlet.state.p ($RES_SIM_67) (48|53) [SCAL] (1) massFlowRate.p_out = max(massFlowRate.p_min, massFlowRate.p_in) ($RES_SIM_5) (49|54) [SCAL] (1) massFlowRate.dr_corr = massFlowRate.p_in - massFlowRate.p_out ($RES_SIM_4) (50|55) [SCAL] (1) pressureTank.inlet.state.T = massFlowRate.outlet.state.T ($RES_SIM_69) (51|56) [SCAL] (1) compressor.pRatio = compressor.p_out / compressor.p_in ($RES_BND_90) (52|57) [SCAL] (1) pressureTank.medium.h = ThermofluidStream.Media.myMedia.IdealGases.Common.Functions.h_T(ThermofluidStream.Media.myMedia.IdealGases.Common.DataRecord(\"CO2\", 0.0440095, -8.941478544405185e6, 212805.6215135368, 1000.0, {49436.5054, -626.411601, 5.30172524, 0.002503813816, -2.127308728e-7, -7.68998878e-10, 2.849677801e-13}, {-45281.9846, -7.04827944}, {117696.2419, -1788.791477, 8.29152319, -9.22315678e-5, 4.86367688e-9, -1.891053312e-12, 6.330036589999999e-16}, {-39083.5059, -26.52669281}, 188.9244822140674), pressureTank.medium.T, true, ThermofluidStream.Media.myMedia.Interfaces.Choices.ReferenceEnthalpy.ZeroAt0K, 0.0) ($RES_AUX_120) (53|58) [SCAL] (1) $FUN_17 = sqrt($FUN_16) ($RES_AUX_105) (54|59) [RECD] (2) massFlowRate.outlet.state = $FUN_4 ($RES_SIM_3) (55|61) [SCAL] (1) $FUN_16 = abs((2.0 * pressureTank.L) / (pressureTank.V_par * max(pressureTank.density_derp_h_set, 1e-10))) ($RES_AUX_106) (56|62) [SCAL] (1) pressureTank.p_in = pressureTank.state_in.p ($RES_AUX_107) (57|63) [SCAL] (1) $FUN_14 = ThermofluidStream.Media.myMedia.IdealGases.Common.Functions.h_T(ThermofluidStream.Media.myMedia.IdealGases.Common.DataRecord(\"CO2\", 0.0440095, -8.941478544405185e6, 212805.6215135368, 1000.0, {49436.5054, -626.411601, 5.30172524, 0.002503813816, -2.127308728e-7, -7.68998878e-10, 2.849677801e-13}, {-45281.9846, -7.04827944}, {117696.2419, -1788.791477, 8.29152319, -9.22315678e-5, 4.86367688e-9, -1.891053312e-12, 6.330036589999999e-16}, {-39083.5059, -26.52669281}, 188.9244822140674), pressureTank.state_in.T, true, ThermofluidStream.Media.myMedia.Interfaces.Choices.ReferenceEnthalpy.ZeroAt0K, 0.0) ($RES_AUX_108) (58|64) [SCAL] (1) $FUN_13 = ThermofluidStream.Media.myMedia.IdealGases.Common.Functions.h_T(ThermofluidStream.Media.myMedia.IdealGases.Common.DataRecord(\"CO2\", 0.0440095, -8.941478544405185e6, 212805.6215135368, 1000.0, {49436.5054, -626.411601, 5.30172524, 0.002503813816, -2.127308728e-7, -7.68998878e-10, 2.849677801e-13}, {-45281.9846, -7.04827944}, {117696.2419, -1788.791477, 8.29152319, -9.22315678e-5, 4.86367688e-9, -1.891053312e-12, 6.330036589999999e-16}, {-39083.5059, -26.52669281}, 188.9244822140674), pressureTank.state_out.T, true, ThermofluidStream.Media.myMedia.Interfaces.Choices.ReferenceEnthalpy.ZeroAt0K, 0.0) ($RES_AUX_109) =================== Scalar Matching =================== variable to equation ********************** var 1 --> eqn 27 var 2 --> eqn 42 var 3 --> eqn 16 var 4 --> eqn 58 var 5 --> eqn 23 var 6 --> eqn 61 var 7 --> eqn 62 var 8 --> eqn 15 var 9 --> eqn 4 var 10 --> eqn 63 var 11 --> eqn 34 var 12 --> eqn 9 var 13 --> eqn 33 var 14 --> eqn 21 var 15 --> eqn 54 var 16 --> eqn 3 var 17 --> eqn 55 var 18 --> eqn -1 var 19 --> eqn 6 var 20 --> eqn 39 var 21 --> eqn 13 var 22 --> eqn 46 var 23 --> eqn 12 var 24 --> eqn 38 var 25 --> eqn 2 var 26 --> eqn 56 var 27 --> eqn 41 var 28 --> eqn 28 var 29 --> eqn 47 var 30 --> eqn 19 var 31 --> eqn 60 var 32 --> eqn 64 var 33 --> eqn 24 var 34 --> eqn 20 var 35 --> eqn 5 var 36 --> eqn 51 var 37 --> eqn 35 var 38 --> eqn 44 var 39 --> eqn 57 var 40 --> eqn 52 var 41 --> eqn -1 var 42 --> eqn 7 var 43 --> eqn 45 var 44 --> eqn 49 var 45 --> eqn 37 var 46 --> eqn 11 var 47 --> eqn 17 var 48 --> eqn 36 var 49 --> eqn 50 var 50 --> eqn 30 var 51 --> eqn 40 var 52 --> eqn 29 var 53 --> eqn 25 var 54 --> eqn 10 var 55 --> eqn 26 var 56 --> eqn 43 var 57 --> eqn 59 var 58 --> eqn 48 var 59 --> eqn 53 var 60 --> eqn 22 var 61 --> eqn 32 var 62 --> eqn 31 var 63 --> eqn 8 var 64 --> eqn 1 var 65 --> eqn 18 var 66 --> eqn 14 equation to variable ********************** eqn 1 --> var 64 eqn 2 --> var 25 eqn 3 --> var 16 eqn 4 --> var 9 eqn 5 --> var 35 eqn 6 --> var 19 eqn 7 --> var 42 eqn 8 --> var 63 eqn 9 --> var 12 eqn 10 --> var 54 eqn 11 --> var 46 eqn 12 --> var 23 eqn 13 --> var 21 eqn 14 --> var 66 eqn 15 --> var 8 eqn 16 --> var 3 eqn 17 --> var 47 eqn 18 --> var 65 eqn 19 --> var 30 eqn 20 --> var 34 eqn 21 --> var 14 eqn 22 --> var 60 eqn 23 --> var 5 eqn 24 --> var 33 eqn 25 --> var 53 eqn 26 --> var 55 eqn 27 --> var 1 eqn 28 --> var 28 eqn 29 --> var 52 eqn 30 --> var 50 eqn 31 --> var 62 eqn 32 --> var 61 eqn 33 --> var 13 eqn 34 --> var 11 eqn 35 --> var 37 eqn 36 --> var 48 eqn 37 --> var 45 eqn 38 --> var 24 eqn 39 --> var 20 eqn 40 --> var 51 eqn 41 --> var 27 eqn 42 --> var 2 eqn 43 --> var 56 eqn 44 --> var 38 eqn 45 --> var 43 eqn 46 --> var 22 eqn 47 --> var 29 eqn 48 --> var 58 eqn 49 --> var 44 eqn 50 --> var 49 eqn 51 --> var 36 eqn 52 --> var 40 eqn 53 --> var 59 eqn 54 --> var 15 eqn 55 --> var 17 eqn 56 --> var 26 eqn 57 --> var 39 eqn 58 --> var 4 eqn 59 --> var 57 eqn 60 --> var 31 eqn 61 --> var 6 eqn 62 --> var 7 eqn 63 --> var 10 eqn 64 --> var 32 " [Timeout remaining time 659] [Calling sys.exit(0), Time elapsed: 4.398635856807232] Failed to read output from testmodel.py, exit status != 0: 0.621499240398407 0.632182058 0.028650438 Calling exit ...