Running: ./testmodel.py --libraries=/home/hudson/saved_omc/libraries/.openmodelica/libraries --ompython_omhome=/usr ThermofluidStream_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 0.001518/0.001518, allocations: 92.2 kB / 20.22 MB, free: 4.176 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 0.001634/0.001634, allocations: 165.3 kB / 23.53 MB, free: 0.8633 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 1.47/1.47, allocations: 177.2 MB / 203.9 MB, free: 5.613 MB / 186.7 MB " [Timeout remaining time 178] loadFile("/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermofluidStream 1.4.0/package.mo", uses=false) [Timeout 180] "Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermofluidStream 1.4.0/package.mo): time 1.015/1.015, allocations: 118.6 MB / 379 MB, free: 1.48 MB / 346.7 MB " [Timeout remaining time 179] Using package ThermofluidStream with version 1.4.0 (/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermofluidStream 1.4.0/package.mo) Using package Modelica with version 4.1.0 (/home/hudson/saved_omc/libraries/.openmodelica/libraries/Modelica 4.1.0+maint.om/package.mo) Using package Complex with version 4.1.0 (/home/hudson/saved_omc/libraries/.openmodelica/libraries/Complex 4.1.0+maint.om/package.mo) Using package ModelicaServices with version 4.1.0 (/home/hudson/saved_omc/libraries/.openmodelica/libraries/ModelicaServices 4.1.0+maint.om/package.mo) Running command: translateModel(ThermofluidStream.Idealized.Examples.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_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_ThermofluidStream.Idealized.Examples.Volumes.Volume") [Timeout 660] "Notification: Performance of FrontEnd - Absyn->SCode: time 1.748e-05/1.748e-05, allocations: 5.125 kB / 483.7 MB, free: 8.25 MB / 410.7 MB Notification: Performance of NFInst.instantiate(ThermofluidStream.Idealized.Examples.Volumes.Volume): time 0.2036/0.2037, allocations: 152.6 MB / 0.6214 GB, free: 7.879 MB / 0.5417 GB Notification: Performance of NFInst.instExpressions: time 0.004306/0.208, allocations: 2.478 MB / 0.6238 GB, free: 5.391 MB / 0.5417 GB Notification: Performance of NFInst.updateImplicitVariability: time 0.0003197/0.2083, allocations: 35.62 kB / 0.6239 GB, free: 5.355 MB / 0.5417 GB Notification: Performance of NFTyping.typeComponents: time 0.0007188/0.209, allocations: 250.1 kB / 0.6241 GB, free: 5.109 MB / 0.5417 GB Notification: Performance of NFTyping.typeBindings: time 0.002596/0.2116, allocations: 1.056 MB / 0.6251 GB, free: 4.047 MB / 0.5417 GB Notification: Performance of NFTyping.typeClassSections: time 0.001605/0.2132, allocations: 0.6498 MB / 0.6258 GB, free: 3.395 MB / 0.5417 GB Notification: Performance of NFFlatten.flatten: time 0.001605/0.2148, allocations: 1.316 MB / 0.627 GB, free: 2.074 MB / 0.5417 GB Notification: Performance of NFFlatten.resolveConnections: time 0.0001996/0.215, allocations: 67.58 kB / 0.6271 GB, free: 2.008 MB / 0.5417 GB Notification: Performance of NFEvalConstants.evaluate: time 0.002082/0.2171, allocations: 1.001 MB / 0.6281 GB, free: 1.004 MB / 0.5417 GB Notification: Performance of NFSimplifyModel.simplify: time 0.0004358/0.2175, allocations: 259.1 kB / 0.6283 GB, free: 0.75 MB / 0.5417 GB Notification: Performance of NFPackage.collectConstants: time 8.816e-05/0.2176, allocations: 40 kB / 0.6284 GB, free: 0.7109 MB / 0.5417 GB Notification: Performance of NFFlatten.collectFunctions: time 0.001506/0.2191, allocations: 0.7642 MB / 0.6291 GB, free: 15.95 MB / 0.5573 GB Notification: Performance of combineBinaries: time 0.001186/0.2203, allocations: 1.071 MB / 0.6302 GB, free: 14.86 MB / 0.5573 GB Notification: Performance of replaceArrayConstructors: time 0.0006296/0.2209, allocations: 0.6941 MB / 0.6308 GB, free: 14.16 MB / 0.5573 GB Notification: Performance of NFVerifyModel.verify: time 9.672e-05/0.221, allocations: 63.94 kB / 0.6309 GB, free: 14.1 MB / 0.5573 GB Notification: Performance of FrontEnd: time 0.0002872/0.2213, allocations: 123.6 kB / 0.631 GB, free: 13.98 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: 98 (92) * Number of variables: 100 (100) Notification: Performance of [SIM] Bindings: time 0.003635/0.225, allocations: 2.752 MB / 0.6337 GB, free: 11.08 MB / 0.5573 GB Notification: Performance of [SIM] FunctionAlias: time 0.0009038/0.2259, allocations: 475.1 kB / 0.6342 GB, free: 10.61 MB / 0.5573 GB Notification: Performance of [SIM] Early Inline: time 0.003231/0.2291, allocations: 2.36 MB / 0.6365 GB, free: 8.254 MB / 0.5573 GB Notification: Performance of [SIM] Simplify 1: time 0.0004388/0.2295, allocations: 244 kB / 0.6367 GB, free: 7.988 MB / 0.5573 GB Notification: Performance of [SIM] Alias: time 0.003916/0.2334, allocations: 2.463 MB / 0.6391 GB, free: 5.168 MB / 0.5573 GB Notification: Performance of [SIM] Simplify 2: time 0.0003256/0.2338, allocations: 184.7 kB / 0.6393 GB, free: 4.961 MB / 0.5573 GB Notification: Performance of [SIM] Remove Stream: time 0.0002018/0.234, allocations: 136.3 kB / 0.6394 GB, free: 4.801 MB / 0.5573 GB Notification: Performance of [SIM] Detect States: time 0.0005126/0.2345, allocations: 379.6 kB / 0.6398 GB, free: 4.379 MB / 0.5573 GB Notification: Performance of [SIM] Events: time 0.0002041/0.2347, allocations: 135.9 kB / 0.6399 GB, free: 4.246 MB / 0.5573 GB Notification: Performance of [SIM] Partitioning: time 0.0007783/0.2355, allocations: 0.4993 MB / 0.6404 GB, free: 3.699 MB / 0.5573 GB Error: Internal error NBSorting.tarjan failed to sort system: System Variables (54/54) ************************** (1|1) [ALGB] (1) Real pressureTank.medium.T (start = 500.0, min = 200.0, max = 6000.0, nominal = 500.0, StateSelect = default) (2|2) [ALGB] (1) Real source.outlet.r (3|3) [ALGB] (1) protected Real pressureTank.state_in.p (start = 1e6, min = 0.0, max = 1e8, nominal = 1e6) (4|4) [ALGB] (1) protected Real pressureTank.r_in (5|5) [ALGB] (1) Real compressor.P_in_internal (6|6) [ALGB] (1) Real compressor.dp (7|7) [ALGB] (1) Real compressor.outlet.r (8|8) [DISC] (1) Boolean $SEV_0 (9|9) [ALGB] (1) protected Real pressureTank.state_in.T (start = 500.0, min = 200.0, max = 6000.0, nominal = 500.0) (10|10) [ALGB] (1) Real compressor.p_in = ThermofluidStream.Idealized.Examples.Volumes.Volume.compressor.Medium.pressure(compressor.adiabaticModel.state_in) (start = 1e6, min = 0.0, max = 1e8, nominal = 1e6) (11|11) [ALGB] (1) Real pressureTank.medium.h (12|12) [ALGB] (1) Real compressor.p_out (start = 1e6, min = 0.0, max = 1e8, nominal = 1e6) (13|13) [ALGB] (1) output Real source.outlet.state.T (start = 500.0, min = 200.0, max = 6000.0, nominal = 500.0) (14|14) [ALGB] (1) Real compressor.dh (15|15) [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) (16|16) [ALGB] (1) Real compressor.pRatio = compressor.p_out / compressor.p_in (17|17) [DER-] (1) Real $DER.pressureTank.U_med (18|18) [ALGB] (1) Real pressureTank.medium.d (start = 10.0, min = 0.0, max = 1e5, nominal = 10.0) (19|19) [ALGB] (1) Real massFlowRate.h_out (start = 212805.6215135368, min = -1e10, max = 1e10, nominal = 1e5) (20|20) [ALGB] (1) Real $FUN_17 (21|21) [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) (22|22) [ALGB] (1) Real $FUN_16 (23|23) [ALGB] (1) Real pressureTank.medium.u (min = -1e8, max = 1e8, nominal = 1e6) (24|24) [ALGB] (1) final Real compressor.adiabaticModel.w_t_is (25|25) [ALGB] (1) Real $FUN_14 (start = 212805.6215135368, min = -1e10, max = 1e10, nominal = 1e5) (26|26) [ALGB] (1) Real compressor.h_out (start = 212805.6215135368, min = -1e10, max = 1e10, nominal = 1e5) (27|27) [ALGB] (1) Real $FUN_13 (start = 212805.6215135368, min = -1e10, max = 1e10, nominal = 1e5) (28|28) [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) (29|29) [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) (30|30) [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) (31|31) [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) (32|32) [ALGB] (1) input Real massFlowRate.inlet.state.p (start = 1e6, min = 0.0, max = 1e8, nominal = 1e6) (33|33) [ALGB] (1) protected Real pressureTank.r_damping = pressureTank.d * der(pressureTank.M) (34|34) [ALGB] (1) output Real massFlowRate.outlet.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.d = pressureTank.k_volume_damping * sqrt(abs((2.0 * pressureTank.L) / (pressureTank.V_par * max(pressureTank.density_derp_h_set, 1e-10)))) (37|37) [ALGB] (1) output Real source.outlet.state.p (start = 1e6, min = 0.0, max = 1e8, nominal = 1e6) (38|38) [DER-] (1) Real $DER.pressureTank.M (39|39) [ALGB] (1) protected Real pressureTank.r (40|40) [ALGB] (1) protected Real pressureTank.r_out (41|41) [ALGB] (1) Real massFlowRate.dr_corr (42|42) [ALGB] (1) final input Real compressor.adiabaticModel.state_in.p = compressor.inlet.state.p (start = 1e6, min = 0.0, max = 1e8, nominal = 1e6) (43|43) [ALGB] (1) Real compressor.h_in = ThermofluidStream.Idealized.Examples.Volumes.Volume.compressor.Medium.specificEnthalpy(compressor.adiabaticModel.state_in) (start = 212805.6215135368, min = -1e10, max = 1e10, nominal = 1e5) (44|44) [ALGB] (1) output Real compressor.outlet.state.T (start = 500.0, min = 200.0, max = 6000.0, nominal = 500.0) (45|45) [ALGB] (1) protected Real pressureTank.state_out.p (start = 1e6, min = 0.0, max = 1e8, nominal = 1e6) (46|46) [ALGB] (1) input Real massFlowRate.inlet.state.T (start = 500.0, min = 200.0, max = 6000.0, nominal = 500.0) (47|47) [ALGB] (1) protected Real pressureTank.state_out.T (start = 500.0, min = 200.0, max = 6000.0, nominal = 500.0) (48|48) [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) (49|49) [ALGB] (1) output Real compressor.outlet.state.p (start = 1e6, min = 0.0, max = 1e8, nominal = 1e6) (50|50) [ALGB] (1) final Real compressor.adiabaticModel.w_t (51|51) [ALGB] (1) Real massFlowRate.p_out (start = 1e6, min = 0.0, max = 1e8, nominal = 1e6) (52|52) [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) (53|53) [ALGB] (1) output Real massFlowRate.outlet.state.T (start = 500.0, min = 200.0, max = 6000.0, nominal = 500.0) (54|54) [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) System Equations (52/52) ************************** (1|1) [SCAL] (1) compressor.p_out = compressor.p_in + compressor.dp; ($RES_SIM_14) (2|2) [SCAL] (1) compressor.outlet.r = source.outlet.r - 0.0 * compressor.L; ($RES_SIM_15) (3|3) [SCAL] (1) pressureTank.Q_flow = pressureTank.A * pressureTank.U * (fixedTemperature.T - pressureTank.medium.T); ($RES_SIM_31) (4|4) [SCAL] (1) $DER.pressureTank.U_med = pressureTank.h_in * massFlowRate.m_flow_fixed + pressureTank.Q_flow; ($RES_SIM_32) (5|5) [SCAL] (1) $DER.pressureTank.M = massFlowRate.m_flow_fixed; ($RES_SIM_33) (6|6) [SCAL] (1) compressor.P_in_internal = massFlowRate.m_flow_fixed * compressor.dh; ($RES_SIM_18) (7|7) [SCAL] (1) 0.0 = pressureTank.r_out - pressureTank.r_damping; ($RES_SIM_34) (8|8) [SCAL] (1) 0.0 * pressureTank.L = pressureTank.r_in - (pressureTank.r_damping + pressureTank.r); ($RES_SIM_35) (9|9) [SCAL] (1) pressureTank.medium.u = pressureTank.medium.h - 188.9244822140674 * pressureTank.medium.T; ($RES_SIM_50) (10|10) [SCAL] (1) pressureTank.state_in.p = massFlowRate.outlet.state.p; ($RES_SIM_70) (11|11) [SCAL] (1) source.L * 0.0 = source.outlet.r; ($RES_SIM_56) (12|12) [SCAL] (1) source.outlet.state.T = compressor.adiabaticModel.state_in.T; ($RES_SIM_72) (13|13) [SCAL] (1) source.outlet.state.p = compressor.adiabaticModel.state_in.p; ($RES_SIM_73) (14|14) [SCAL] (1) compressor.p_in = compressor.adiabaticModel.state_in.p; ($RES_AUX_110) (15|15) [SCAL] (1) compressor.h_in = ThermofluidStream.Media.myMedia.IdealGases.Common.Functions.h_T(ThermofluidStream.Media.myMedia.IdealGases.Common.DataRecord(\"CO2\", 0.0440095, -8.941478544405185e6, 212805.6215135368, 1000.0, {49436.5054, -626.411601, 5.30172524, 0.002503813816, -2.127308728e-7, -7.68998878e-10, 2.849677801e-13}, {-45281.9846, -7.04827944}, {117696.2419, -1788.791477, 8.29152319, -9.22315678e-5, 4.86367688e-9, -1.891053312e-12, 6.330036589999999e-16}, {-39083.5059, -26.52669281}, 188.9244822140674), compressor.adiabaticModel.state_in.T, true, ThermofluidStream.Media.myMedia.Interfaces.Choices.ReferenceEnthalpy.ZeroAt0K, 0.0); ($RES_AUX_111) (16|16) [SCAL] (1) pressureTank.d = pressureTank.k_volume_damping * $FUN_17; ($RES_BND_82) (17|17) [SCAL] (1) compressor.adiabaticModel.p_in = compressor.adiabaticModel.state_in.p; ($RES_AUX_112) (18|18) [SCAL] (1) source.outlet.state.p = source.p0_par; ($RES_SIM_123) (19|19) [SCAL] (1) pressureTank.r_damping = pressureTank.d * $DER.pressureTank.M; ($RES_BND_83) (20|20) [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); ($RES_AUX_113) (21|21) [SCAL] (1) source.outlet.state.T = source.T0_par; ($RES_SIM_124) (22|22) [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); ($RES_AUX_114) (23|23) [SCAL] (1) compressor.outlet.state.p = compressor.p_out; ($RES_SIM_125) (24|24) [SCAL] (1) pressureTank.h_in = if noEvent(massFlowRate.m_flow_fixed >= 0.0) then $FUN_14 else pressureTank.medium.h; ($RES_BND_85) (25|25) [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); ($RES_AUX_115) (26|26) [SCAL] (1) compressor.outlet.state.T = ThermofluidStream.Idealized.Examples.Volumes.Volume.compressor.Medium.T_h(compressor.h_out); ($RES_SIM_126) (27|27) [SCAL] (1) pressureTank.h_out = $FUN_13; ($RES_BND_86) (28|28) [SCAL] (1) massFlowRate.p_in = massFlowRate.inlet.state.p; ($RES_AUX_116) (29|29) [SCAL] (1) massFlowRate.outlet.state.p = massFlowRate.p_out; ($RES_SIM_127) (30|30) [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); ($RES_AUX_117) (31|31) [SCAL] (1) massFlowRate.outlet.state.T = ThermofluidStream.Idealized.Examples.Volumes.Volume.massFlowRate.Medium.T_h(massFlowRate.h_out); ($RES_SIM_128) (32|32) [SCAL] (1) compressor.dh = compressor.h_out - compressor.h_in; ($RES_SIM_20) (33|33) [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) (34|34) [SCAL] (1) compressor.adiabaticModel.w_t = compressor.h_out - compressor.adiabaticModel.h_in; ($RES_SIM_28) (35|35) [SCAL] (1) compressor.adiabaticModel.w_t_is = compressor.adiabaticModel.h_out_is - compressor.adiabaticModel.h_in; ($RES_SIM_29) (36|36) [SCAL] (1) pressureTank.state_out.p = compressor.p_out; ($RES_SIM_47) (37|37) [SCAL] (1) pressureTank.state_out.T = pressureTank.medium.T; ($RES_SIM_48) (38|38) [SCAL] (1) pressureTank.medium.d = (0.005293120236618753 * compressor.p_out) / pressureTank.medium.T; ($RES_SIM_49) (39|39) [SCAL] (1) compressor.outlet.state.T = massFlowRate.inlet.state.T; ($RES_SIM_66) (40|40) [SCAL] (1) pressureTank.r_in = (massFlowRate.dr_corr + compressor.outlet.r) - 0.0 * massFlowRate.L; ($RES_SIM_6) (41|41) [SCAL] (1) compressor.outlet.state.p = massFlowRate.inlet.state.p; ($RES_SIM_67) (42|42) [SCAL] (1) massFlowRate.p_out = max(massFlowRate.p_min, massFlowRate.p_in); ($RES_SIM_5) (43|43) [SCAL] (1) $SEV_0 = compressor.p_out >= compressor.adiabaticModel.p_in; ($RES_EVT_167) (44|44) [SCAL] (1) compressor.pRatio = compressor.p_out / compressor.p_in; ($RES_BND_90) (45|45) [SCAL] (1) massFlowRate.dr_corr = massFlowRate.p_in - massFlowRate.p_out; ($RES_SIM_4) (46|46) [SCAL] (1) pressureTank.state_in.T = massFlowRate.outlet.state.T; ($RES_SIM_69) (47|47) [SCAL] (1) pressureTank.medium.h = ThermofluidStream.Media.myMedia.IdealGases.Common.Functions.h_T(ThermofluidStream.Media.myMedia.IdealGases.Common.DataRecord(\"CO2\", 0.0440095, -8.941478544405185e6, 212805.6215135368, 1000.0, {49436.5054, -626.411601, 5.30172524, 0.002503813816, -2.127308728e-7, -7.68998878e-10, 2.849677801e-13}, {-45281.9846, -7.04827944}, {117696.2419, -1788.791477, 8.29152319, -9.22315678e-5, 4.86367688e-9, -1.891053312e-12, 6.330036589999999e-16}, {-39083.5059, -26.52669281}, 188.9244822140674), pressureTank.medium.T, true, ThermofluidStream.Media.myMedia.Interfaces.Choices.ReferenceEnthalpy.ZeroAt0K, 0.0); ($RES_AUX_120) (48|48) [SCAL] (1) $FUN_17 = sqrt($FUN_16); ($RES_AUX_105) (49|49) [SCAL] (1) $FUN_16 = abs((2.0 * pressureTank.L) / (pressureTank.V_par * max(pressureTank.density_derp_h_set, 1e-10))); ($RES_AUX_106) (50|50) [SCAL] (1) pressureTank.p_in = pressureTank.state_in.p; ($RES_AUX_107) (51|51) [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) (52|52) [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 37 var 2 --> eqn 11 var 3 --> eqn 10 var 4 --> eqn 40 var 5 --> eqn 6 var 6 --> eqn 1 var 7 --> eqn 2 var 8 --> eqn 43 var 9 --> eqn 46 var 10 --> eqn 14 var 11 --> eqn 47 var 12 --> eqn 25 var 13 --> eqn 21 var 14 --> eqn 32 var 15 --> eqn 50 var 16 --> eqn 44 var 17 --> eqn 4 var 18 --> eqn 38 var 19 --> eqn -1 var 20 --> eqn 48 var 21 --> eqn 17 var 22 --> eqn 49 var 23 --> eqn 9 var 24 --> eqn 33 var 25 --> eqn 51 var 26 --> eqn 26 var 27 --> eqn 27 var 28 --> eqn 22 var 29 --> eqn 20 var 30 --> eqn 28 var 31 --> eqn -1 var 32 --> eqn 41 var 33 --> eqn 19 var 34 --> eqn 29 var 35 --> eqn 3 var 36 --> eqn 16 var 37 --> eqn 18 var 38 --> eqn 5 var 39 --> eqn 8 var 40 --> eqn 7 var 41 --> eqn 45 var 42 --> eqn 13 var 43 --> eqn 15 var 44 --> eqn 39 var 45 --> eqn 36 var 46 --> eqn 30 var 47 --> eqn 52 var 48 --> eqn 12 var 49 --> eqn 23 var 50 --> eqn 34 var 51 --> eqn 42 var 52 --> eqn 35 var 53 --> eqn 31 var 54 --> eqn 24 equation to variable ********************** eqn 1 --> var 6 eqn 2 --> var 7 eqn 3 --> var 35 eqn 4 --> var 17 eqn 5 --> var 38 eqn 6 --> var 5 eqn 7 --> var 40 eqn 8 --> var 39 eqn 9 --> var 23 eqn 10 --> var 3 eqn 11 --> var 2 eqn 12 --> var 48 eqn 13 --> var 42 eqn 14 --> var 10 eqn 15 --> var 43 eqn 16 --> var 36 eqn 17 --> var 21 eqn 18 --> var 37 eqn 19 --> var 33 eqn 20 --> var 29 eqn 21 --> var 13 eqn 22 --> var 28 eqn 23 --> var 49 eqn 24 --> var 54 eqn 25 --> var 12 eqn 26 --> var 26 eqn 27 --> var 27 eqn 28 --> var 30 eqn 29 --> var 34 eqn 30 --> var 46 eqn 31 --> var 53 eqn 32 --> var 14 eqn 33 --> var 24 eqn 34 --> var 50 eqn 35 --> var 52 eqn 36 --> var 45 eqn 37 --> var 1 eqn 38 --> var 18 eqn 39 --> var 44 eqn 40 --> var 4 eqn 41 --> var 32 eqn 42 --> var 51 eqn 43 --> var 8 eqn 44 --> var 16 eqn 45 --> var 41 eqn 46 --> var 9 eqn 47 --> var 11 eqn 48 --> var 20 eqn 49 --> var 22 eqn 50 --> var 15 eqn 51 --> var 25 eqn 52 --> var 47 " [Timeout remaining time 660] [Calling sys.exit(0), Time elapsed: 3.7990838559926488]