Running: ./testmodel.py --libraries=/home/hudson/saved_omc/libraries/.openmodelica/libraries --ompython_omhome=/usr ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.Volumes.Reservoir.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 0.001597/0.001597, allocations: 81.3 kB / 20.05 MB, free: 1.48 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 0.002182/0.002182, allocations: 166.6 kB / 23.34 MB, free: 4.469 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 1.572/1.572, allocations: 177.1 MB / 203.7 MB, free: 9.133 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 1.057/1.057, allocations: 116 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.Reservoir,tolerance=1e-06,outputFormat="mat",numberOfIntervals=1000,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|Time|_GlobalScope.ThermofluidStream.Media.myMedia.Water.WaterIF97_ph.fluidConstants.1..HCRIT0|_GlobalScope.ThermofluidStream.Media.myMedia.Water.WaterIF97_ph.fluidConstants.1..SCRIT0|_GlobalScope.ThermofluidStream.Media.myMedia.Water.WaterIF97_ph.fluidConstants.1..acentricFactor|_GlobalScope.ThermofluidStream.Media.myMedia.Water.WaterIF97_ph.fluidConstants.1..criticalMolarVolume|_GlobalScope.ThermofluidStream.Media.myMedia.Water.WaterIF97_ph.fluidConstants.1..criticalPressure|_GlobalScope.ThermofluidStream.Media.myMedia.Water.WaterIF97_ph.fluidConstants.1..criticalTemperature|_GlobalScope.ThermofluidStream.Media.myMedia.Water.WaterIF97_ph.fluidConstants.1..deltah|_GlobalScope.ThermofluidStream.Media.myMedia.Water.WaterIF97_ph.fluidConstants.1..deltas|_GlobalScope.ThermofluidStream.Media.myMedia.Water.WaterIF97_ph.fluidConstants.1..dipoleMoment|_GlobalScope.ThermofluidStream.Media.myMedia.Water.WaterIF97_ph.fluidConstants.1..hasAccurateConductivityData|_GlobalScope.ThermofluidStream.Media.myMedia.Water.WaterIF97_ph.fluidConstants.1..hasAccurateViscosityData|_GlobalScope.ThermofluidStream.Media.myMedia.Water.WaterIF97_ph.fluidConstants.1..hasAcentricFactor|_GlobalScope.ThermofluidStream.Media.myMedia.Water.WaterIF97_ph.fluidConstants.1..hasCriticalData|_GlobalScope.ThermofluidStream.Media.myMedia.Water.WaterIF97_ph.fluidConstants.1..hasDipoleMoment|_GlobalScope.ThermofluidStream.Media.myMedia.Water.WaterIF97_ph.fluidConstants.1..hasFundamentalEquation|_GlobalScope.ThermofluidStream.Media.myMedia.Water.WaterIF97_ph.fluidConstants.1..hasIdealGasHeatCapacity|_GlobalScope.ThermofluidStream.Media.myMedia.Water.WaterIF97_ph.fluidConstants.1..hasLiquidHeatCapacity|_GlobalScope.ThermofluidStream.Media.myMedia.Water.WaterIF97_ph.fluidConstants.1..hasSolidHeatCapacity|_GlobalScope.ThermofluidStream.Media.myMedia.Water.WaterIF97_ph.fluidConstants.1..hasVapourPressureCurve|_GlobalScope.ThermofluidStream.Media.myMedia.Water.WaterIF97_ph.fluidConstants.1..meltingPoint|_GlobalScope.ThermofluidStream.Media.myMedia.Water.WaterIF97_ph.fluidConstants.1..molarMass|_GlobalScope.ThermofluidStream.Media.myMedia.Water.WaterIF97_ph.fluidConstants.1..normalBoilingPoint|_GlobalScope.ThermofluidStream.Media.myMedia.Water.WaterIF97_ph.fluidConstants.1..triplePointPressure|_GlobalScope.ThermofluidStream.Media.myMedia.Water.WaterIF97_ph.fluidConstants.1..triplePointTemperature|_GlobalScope.ThermofluidStream.Media.myMedia.Water.waterConstants.1..HCRIT0|_GlobalScope.ThermofluidStream.Media.myMedia.Water.waterConstants.1..SCRIT0|_GlobalScope.ThermofluidStream.Media.myMedia.Water.waterConstants.1..acentricFactor|_GlobalScope.ThermofluidStream.Media.myMedia.Water.waterConstants.1..criticalMolarVolume|_GlobalScope.ThermofluidStream.Media.myMedia.Water.waterConstants.1..criticalPressure|_GlobalScope.ThermofluidStream.Media.myMedia.Water.waterConstants.1..criticalTemperature|_GlobalScope.ThermofluidStream.Media.myMedia.Water.waterConstants.1..deltah|_GlobalScope.ThermofluidStream.Media.myMedia.Water.waterConstants.1..deltas|_GlobalScope.ThermofluidStream.Media.myMedia.Water.waterConstants.1..dipoleMoment|_GlobalScope.ThermofluidStream.Media.myMedia.Water.waterConstants.1..hasAccurateConductivityData|_GlobalScope.ThermofluidStream.Media.myMedia.Water.waterConstants.1..hasAccurateViscosityData|_GlobalScope.ThermofluidStream.Media.myMedia.Water.waterConstants.1..hasAcentricFactor|_GlobalScope.ThermofluidStream.Media.myMedia.Water.waterConstants.1..hasCriticalData|_GlobalScope.ThermofluidStream.Media.myMedia.Water.waterConstants.1..hasDipoleMoment|_GlobalScope.ThermofluidStream.Media.myMedia.Water.waterConstants.1..hasFundamentalEquation|_GlobalScope.ThermofluidStream.Media.myMedia.Water.waterConstants.1..hasIdealGasHeatCapacity|_GlobalScope.ThermofluidStream.Media.myMedia.Water.waterConstants.1..hasLiquidHeatCapacity|_GlobalScope.ThermofluidStream.Media.myMedia.Water.waterConstants.1..hasSolidHeatCapacity|_GlobalScope.ThermofluidStream.Media.myMedia.Water.waterConstants.1..hasVapourPressureCurve|_GlobalScope.ThermofluidStream.Media.myMedia.Water.waterConstants.1..meltingPoint|_GlobalScope.ThermofluidStream.Media.myMedia.Water.waterConstants.1..molarMass|_GlobalScope.ThermofluidStream.Media.myMedia.Water.waterConstants.1..normalBoilingPoint|_GlobalScope.ThermofluidStream.Media.myMedia.Water.waterConstants.1..triplePointPressure|_GlobalScope.ThermofluidStream.Media.myMedia.Water.waterConstants.1..triplePointTemperature|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|isenthalpic.L|isenthalpic.assertionLevel|isenthalpic.clip_p_out|isenthalpic.dp|isenthalpic.dpLoss|isenthalpic.dpLoss_fixed|isenthalpic.dpLoss_set|isenthalpic.dr_corr|isenthalpic.h_in|isenthalpic.h_out|isenthalpic.initM_flow|der.isenthalpic.inlet.m_flow.|isenthalpic.inlet.m_flow|isenthalpic.inlet.r|isenthalpic.inlet.state.T|isenthalpic.inlet.state.d|isenthalpic.inlet.state.h|isenthalpic.inlet.state.p|isenthalpic.inlet.state.phase|isenthalpic.isDPLossAligned|isenthalpic.isDPLossSetAligned|isenthalpic.m_acceleration_0|isenthalpic.m_flow|isenthalpic.m_flowStateSelect|isenthalpic.m_flow_0|isenthalpic.outlet.m_flow|isenthalpic.outlet.r|isenthalpic.outlet.state.T|isenthalpic.outlet.state.d|isenthalpic.outlet.state.h|isenthalpic.outlet.state.p|isenthalpic.outlet.state.phase|isenthalpic.outletSpec|isenthalpic.outletSpec_actual|isenthalpic.outletSpec_prescribed|isenthalpic.outletValueSpec|isenthalpic.p_in|isenthalpic.p_min|isenthalpic.p_out|isenthalpic.p_out_fixed|isenthalpic.prLoss|isenthalpic.prLoss_fixed|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.d|massFlowRate.inlet.state.h|massFlowRate.inlet.state.p|massFlowRate.inlet.state.phase|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.d|massFlowRate.outlet.state.h|massFlowRate.outlet.state.p|massFlowRate.outlet.state.phase|massFlowRate.p_in|massFlowRate.p_min|massFlowRate.p_out|reservoir.A|reservoir.A_surf|reservoir.L|reservoir.M|reservoir.Q_flow|reservoir.T_heatPort|reservoir.T_start|reservoir.U|reservoir.U_med|reservoir.V|reservoir.W_v|reservoir.d|reservoir.density_derp_h|der.reservoir.M.|der.reservoir.U_med.|der.reservoir.V.|der.reservoir.m_flow_in.|der.reservoir.m_flow_out.|reservoir.g|reservoir.h_in|reservoir.h_out|reservoir.h_start|reservoir.height|reservoir.height_0|reservoir.height_min|reservoir.inlet.m_flow|reservoir.inlet.r|reservoir.inlet.state.T|reservoir.inlet.state.d|reservoir.inlet.state.h|reservoir.inlet.state.p|reservoir.inlet.state.phase|reservoir.k_volume_damping|reservoir.m_flow_assert|reservoir.m_flow_in|reservoir.m_flow_out|reservoir.medium.MM|reservoir.medium.R_s|reservoir.medium.T|reservoir.medium.T_degC|reservoir.medium.X.1.|reservoir.medium.d|der.reservoir.medium.u.|reservoir.medium.h|reservoir.medium.p|reservoir.medium.p_bar|reservoir.medium.phase|reservoir.medium.preferredMediumStates|reservoir.medium.sat.Tsat|reservoir.medium.sat.psat|reservoir.medium.standardOrderComponents|reservoir.medium.state.T|reservoir.medium.state.d|reservoir.medium.state.h|reservoir.medium.state.p|reservoir.medium.state.phase|reservoir.medium.u|reservoir.p_env|reservoir.p_env_par|reservoir.p_in|reservoir.p_start|reservoir.r|reservoir.r_damping|reservoir.r_in|reservoir.r_out|reservoir.state_in.T|reservoir.state_in.d|reservoir.state_in.h|reservoir.state_in.p|reservoir.state_in.phase|reservoir.state_out.T|reservoir.state_out.d|der.reservoir.state_out.d.|der.reservoir.state_out.h.|der.reservoir.state_out.p.|reservoir.state_out.h|reservoir.state_out.p|reservoir.state_out.phase|reservoirPressure.y|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.d|source.outlet.state.h|source.outlet.state.p|source.outlet.state.phase|source.p0|source.p0_par",fileNamePrefix="ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.Volumes.Reservoir") translateModel(ThermofluidStream.Idealized.Examples.Volumes.Reservoir,tolerance=1e-06,outputFormat="mat",numberOfIntervals=1000,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|Time|_GlobalScope.ThermofluidStream.Media.myMedia.Water.WaterIF97_ph.fluidConstants.1..HCRIT0|_GlobalScope.ThermofluidStream.Media.myMedia.Water.WaterIF97_ph.fluidConstants.1..SCRIT0|_GlobalScope.ThermofluidStream.Media.myMedia.Water.WaterIF97_ph.fluidConstants.1..acentricFactor|_GlobalScope.ThermofluidStream.Media.myMedia.Water.WaterIF97_ph.fluidConstants.1..criticalMolarVolume|_GlobalScope.ThermofluidStream.Media.myMedia.Water.WaterIF97_ph.fluidConstants.1..criticalPressure|_GlobalScope.ThermofluidStream.Media.myMedia.Water.WaterIF97_ph.fluidConstants.1..criticalTemperature|_GlobalScope.ThermofluidStream.Media.myMedia.Water.WaterIF97_ph.fluidConstants.1..deltah|_GlobalScope.ThermofluidStream.Media.myMedia.Water.WaterIF97_ph.fluidConstants.1..deltas|_GlobalScope.ThermofluidStream.Media.myMedia.Water.WaterIF97_ph.fluidConstants.1..dipoleMoment|_GlobalScope.ThermofluidStream.Media.myMedia.Water.WaterIF97_ph.fluidConstants.1..hasAccurateConductivityData|_GlobalScope.ThermofluidStream.Media.myMedia.Water.WaterIF97_ph.fluidConstants.1..hasAccurateViscosityData|_GlobalScope.ThermofluidStream.Media.myMedia.Water.WaterIF97_ph.fluidConstants.1..hasAcentricFactor|_GlobalScope.ThermofluidStream.Media.myMedia.Water.WaterIF97_ph.fluidConstants.1..hasCriticalData|_GlobalScope.ThermofluidStream.Media.myMedia.Water.WaterIF97_ph.fluidConstants.1..hasDipoleMoment|_GlobalScope.ThermofluidStream.Media.myMedia.Water.WaterIF97_ph.fluidConstants.1..hasFundamentalEquation|_GlobalScope.ThermofluidStream.Media.myMedia.Water.WaterIF97_ph.fluidConstants.1..hasIdealGasHeatCapacity|_GlobalScope.ThermofluidStream.Media.myMedia.Water.WaterIF97_ph.fluidConstants.1..hasLiquidHeatCapacity|_GlobalScope.ThermofluidStream.Media.myMedia.Water.WaterIF97_ph.fluidConstants.1..hasSolidHeatCapacity|_GlobalScope.ThermofluidStream.Media.myMedia.Water.WaterIF97_ph.fluidConstants.1..hasVapourPressureCurve|_GlobalScope.ThermofluidStream.Media.myMedia.Water.WaterIF97_ph.fluidConstants.1..meltingPoint|_GlobalScope.ThermofluidStream.Media.myMedia.Water.WaterIF97_ph.fluidConstants.1..molarMass|_GlobalScope.ThermofluidStream.Media.myMedia.Water.WaterIF97_ph.fluidConstants.1..normalBoilingPoint|_GlobalScope.ThermofluidStream.Media.myMedia.Water.WaterIF97_ph.fluidConstants.1..triplePointPressure|_GlobalScope.ThermofluidStream.Media.myMedia.Water.WaterIF97_ph.fluidConstants.1..triplePointTemperature|_GlobalScope.ThermofluidStream.Media.myMedia.Water.waterConstants.1..HCRIT0|_GlobalScope.ThermofluidStream.Media.myMedia.Water.waterConstants.1..SCRIT0|_GlobalScope.ThermofluidStream.Media.myMedia.Water.waterConstants.1..acentricFactor|_GlobalScope.ThermofluidStream.Media.myMedia.Water.waterConstants.1..criticalMolarVolume|_GlobalScope.ThermofluidStream.Media.myMedia.Water.waterConstants.1..criticalPressure|_GlobalScope.ThermofluidStream.Media.myMedia.Water.waterConstants.1..criticalTemperature|_GlobalScope.ThermofluidStream.Media.myMedia.Water.waterConstants.1..deltah|_GlobalScope.ThermofluidStream.Media.myMedia.Water.waterConstants.1..deltas|_GlobalScope.ThermofluidStream.Media.myMedia.Water.waterConstants.1..dipoleMoment|_GlobalScope.ThermofluidStream.Media.myMedia.Water.waterConstants.1..hasAccurateConductivityData|_GlobalScope.ThermofluidStream.Media.myMedia.Water.waterConstants.1..hasAccurateViscosityData|_GlobalScope.ThermofluidStream.Media.myMedia.Water.waterConstants.1..hasAcentricFactor|_GlobalScope.ThermofluidStream.Media.myMedia.Water.waterConstants.1..hasCriticalData|_GlobalScope.ThermofluidStream.Media.myMedia.Water.waterConstants.1..hasDipoleMoment|_GlobalScope.ThermofluidStream.Media.myMedia.Water.waterConstants.1..hasFundamentalEquation|_GlobalScope.ThermofluidStream.Media.myMedia.Water.waterConstants.1..hasIdealGasHeatCapacity|_GlobalScope.ThermofluidStream.Media.myMedia.Water.waterConstants.1..hasLiquidHeatCapacity|_GlobalScope.ThermofluidStream.Media.myMedia.Water.waterConstants.1..hasSolidHeatCapacity|_GlobalScope.ThermofluidStream.Media.myMedia.Water.waterConstants.1..hasVapourPressureCurve|_GlobalScope.ThermofluidStream.Media.myMedia.Water.waterConstants.1..meltingPoint|_GlobalScope.ThermofluidStream.Media.myMedia.Water.waterConstants.1..molarMass|_GlobalScope.ThermofluidStream.Media.myMedia.Water.waterConstants.1..normalBoilingPoint|_GlobalScope.ThermofluidStream.Media.myMedia.Water.waterConstants.1..triplePointPressure|_GlobalScope.ThermofluidStream.Media.myMedia.Water.waterConstants.1..triplePointTemperature|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|isenthalpic.L|isenthalpic.assertionLevel|isenthalpic.clip_p_out|isenthalpic.dp|isenthalpic.dpLoss|isenthalpic.dpLoss_fixed|isenthalpic.dpLoss_set|isenthalpic.dr_corr|isenthalpic.h_in|isenthalpic.h_out|isenthalpic.initM_flow|der.isenthalpic.inlet.m_flow.|isenthalpic.inlet.m_flow|isenthalpic.inlet.r|isenthalpic.inlet.state.T|isenthalpic.inlet.state.d|isenthalpic.inlet.state.h|isenthalpic.inlet.state.p|isenthalpic.inlet.state.phase|isenthalpic.isDPLossAligned|isenthalpic.isDPLossSetAligned|isenthalpic.m_acceleration_0|isenthalpic.m_flow|isenthalpic.m_flowStateSelect|isenthalpic.m_flow_0|isenthalpic.outlet.m_flow|isenthalpic.outlet.r|isenthalpic.outlet.state.T|isenthalpic.outlet.state.d|isenthalpic.outlet.state.h|isenthalpic.outlet.state.p|isenthalpic.outlet.state.phase|isenthalpic.outletSpec|isenthalpic.outletSpec_actual|isenthalpic.outletSpec_prescribed|isenthalpic.outletValueSpec|isenthalpic.p_in|isenthalpic.p_min|isenthalpic.p_out|isenthalpic.p_out_fixed|isenthalpic.prLoss|isenthalpic.prLoss_fixed|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.d|massFlowRate.inlet.state.h|massFlowRate.inlet.state.p|massFlowRate.inlet.state.phase|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.d|massFlowRate.outlet.state.h|massFlowRate.outlet.state.p|massFlowRate.outlet.state.phase|massFlowRate.p_in|massFlowRate.p_min|massFlowRate.p_out|reservoir.A|reservoir.A_surf|reservoir.L|reservoir.M|reservoir.Q_flow|reservoir.T_heatPort|reservoir.T_start|reservoir.U|reservoir.U_med|reservoir.V|reservoir.W_v|reservoir.d|reservoir.density_derp_h|der.reservoir.M.|der.reservoir.U_med.|der.reservoir.V.|der.reservoir.m_flow_in.|der.reservoir.m_flow_out.|reservoir.g|reservoir.h_in|reservoir.h_out|reservoir.h_start|reservoir.height|reservoir.height_0|reservoir.height_min|reservoir.inlet.m_flow|reservoir.inlet.r|reservoir.inlet.state.T|reservoir.inlet.state.d|reservoir.inlet.state.h|reservoir.inlet.state.p|reservoir.inlet.state.phase|reservoir.k_volume_damping|reservoir.m_flow_assert|reservoir.m_flow_in|reservoir.m_flow_out|reservoir.medium.MM|reservoir.medium.R_s|reservoir.medium.T|reservoir.medium.T_degC|reservoir.medium.X.1.|reservoir.medium.d|der.reservoir.medium.u.|reservoir.medium.h|reservoir.medium.p|reservoir.medium.p_bar|reservoir.medium.phase|reservoir.medium.preferredMediumStates|reservoir.medium.sat.Tsat|reservoir.medium.sat.psat|reservoir.medium.standardOrderComponents|reservoir.medium.state.T|reservoir.medium.state.d|reservoir.medium.state.h|reservoir.medium.state.p|reservoir.medium.state.phase|reservoir.medium.u|reservoir.p_env|reservoir.p_env_par|reservoir.p_in|reservoir.p_start|reservoir.r|reservoir.r_damping|reservoir.r_in|reservoir.r_out|reservoir.state_in.T|reservoir.state_in.d|reservoir.state_in.h|reservoir.state_in.p|reservoir.state_in.phase|reservoir.state_out.T|reservoir.state_out.d|der.reservoir.state_out.d.|der.reservoir.state_out.h.|der.reservoir.state_out.p.|reservoir.state_out.h|reservoir.state_out.p|reservoir.state_out.phase|reservoirPressure.y|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.d|source.outlet.state.h|source.outlet.state.p|source.outlet.state.phase|source.p0|source.p0_par",fileNamePrefix="ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.Volumes.Reservoir") [Timeout 660] "Notification: Performance of FrontEnd - Absyn->SCode: time 2.427e-05/2.427e-05, allocations: 2.281 kB / 0.5547 GB, free: 13.53 MB / 478.1 MB Notification: Performance of NFInst.instantiate(ThermofluidStream.Idealized.Examples.Volumes.Reservoir): time 0.04595/0.04598, allocations: 35.24 MB / 0.5892 GB, free: 10.16 MB / 0.4981 GB Notification: Performance of NFInst.instExpressions: time 0.01889/0.06487, allocations: 12.32 MB / 0.6012 GB, free: 13.8 MB / 0.5137 GB Notification: Performance of NFInst.updateImplicitVariability: time 0.0007213/0.06559, allocations: 31.69 kB / 0.6012 GB, free: 13.77 MB / 0.5137 GB Notification: Performance of NFTyping.typeComponents: time 0.001197/0.06679, allocations: 321.7 kB / 0.6015 GB, free: 13.45 MB / 0.5137 GB Notification: Performance of NFTyping.typeBindings: time 0.002141/0.06893, allocations: 0.6361 MB / 0.6021 GB, free: 12.81 MB / 0.5137 GB Notification: Performance of NFTyping.typeClassSections: time 0.01669/0.08562, allocations: 5.451 MB / 0.6075 GB, free: 7.34 MB / 0.5137 GB Notification: Performance of NFFlatten.flatten: time 0.001996/0.08762, allocations: 1.296 MB / 0.6087 GB, free: 6.035 MB / 0.5137 GB Notification: Performance of NFFlatten.resolveConnections: time 0.000292/0.08791, allocations: 77.58 kB / 0.6088 GB, free: 5.957 MB / 0.5137 GB Notification: Performance of NFEvalConstants.evaluate: time 0.01093/0.09884, allocations: 4.051 MB / 0.6128 GB, free: 1.852 MB / 0.5137 GB Notification: Performance of NFSimplifyModel.simplify: time 0.0005351/0.09938, allocations: 271.1 kB / 0.613 GB, free: 1.586 MB / 0.5137 GB Notification: Performance of NFPackage.collectConstants: time 9.803e-05/0.09947, allocations: 44 kB / 0.6131 GB, free: 1.543 MB / 0.5137 GB Notification: Performance of NFFlatten.collectFunctions: time 0.0136/0.1131, allocations: 6.45 MB / 0.6194 GB, free: 11.09 MB / 0.5294 GB Notification: Performance of combineBinaries: time 0.001479/0.1146, allocations: 1.079 MB / 0.6204 GB, free: 9.996 MB / 0.5294 GB Notification: Performance of replaceArrayConstructors: time 0.0005908/0.1151, allocations: 0.6942 MB / 0.6211 GB, free: 9.293 MB / 0.5294 GB Notification: Performance of NFVerifyModel.verify: time 0.0001654/0.1153, allocations: 67.94 kB / 0.6212 GB, free: 9.227 MB / 0.5294 GB Notification: Performance of FrontEnd: time 0.0003656/0.1157, allocations: 67.8 kB / 0.6212 GB, free: 9.16 MB / 0.5294 GB Notification: Model statistics after passing the front-end and creating the data structures used by the back-end: * Number of equations: 115 (95) * Number of variables: 117 (117) Notification: Performance of [SIM] Bindings: time 0.004045/0.1197, allocations: 3.134 MB / 0.6243 GB, free: 5.875 MB / 0.5294 GB Notification: Performance of [SIM] FunctionAlias: time 0.0007708/0.1205, allocations: 0.5063 MB / 0.6248 GB, free: 5.352 MB / 0.5294 GB Notification: Performance of [SIM] Early Inline: time 0.002744/0.1232, allocations: 2.04 MB / 0.6268 GB, free: 3.297 MB / 0.5294 GB Notification: Performance of [SIM] Simplify 1: time 0.0003553/0.1236, allocations: 204.1 kB / 0.627 GB, free: 3.066 MB / 0.5294 GB Notification: Performance of [SIM] Alias: time 0.003237/0.1268, allocations: 2.024 MB / 0.6289 GB, free: 0.8047 MB / 0.5294 GB Notification: Performance of [SIM] Simplify 2: time 0.0002692/0.1271, allocations: 176.7 kB / 0.6291 GB, free: 0.6055 MB / 0.5294 GB Notification: Performance of [SIM] Remove Stream: time 0.000228/0.1273, allocations: 172.1 kB / 0.6293 GB, free: 420 kB / 0.5294 GB Notification: Performance of [SIM] Detect States: time 0.0007282/0.1281, allocations: 0.5002 MB / 0.6298 GB, free: 15.84 MB / 0.545 GB Notification: Performance of [SIM] Events: time 0.0001132/0.1282, allocations: 56.27 kB / 0.6298 GB, free: 15.79 MB / 0.545 GB Notification: Performance of [SIM] Partitioning: time 0.001027/0.1292, allocations: 0.6753 MB / 0.6305 GB, free: 15.07 MB / 0.545 GB Error: Internal error NBSorting.tarjan failed to sort system: System Variables (107/107) **************************** (1|1) [DER-] (1) Real $DER.reservoir.M (2|2) [DER-] (1) Real $DER.reservoir.U_med (3|3) [ALGB] (1) Real reservoir.medium.state.d (start = 150.0, min = 0.0, max = 1e5, nominal = 500.0) (4|4) [ALGB] (1) output Real source.outlet.state.p (start = 5e6, min = 611.657, max = 1e8, nominal = 1e6) (5|5) [ALGB] (1) output Real isenthalpic.outlet.state.d (start = 150.0, min = 0.0, max = 1e5, nominal = 500.0) (6|6) [ALGB] (1) Real reservoir.height (min = 0.0) (7|7) [ALGB] (1) Real $FUN_19 (8|8) [ALGB] (1) Real $FUN_18 (9|9) [ALGB] (1) protected Real reservoir.state_out.h (start = 1e5, min = -1e10, max = 1e10, nominal = 5e5) (10|10) [ALGB] (1) Real $FUN_16 (11|11) [ALGB] (1) Real $FUN_15 (12|12) [ALGB] (1) Real reservoir.medium.state.T (start = 500.0, min = 273.15, max = 2273.15, nominal = 500.0) (13|13) [ALGB] (1) input Real isenthalpic.inlet.state.h (start = 1e5, min = -1e10, max = 1e10, nominal = 5e5) (14|14) [ALGB] (1) input Real isenthalpic.inlet.state.T (start = 500.0, min = 273.15, max = 2273.15, nominal = 500.0) (15|15) [ALGB] (1) Real massFlowRate.dr_corr (16|16) [ALGB] (1) output Real source.outlet.state.d (start = 150.0, min = 0.0, max = 1e5, nominal = 500.0) (17|17) [ALGB] (1) protected Real reservoir.density_derp_h (18|18) [ALGB] (1) output Real massFlowRate.outlet.state.d (start = 150.0, min = 0.0, max = 1e5, nominal = 500.0) (19|19) [ALGB] (1) protected Real reservoir.state_out.d (start = 150.0, min = 0.0, max = 1e5, nominal = 500.0) (20|20) [ALGB] (1) Real reservoir.medium.state.p (start = 5e6, min = 611.657, max = 1e8, nominal = 1e6) (21|21) [DISC] (1) input Integer massFlowRate.inlet.state.phase (min = 0, max = 2) (22|22) [ALGB] (1) protected Real reservoir.state_out.p (start = 5e6, min = 611.657, max = 1e8, nominal = 1e6) (23|23) [ALGB] (1) input Real isenthalpic.inlet.state.p (start = 5e6, min = 611.657, max = 1e8, nominal = 1e6) (24|24) [DISC] (1) output Integer massFlowRate.outlet.state.phase (min = 0, max = 2) (25|25) [ALGB] (1) protected Real reservoir.p_in = ThermofluidStream.Idealized.Examples.Volumes.Reservoir.reservoir.Medium.pressure(reservoir.state_in) (start = 5e6, min = 611.657, max = 1e8, nominal = 1e6) (26|26) [ALGB] (1) Real reservoir.medium.sat.Tsat (start = 500.0, min = 273.15, max = 2273.15, nominal = 500.0) (27|27) [DISC] (1) protected Integer reservoir.state_out.phase (min = 0, max = 2) (28|28) [ALGB] (1) input Real massFlowRate.inlet.state.h (start = 1e5, min = -1e10, max = 1e10, nominal = 5e5) (29|29) [ALGB] (1) Real $FUN_8.d (30|30) [DISC] (1) protected Integer reservoir.state_in.phase (min = 0, max = 2) (31|31) [ALGB] (1) protected Real reservoir.r_damping = reservoir.d * der(reservoir.M) (32|32) [ALGB] (1) Real isenthalpic.isDPLossSetAligned = CAST(Real, sign(massFlowRate.m_flow_fixed * isenthalpic.dpLoss_set)) (33|33) [ALGB] (1) Real $FUN_7.d (34|34) [ALGB] (1) Real $FUN_8.T (35|35) [ALGB] (1) Real $FUN_7.T (36|36) [ALGB] (1) Real reservoir.medium.state.h (start = 1e5, min = -1e10, max = 1e10, nominal = 5e5) (37|37) [ALGB] (1) Real $FUN_1.d (38|38) [ALGB] (1) Real reservoir.medium.sat.psat (start = 5e6, min = 611.657, max = 1e8, nominal = 1e6) (39|39) [ALGB] (1) Real $FUN_1.T (40|40) [ALGB] (1) input Real reservoir.inlet.state.p = reservoir.state_in.p (start = 5e6, min = 611.657, max = 1e8, nominal = 1e6) (41|41) [ALGB] (1) Real $FUN_6 (42|42) [ALGB] (1) Real $FUN_3 (43|43) [ALGB] (1) protected Real reservoir.state_in.T (start = 500.0, min = 273.15, max = 2273.15, nominal = 500.0) (44|44) [ALGB] (1) Real $FUN_2 (45|45) [DISC] (1) Integer $FUN_1.phase (46|46) [ALGB] (1) protected Real reservoir.state_out.T (start = 500.0, min = 273.15, max = 2273.15, nominal = 500.0) (47|47) [ALGB] (1) Real isenthalpic.p_out (start = 5e6, min = 611.657, max = 1e8, nominal = 1e6) (48|48) [ALGB] (1) Real isenthalpic.outlet.r (49|49) [ALGB] (1) input Real massFlowRate.inlet.state.d (start = 150.0, min = 0.0, max = 1e5, nominal = 500.0) (50|50) [DISC] (1) Integer $FUN_7.phase (51|51) [DISC] (1) input Integer isenthalpic.inlet.state.phase (min = 0, max = 2) (52|52) [DISC] (1) output Integer isenthalpic.outlet.state.phase (min = 0, max = 2) (53|53) [DISC] (1) Integer $FUN_8.phase (54|54) [ALGB] (1) protected Real reservoir.state_in.d (start = 150.0, min = 0.0, max = 1e5, nominal = 500.0) (55|55) [ALGB] (1) output Real massFlowRate.outlet.state.T (start = 500.0, min = 273.15, max = 2273.15, nominal = 500.0) (56|56) [ALGB] (1) protected Real reservoir.state_in.h (start = 1e5, min = -1e10, max = 1e10, nominal = 5e5) (57|57) [ALGB] (1) Real reservoir.Q_flow (58|58) [ALGB] (1) protected Real reservoir.T_heatPort (start = 500.0, min = 273.15, max = 2273.15, nominal = 500.0) (59|59) [ALGB] (1) protected Real reservoir.h_out = if noEvent((-0.0) >= 0.0) then ThermofluidStream.Idealized.Examples.Volumes.Reservoir.reservoir.Medium.specificEnthalpy(reservoir.state_out) else reservoir.medium.h (start = 1e5, min = -1e10, max = 1e10, nominal = 5e5) (60|60) [ALGB] (1) protected Real reservoir.state_in.p (start = 5e6, min = 611.657, max = 1e8, nominal = 1e6) (61|61) [ALGB] (1) protected Real reservoir.d = reservoir.k_volume_damping * sqrt(abs((2.0 * reservoir.L) / (reservoir.V * max(reservoir.density_derp_h, 1e-10)))) (62|62) [ALGB] (1) input Real reservoir.inlet.state.h = reservoir.state_in.h (start = 1e5, min = -1e10, max = 1e10, nominal = 5e5) (63|63) [ALGB] (1) Real massFlowRate.p_in = ThermofluidStream.Idealized.Examples.Volumes.Reservoir.massFlowRate.Medium.pressure(massFlowRate.inlet.state) (start = 5e6, min = 611.657, max = 1e8, nominal = 1e6) (64|64) [ALGB] (1) input Real massFlowRate.inlet.state.p (start = 5e6, min = 611.657, max = 1e8, nominal = 1e6) (65|65) [ALGB] (1) Real massFlowRate.h_out (start = 1e5, min = -1e10, max = 1e10, nominal = 5e5) (66|66) [ALGB] (1) Real isenthalpic.dp (67|67) [ALGB] (1) Real reservoir.W_v (68|68) [DISC] (1) output Integer source.outlet.state.phase (min = 0, max = 2) (69|69) [ALGB] (1) protected Real reservoir.r (70|70) [ALGB] (1) Real reservoir.medium.h (StateSelect = default) (71|71) [ALGB] (1) output Real isenthalpic.outlet.state.h (start = 1e5, min = -1e10, max = 1e10, nominal = 5e5) (72|72) [ALGB] (1) Real isenthalpic.h_out (start = 1e5, min = -1e10, max = 1e10, nominal = 5e5) (73|73) [ALGB] (1) Real isenthalpic.prLoss = isenthalpic.dpLoss / isenthalpic.p_in (74|74) [ALGB] (1) protected Real reservoir.r_out (75|75) [ALGB] (1) Real reservoir.medium.u (min = -1e8, max = 1e8, nominal = 1e6) (76|76) [ALGB] (1) input Real massFlowRate.inlet.state.T (start = 500.0, min = 273.15, max = 2273.15, nominal = 500.0) (77|77) [ALGB] (1) Real $FUN_8.p (78|78) [ALGB] (1) Real $FUN_7.p (79|79) [ALGB] (1) Real $FUN_8.h (80|80) [DER-] (1) Real $DER.reservoir.V (81|81) [ALGB] (1) Real reservoir.medium.d (start = 150.0, min = 0.0, max = 1e5, nominal = 500.0, StateSelect = default) (82|82) [ALGB] (1) output Real source.outlet.state.T (start = 500.0, min = 273.15, max = 2273.15, nominal = 500.0) (83|83) [ALGB] (1) Real $FUN_7.h (84|84) [ALGB] (1) protected Real reservoir.r_in (85|85) [ALGB] (1) Real $FUN_1.p (86|86) [ALGB] (1) Real $FUN_1.h (87|87) [DISC] (1) Boolean $SEV_0 (88|88) [ALGB] (1) Real isenthalpic.p_out_set (min = 0.0) (89|89) [ALGB] (1) output Real isenthalpic.outlet.state.T (start = 500.0, min = 273.15, max = 2273.15, nominal = 500.0) (90|90) [DISC] (1) Integer reservoir.medium.state.phase (min = 0, max = 2) (91|91) [ALGB] (1) Real isenthalpic.p_in = ThermofluidStream.Idealized.Examples.Volumes.Reservoir.isenthalpic.Medium.pressure(isenthalpic.inlet.state) (start = 5e6, min = 611.657, max = 1e8, nominal = 1e6) (92|92) [ALGB] (1) output Real massFlowRate.outlet.state.p (start = 5e6, min = 611.657, max = 1e8, nominal = 1e6) (93|93) [ALGB] (1) Real massFlowRate.p_out (start = 5e6, min = 611.657, max = 1e8, nominal = 1e6) (94|94) [ALGB] (1) input Real reservoir.inlet.state.d = reservoir.state_in.d (start = 150.0, min = 0.0, max = 1e5, nominal = 500.0) (95|95) [ALGB] (1) protected Real reservoir.h_in = if noEvent(massFlowRate.m_flow_fixed >= 0.0) then ThermofluidStream.Idealized.Examples.Volumes.Reservoir.reservoir.Medium.specificEnthalpy(reservoir.state_in) else reservoir.medium.h (start = 1e5, min = -1e10, max = 1e10, nominal = 5e5) (96|96) [ALGB] (1) output Real source.outlet.state.h (start = 1e5, min = -1e10, max = 1e10, nominal = 5e5) (97|97) [ALGB] (1) output Real isenthalpic.outlet.state.p (start = 5e6, min = 611.657, max = 1e8, nominal = 1e6) (98|98) [ALGB] (1) Real isenthalpic.dpLoss_set (99|99) [ALGB] (1) input Real isenthalpic.inlet.state.d (start = 150.0, min = 0.0, max = 1e5, nominal = 500.0) (100|100) [ALGB] (1) output Real massFlowRate.outlet.state.h (start = 1e5, min = -1e10, max = 1e10, nominal = 5e5) (101|101) [ALGB] (1) Real isenthalpic.dpLoss = isenthalpic.p_in - isenthalpic.p_out (102|102) [DISC] (1) input Integer reservoir.inlet.state.phase = reservoir.state_in.phase (min = 0, max = 2) (103|103) [ALGB] (1) Real isenthalpic.isDPLossAligned = CAST(Real, sign(massFlowRate.m_flow_fixed * isenthalpic.dpLoss)) (104|104) [DISC] (1) Integer reservoir.medium.phase (fixed = false, start = 1, min = 0, max = 2) (105|105) [ALGB] (1) Real source.outlet.r (106|106) [ALGB] (1) input Real reservoir.inlet.state.T = reservoir.state_in.T (start = 500.0, min = 273.15, max = 2273.15, nominal = 500.0) (107|107) [ALGB] (1) Real isenthalpic.prLoss_set System Equations (85/105) *************************** (1|1) [SCAL] (1) reservoir.medium.sat.psat = isenthalpic.p_out_set ($RES_SIM_50) (2|2) [SCAL] (1) $FUN_7.phase = 0 ($RES_SIM_132) (3|3) [SCAL] (1) reservoir.medium.sat.Tsat = $FUN_6 ($RES_SIM_51) (4|4) [SCAL] (1) $FUN_7.h = isenthalpic.h_out ($RES_SIM_133) (5|5) [SCAL] (1) reservoir.d = reservoir.k_volume_damping * $FUN_19 ($RES_BND_88) (6|6) [SCAL] (1) isenthalpic.dpLoss = if noEvent(massFlowRate.m_flow_fixed * isenthalpic.dpLoss_set >= 0.0) then isenthalpic.dpLoss_set else 0.0 ($RES_SIM_17) (7|7) [SCAL] (1) $FUN_7.d = ThermofluidStream.Media.myMedia.Water.IF97_Utilities.rho_props_ph(isenthalpic.p_out, isenthalpic.h_out, ThermofluidStream.Media.myMedia.Water.IF97_Utilities.waterBaseProp_ph(isenthalpic.p_out, isenthalpic.h_out, 0, 0)) ($RES_SIM_134) (8|8) [SCAL] (1) reservoir.r_damping = reservoir.d * $DER.reservoir.M ($RES_BND_89) (9|9) [SCAL] (1) isenthalpic.p_out_set = isenthalpic.p_in - isenthalpic.dpLoss_set ($RES_SIM_18) (10|10) [SCAL] (1) $FUN_7.T = ThermofluidStream.Media.myMedia.Water.IF97_Utilities.T_props_ph(isenthalpic.p_out, isenthalpic.h_out, ThermofluidStream.Media.myMedia.Water.IF97_Utilities.waterBaseProp_ph(isenthalpic.p_out, isenthalpic.h_out, 0, 0)) ($RES_SIM_135) (11|11) [SCAL] (1) reservoir.medium.phase = if $SEV_0 then 1 else 2 ($RES_SIM_54) (12|12) [SCAL] (1) isenthalpic.prLoss_set = isenthalpic.dpLoss_set / isenthalpic.p_in ($RES_SIM_19) (13|13) [SCAL] (1) $FUN_7.p = isenthalpic.p_out ($RES_SIM_136) (14|14) [SCAL] (1) $FUN_8.phase = 0 ($RES_SIM_137) (15|15) [RECD] (5) source.outlet.state = $FUN_1 ($RES_SIM_56) (16|20) [SCAL] (1) $FUN_8.h = massFlowRate.h_out ($RES_SIM_138) (17|21) [SCAL] (1) source.L * 0.0 = source.outlet.r ($RES_SIM_57) (18|22) [SCAL] (1) $FUN_8.d = ThermofluidStream.Media.myMedia.Water.IF97_Utilities.rho_props_ph(massFlowRate.p_out, massFlowRate.h_out, ThermofluidStream.Media.myMedia.Water.IF97_Utilities.waterBaseProp_ph(massFlowRate.p_out, massFlowRate.h_out, 0, 0)) ($RES_SIM_139) (19|23) [SCAL] (1) $FUN_16 = reservoir.state_in.h ($RES_AUX_110) (20|24) [SCAL] (1) $FUN_15 = reservoir.state_out.h ($RES_AUX_111) (21|25) [SCAL] (1) isenthalpic.p_in = isenthalpic.inlet.state.p ($RES_AUX_112) (22|26) [SCAL] (1) isenthalpic.h_out = isenthalpic.inlet.state.h ($RES_AUX_113) (23|27) [SCAL] (1) isenthalpic.isDPLossSetAligned = sign(massFlowRate.m_flow_fixed * isenthalpic.dpLoss_set) ($RES_AUX_114) (24|28) [SCAL] (1) isenthalpic.isDPLossAligned = sign(massFlowRate.m_flow_fixed * isenthalpic.dpLoss) ($RES_AUX_115) (25|29) [SCAL] (1) reservoir.h_in = if noEvent(massFlowRate.m_flow_fixed >= 0.0) then $FUN_16 else reservoir.medium.h ($RES_BND_91) (26|30) [SCAL] (1) massFlowRate.p_in = massFlowRate.inlet.state.p ($RES_AUX_116) (27|31) [SCAL] (1) reservoir.h_out = $FUN_15 ($RES_BND_92) (28|32) [SCAL] (1) massFlowRate.h_out = massFlowRate.inlet.state.h ($RES_AUX_117) (29|33) [SCAL] (1) $FUN_8.T = ThermofluidStream.Media.myMedia.Water.IF97_Utilities.T_props_ph(massFlowRate.p_out, massFlowRate.h_out, ThermofluidStream.Media.myMedia.Water.IF97_Utilities.waterBaseProp_ph(massFlowRate.p_out, massFlowRate.h_out, 0, 0)) ($RES_SIM_140) (30|34) [SCAL] (1) $FUN_8.p = massFlowRate.p_out ($RES_SIM_141) (31|35) [SCAL] (1) reservoir.Q_flow = 0.0 ($RES_SIM_25) (32|36) [SCAL] (1) $DER.reservoir.U_med = reservoir.h_in * massFlowRate.m_flow_fixed + reservoir.Q_flow + reservoir.W_v ($RES_SIM_26) (33|37) [SCAL] (1) isenthalpic.dpLoss = isenthalpic.p_in - isenthalpic.p_out ($RES_BND_98) (34|38) [SCAL] (1) $DER.reservoir.M = massFlowRate.m_flow_fixed ($RES_SIM_27) (35|39) [SCAL] (1) 0.0 = reservoir.r_out - reservoir.r_damping ($RES_SIM_28) (36|40) [SCAL] (1) isenthalpic.prLoss = isenthalpic.dpLoss / isenthalpic.p_in ($RES_BND_99) (37|41) [SCAL] (1) 0.0 * reservoir.L = reservoir.r_in - (reservoir.r_damping + reservoir.r) ($RES_SIM_29) (38|42) [SCAL] (1) isenthalpic.outlet.state.p = massFlowRate.inlet.state.p ($RES_SIM_65) (39|43) [SCAL] (1) isenthalpic.outlet.state.T = massFlowRate.inlet.state.T ($RES_SIM_66) (40|44) [SCAL] (1) isenthalpic.outlet.state.d = massFlowRate.inlet.state.d ($RES_SIM_67) (41|45) [SCAL] (1) isenthalpic.outlet.state.h = massFlowRate.inlet.state.h ($RES_SIM_68) (42|46) [SCAL] (1) isenthalpic.outlet.state.phase = massFlowRate.inlet.state.phase ($RES_SIM_69) (43|47) [SCAL] (1) $SEV_0 = (reservoir.medium.h < $FUN_2 or reservoir.medium.h > $FUN_3) or isenthalpic.p_out_set > 2.2064e7 ($RES_EVT_146) (44|48) [SCAL] (1) $FUN_6 = ThermofluidStream.Media.myMedia.Water.IF97_Utilities.BaseIF97.Basic.tsat(isenthalpic.p_out_set) ($RES_AUX_120) (45|49) [SCAL] (1) reservoir.T_heatPort = ThermofluidStream.Media.myMedia.Water.IF97_Utilities.T_props_ph(isenthalpic.p_out_set, reservoir.medium.h, ThermofluidStream.Media.myMedia.Water.IF97_Utilities.waterBaseProp_ph(isenthalpic.p_out_set, reservoir.medium.h, reservoir.medium.phase, 0)) ($RES_AUX_121) (46|50) [SCAL] (1) reservoir.medium.d = ThermofluidStream.Media.myMedia.Water.IF97_Utilities.rho_props_ph(isenthalpic.p_out_set, reservoir.medium.h, ThermofluidStream.Media.myMedia.Water.IF97_Utilities.waterBaseProp_ph(isenthalpic.p_out_set, reservoir.medium.h, reservoir.medium.phase, 0)) ($RES_AUX_122) (47|51) [SCAL] (1) $FUN_3 = ThermofluidStream.Media.myMedia.Water.IF97_Utilities.BaseIF97.Regions.hvl_p(reservoir.medium.sat.psat, ThermofluidStream.Media.myMedia.Water.IF97_Utilities.BaseIF97.Regions.dewcurve_p(reservoir.medium.sat.psat)) ($RES_AUX_123) (48|52) [SCAL] (1) $FUN_2 = ThermofluidStream.Media.myMedia.Water.IF97_Utilities.BaseIF97.Regions.hvl_p(reservoir.medium.sat.psat, ThermofluidStream.Media.myMedia.Water.IF97_Utilities.BaseIF97.Regions.boilingcurve_p(reservoir.medium.sat.psat)) ($RES_AUX_124) (49|53) [RECD] (5) reservoir.state_out = reservoir.medium.state ($RES_SIM_33) (50|58) [SCAL] (1) reservoir.W_v = -$DER.reservoir.V * reservoir.p_env_par ($RES_SIM_35) (51|59) [SCAL] (1) reservoir.inlet.state.p = massFlowRate.outlet.state.p ($RES_SIM_71) (52|60) [SCAL] (1) isenthalpic.p_out_set = reservoir.p_env_par + (reservoir.M / reservoir.A_surf) * reservoir.g ($RES_SIM_36) (53|61) [SCAL] (1) reservoir.inlet.state.T = massFlowRate.outlet.state.T ($RES_SIM_72) (54|62) [SCAL] (1) reservoir.V = reservoir.A_surf * reservoir.height ($RES_SIM_37) (55|63) [SCAL] (1) reservoir.inlet.state.d = massFlowRate.outlet.state.d ($RES_SIM_73) (56|64) [SCAL] (1) reservoir.density_derp_h = 1/(reservoir.g * reservoir.height) ($RES_SIM_38) (57|65) [SCAL] (1) reservoir.inlet.state.h = massFlowRate.outlet.state.h ($RES_SIM_74) (58|66) [SCAL] (1) reservoir.inlet.state.phase = massFlowRate.outlet.state.phase ($RES_SIM_75) (59|67) [SCAL] (1) source.outlet.state.p = isenthalpic.inlet.state.p ($RES_SIM_77) (60|68) [SCAL] (1) source.outlet.state.T = isenthalpic.inlet.state.T ($RES_SIM_78) (61|69) [SCAL] (1) source.outlet.state.d = isenthalpic.inlet.state.d ($RES_SIM_79) (62|70) [SCAL] (1) reservoir.medium.phase = reservoir.medium.state.phase ($RES_SIM_43) (63|71) [SCAL] (1) reservoir.medium.d = reservoir.medium.state.d ($RES_SIM_44) (64|72) [SCAL] (1) source.outlet.state.h = isenthalpic.inlet.state.h ($RES_SIM_80) (65|73) [SCAL] (1) reservoir.T_heatPort = reservoir.medium.state.T ($RES_SIM_45) (66|74) [SCAL] (1) $FUN_1.phase = 1 ($RES_SIM_127) (67|75) [SCAL] (1) source.outlet.state.phase = isenthalpic.inlet.state.phase ($RES_SIM_81) (68|76) [SCAL] (1) isenthalpic.p_out_set = reservoir.medium.state.p ($RES_SIM_46) (69|77) [SCAL] (1) $FUN_1.h = ThermofluidStream.Media.myMedia.Water.IF97_Utilities.h_props_pT(source.p0_par, source.T0_par, ThermofluidStream.Media.myMedia.Water.IF97_Utilities.waterBaseProp_pT(source.p0_par, source.T0_par, 0)) ($RES_SIM_128) (70|78) [SCAL] (1) reservoir.medium.h = reservoir.medium.state.h ($RES_SIM_47) (71|79) [SCAL] (1) $FUN_1.d = ThermofluidStream.Media.myMedia.Water.IF97_Utilities.rho_props_pT(source.p0_par, source.T0_par, ThermofluidStream.Media.myMedia.Water.IF97_Utilities.waterBaseProp_pT(source.p0_par, source.T0_par, 0)) ($RES_SIM_129) (72|80) [SCAL] (1) reservoir.medium.u = reservoir.medium.h - isenthalpic.p_out_set / reservoir.medium.d ($RES_SIM_49) (73|81) [SCAL] (1) reservoir.r_in = (massFlowRate.dr_corr + isenthalpic.outlet.r) - 0.0 * massFlowRate.L ($RES_SIM_5) (74|82) [SCAL] (1) massFlowRate.p_out = max(massFlowRate.p_min, massFlowRate.p_in) ($RES_SIM_4) (75|83) [SCAL] (1) massFlowRate.dr_corr = massFlowRate.p_in - massFlowRate.p_out ($RES_SIM_3) (76|84) [RECD] (5) massFlowRate.outlet.state = $FUN_8 ($RES_SIM_2) (77|89) [RECD] (5) reservoir.inlet.state = reservoir.state_in ($RES_BND_104) (78|94) [RECD] (5) isenthalpic.outlet.state = $FUN_7 ($RES_SIM_11) (79|99) [SCAL] (1) $FUN_19 = sqrt($FUN_18) ($RES_AUX_107) (80|100) [SCAL] (1) $FUN_18 = abs((2.0 * reservoir.L) / (reservoir.V * max(reservoir.density_derp_h, 1e-10))) ($RES_AUX_108) (81|101) [SCAL] (1) isenthalpic.p_out = isenthalpic.p_in + isenthalpic.dp ($RES_SIM_13) (82|102) [SCAL] (1) reservoir.p_in = reservoir.state_in.p ($RES_AUX_109) (83|103) [SCAL] (1) $FUN_1.T = source.T0_par ($RES_SIM_130) (84|104) [SCAL] (1) isenthalpic.outlet.r = source.outlet.r - 0.0 * isenthalpic.L ($RES_SIM_14) (85|105) [SCAL] (1) $FUN_1.p = source.p0_par ($RES_SIM_131) =================== Scalar Matching =================== variable to equation ********************** var 1 --> eqn 38 var 2 --> eqn -1 var 3 --> eqn 71 var 4 --> eqn 19 var 5 --> eqn 96 var 6 --> eqn 62 var 7 --> eqn 99 var 8 --> eqn 100 var 9 --> eqn 54 var 10 --> eqn 23 var 11 --> eqn 24 var 12 --> eqn 73 var 13 --> eqn 72 var 14 --> eqn 68 var 15 --> eqn 83 var 16 --> eqn 17 var 17 --> eqn 64 var 18 --> eqn 86 var 19 --> eqn 55 var 20 --> eqn 76 var 21 --> eqn 46 var 22 --> eqn 57 var 23 --> eqn 67 var 24 --> eqn 84 var 25 --> eqn 102 var 26 --> eqn 3 var 27 --> eqn 53 var 28 --> eqn 45 var 29 --> eqn 22 var 30 --> eqn 89 var 31 --> eqn 8 var 32 --> eqn 27 var 33 --> eqn 7 var 34 --> eqn 33 var 35 --> eqn 10 var 36 --> eqn 78 var 37 --> eqn 79 var 38 --> eqn 1 var 39 --> eqn 103 var 40 --> eqn 59 var 41 --> eqn 48 var 42 --> eqn 51 var 43 --> eqn 92 var 44 --> eqn 52 var 45 --> eqn 74 var 46 --> eqn 56 var 47 --> eqn 37 var 48 --> eqn 104 var 49 --> eqn 44 var 50 --> eqn 2 var 51 --> eqn 75 var 52 --> eqn 94 var 53 --> eqn 14 var 54 --> eqn 91 var 55 --> eqn 87 var 56 --> eqn 90 var 57 --> eqn 35 var 58 --> eqn 49 var 59 --> eqn 31 var 60 --> eqn 93 var 61 --> eqn 5 var 62 --> eqn 65 var 63 --> eqn 30 var 64 --> eqn 42 var 65 --> eqn 32 var 66 --> eqn 101 var 67 --> eqn -1 var 68 --> eqn 15 var 69 --> eqn 41 var 70 --> eqn 29 var 71 --> eqn 95 var 72 --> eqn 26 var 73 --> eqn 40 var 74 --> eqn 39 var 75 --> eqn 80 var 76 --> eqn 43 var 77 --> eqn 34 var 78 --> eqn 13 var 79 --> eqn 20 var 80 --> eqn 58 var 81 --> eqn 50 var 82 --> eqn 18 var 83 --> eqn 4 var 84 --> eqn 81 var 85 --> eqn 105 var 86 --> eqn 77 var 87 --> eqn 47 var 88 --> eqn 60 var 89 --> eqn 97 var 90 --> eqn 70 var 91 --> eqn 25 var 92 --> eqn 88 var 93 --> eqn 82 var 94 --> eqn 63 var 95 --> eqn 36 var 96 --> eqn 16 var 97 --> eqn 98 var 98 --> eqn 9 var 99 --> eqn 69 var 100 --> eqn 85 var 101 --> eqn 6 var 102 --> eqn 66 var 103 --> eqn 28 var 104 --> eqn 11 var 105 --> eqn 21 var 106 --> eqn 61 var 107 --> eqn 12 equation to variable ********************** eqn 1 --> var 38 eqn 2 --> var 50 eqn 3 --> var 26 eqn 4 --> var 83 eqn 5 --> var 61 eqn 6 --> var 101 eqn 7 --> var 33 eqn 8 --> var 31 eqn 9 --> var 98 eqn 10 --> var 35 eqn 11 --> var 104 eqn 12 --> var 107 eqn 13 --> var 78 eqn 14 --> var 53 eqn 15 --> var 68 eqn 16 --> var 96 eqn 17 --> var 16 eqn 18 --> var 82 eqn 19 --> var 4 eqn 20 --> var 79 eqn 21 --> var 105 eqn 22 --> var 29 eqn 23 --> var 10 eqn 24 --> var 11 eqn 25 --> var 91 eqn 26 --> var 72 eqn 27 --> var 32 eqn 28 --> var 103 eqn 29 --> var 70 eqn 30 --> var 63 eqn 31 --> var 59 eqn 32 --> var 65 eqn 33 --> var 34 eqn 34 --> var 77 eqn 35 --> var 57 eqn 36 --> var 95 eqn 37 --> var 47 eqn 38 --> var 1 eqn 39 --> var 74 eqn 40 --> var 73 eqn 41 --> var 69 eqn 42 --> var 64 eqn 43 --> var 76 eqn 44 --> var 49 eqn 45 --> var 28 eqn 46 --> var 21 eqn 47 --> var 87 eqn 48 --> var 41 eqn 49 --> var 58 eqn 50 --> var 81 eqn 51 --> var 42 eqn 52 --> var 44 eqn 53 --> var 27 eqn 54 --> var 9 eqn 55 --> var 19 eqn 56 --> var 46 eqn 57 --> var 22 eqn 58 --> var 80 eqn 59 --> var 40 eqn 60 --> var 88 eqn 61 --> var 106 eqn 62 --> var 6 eqn 63 --> var 94 eqn 64 --> var 17 eqn 65 --> var 62 eqn 66 --> var 102 eqn 67 --> var 23 eqn 68 --> var 14 eqn 69 --> var 99 eqn 70 --> var 90 eqn 71 --> var 3 eqn 72 --> var 13 eqn 73 --> var 12 eqn 74 --> var 45 eqn 75 --> var 51 eqn 76 --> var 20 eqn 77 --> var 86 eqn 78 --> var 36 eqn 79 --> var 37 eqn 80 --> var 75 eqn 81 --> var 84 eqn 82 --> var 93 eqn 83 --> var 15 eqn 84 --> var 24 eqn 85 --> var 100 eqn 86 --> var 18 eqn 87 --> var 55 eqn 88 --> var 92 eqn 89 --> var 30 eqn 90 --> var 56 eqn 91 --> var 54 eqn 92 --> var 43 eqn 93 --> var 60 eqn 94 --> var 52 eqn 95 --> var 71 eqn 96 --> var 5 eqn 97 --> var 89 eqn 98 --> var 97 eqn 99 --> var 7 eqn 100 --> var 8 eqn 101 --> var 66 eqn 102 --> var 25 eqn 103 --> var 39 eqn 104 --> var 48 eqn 105 --> var 85 " [Timeout remaining time 660] [Calling sys.exit(0), Time elapsed: 3.9549046345055103] Failed to read output from testmodel.py, exit status != 0: 0.14425956830382347 0.159157362 0.039940834 Calling exit ...