Running: ./testmodel.py --libraries=/home/hudson/saved_omc/libraries/.openmodelica/libraries --ompython_omhome=/usr ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating.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 0.001502/0.001502, allocations: 93.06 kB / 19.65 MB, free: 280 kB / 13.93 MB " [Timeout remaining time 180] loadFile("/home/hudson/saved_omc/libraries/.openmodelica/libraries/Complex 4.1.0+maint.om/package.mo", uses=false) [Timeout 180] "Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/Complex 4.1.0+maint.om/package.mo): time 0.001746/0.001746, allocations: 169.3 kB / 23.02 MB, free: 1.555 MB / 18.57 MB " [Timeout remaining time 180] loadFile("/home/hudson/saved_omc/libraries/.openmodelica/libraries/Modelica 4.1.0+maint.om/package.mo", uses=false) [Timeout 180] "Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/Modelica 4.1.0+maint.om/package.mo): time 0.9227/0.9227, allocations: 177.1 MB / 203.4 MB, free: 5.633 MB / 186.7 MB " [Timeout remaining time 179] loadFile("/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermofluidStream main/package.mo", uses=false) [Timeout 180] "Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermofluidStream main/package.mo): time 0.6642/0.6642, allocations: 118.6 MB / 378.6 MB, free: 1.484 MB / 346.7 MB " [Timeout remaining time 179] Using package ThermofluidStream with version 1.4.0 (/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.Boundaries.Tests.TankHeating,tolerance=1e-06,outputFormat="mat",numberOfIntervals=2500,variableFilter="CPUtime|EventCounter|NonlinearSystems.simulation.[0-9,]+..Calls|NonlinearSystems.simulation.[0-9,]+..Iterations|NonlinearSystems.simulation.[0-9,]+..Jacobians|NonlinearSystems.simulation.[0-9,]+..Residues|Time|_GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.H0|_GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.Hf|_GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.MM|_GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.R_s|_GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.Tlimit|_GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.ahigh.[0-9,]+.|_GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.alow.[0-9,]+.|_GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.bhigh.[0-9,]+.|_GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.blow.[0-9,]+.|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.H0|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.Hf|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.MM|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.R_s|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.Tlimit|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.ahigh.[0-9,]+.|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.alow.[0-9,]+.|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.bhigh.[0-9,]+.|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.blow.[0-9,]+.|acceleration.a.[0-9,]+.|acceleration.ax|acceleration.ay|acceleration.az|acceleration.setFromInputs|dropOfCommons.L|dropOfCommons.assertionLevel|dropOfCommons.g|dropOfCommons.instanceNameColor.[0-9,]+.|dropOfCommons.k_volume_damping|dropOfCommons.m_flow_reg|dropOfCommons.omega_reg|dropOfCommons.p_min|dropOfCommons.rho_min|fixedHeatFlow.Q_flow|fixedHeatFlow.T_ref|fixedHeatFlow.alpha|fixedHeatFlow.port.Q_flow|fixedHeatFlow.port.T|flowResistance.D_h|flowResistance.L|flowResistance.L_value|flowResistance.Xi_in.[0-9,]+.|flowResistance.Xi_out.[0-9,]+.|flowResistance.a|flowResistance.areaCross|flowResistance.areaCrossInput|flowResistance.areaHydraulic|flowResistance.b|flowResistance.clip_p_out|flowResistance.dp|flowResistance.dr_corr|flowResistance.h_in|flowResistance.h_out|flowResistance.initM_flow|der.flowResistance.inlet.m_flow.|flowResistance.inlet.m_flow|flowResistance.inlet.r|flowResistance.inlet.state.T|flowResistance.inlet.state.X.[0-9,]+.|flowResistance.inlet.state.p|flowResistance.l|flowResistance.m_acceleration_0|flowResistance.m_flow|flowResistance.m_flowStateSelect|flowResistance.m_flow_0|flowResistance.mu_in|flowResistance.outlet.m_flow|flowResistance.outlet.r|flowResistance.outlet.state.T|flowResistance.outlet.state.X.[0-9,]+.|flowResistance.outlet.state.p|flowResistance.p_in|flowResistance.p_min|flowResistance.p_out|flowResistance.perimeter|flowResistance.perimeterInput|flowResistance.r|flowResistance.rho_in|flowResistance.rho_min|flowResistance.shape|flowResistance1.D_h|flowResistance1.L|flowResistance1.L_value|flowResistance1.Xi_in.[0-9,]+.|flowResistance1.Xi_out.[0-9,]+.|flowResistance1.a|flowResistance1.areaCross|flowResistance1.areaCrossInput|flowResistance1.areaHydraulic|flowResistance1.b|flowResistance1.clip_p_out|flowResistance1.dp|flowResistance1.dr_corr|flowResistance1.h_in|flowResistance1.h_out|flowResistance1.initM_flow|der.flowResistance1.inlet.m_flow.|flowResistance1.inlet.m_flow|flowResistance1.inlet.r|flowResistance1.inlet.state.T|flowResistance1.inlet.state.X.[0-9,]+.|flowResistance1.inlet.state.p|flowResistance1.l|flowResistance1.m_acceleration_0|flowResistance1.m_flow|flowResistance1.m_flowStateSelect|flowResistance1.m_flow_0|flowResistance1.mu_in|flowResistance1.outlet.m_flow|flowResistance1.outlet.r|flowResistance1.outlet.state.T|flowResistance1.outlet.state.X.[0-9,]+.|flowResistance1.outlet.state.p|flowResistance1.p_in|flowResistance1.p_min|flowResistance1.p_out|flowResistance1.perimeter|flowResistance1.perimeterInput|flowResistance1.r|flowResistance1.rho_in|flowResistance1.rho_min|flowResistance1.shape|flowResistance2.D_h|flowResistance2.L|flowResistance2.L_value|flowResistance2.Xi_in.[0-9,]+.|flowResistance2.Xi_out.[0-9,]+.|flowResistance2.a|flowResistance2.areaCross|flowResistance2.areaCrossInput|flowResistance2.areaHydraulic|flowResistance2.b|flowResistance2.clip_p_out|flowResistance2.dp|flowResistance2.dr_corr|flowResistance2.h_in|flowResistance2.h_out|flowResistance2.initM_flow|der.flowResistance2.inlet.m_flow.|flowResistance2.inlet.m_flow|flowResistance2.inlet.r|flowResistance2.inlet.state.T|flowResistance2.inlet.state.X.[0-9,]+.|flowResistance2.inlet.state.p|flowResistance2.l|flowResistance2.m_acceleration_0|flowResistance2.m_flow|flowResistance2.m_flowStateSelect|flowResistance2.m_flow_0|flowResistance2.mu_in|flowResistance2.outlet.m_flow|flowResistance2.outlet.r|flowResistance2.outlet.state.T|flowResistance2.outlet.state.X.[0-9,]+.|flowResistance2.outlet.state.p|flowResistance2.p_in|flowResistance2.p_min|flowResistance2.p_out|flowResistance2.perimeter|flowResistance2.perimeterInput|flowResistance2.r|flowResistance2.rho_in|flowResistance2.rho_min|flowResistance2.shape|flowResistance3.D_h|flowResistance3.L|flowResistance3.L_value|flowResistance3.Xi_in.[0-9,]+.|flowResistance3.Xi_out.[0-9,]+.|flowResistance3.a|flowResistance3.areaCross|flowResistance3.areaCrossInput|flowResistance3.areaHydraulic|flowResistance3.b|flowResistance3.clip_p_out|flowResistance3.dp|flowResistance3.dr_corr|flowResistance3.h_in|flowResistance3.h_out|flowResistance3.initM_flow|der.flowResistance3.inlet.m_flow.|flowResistance3.inlet.m_flow|flowResistance3.inlet.r|flowResistance3.inlet.state.T|flowResistance3.inlet.state.X.[0-9,]+.|flowResistance3.inlet.state.p|flowResistance3.l|flowResistance3.m_acceleration_0|flowResistance3.m_flow|flowResistance3.m_flowStateSelect|flowResistance3.m_flow_0|flowResistance3.mu_in|flowResistance3.outlet.m_flow|flowResistance3.outlet.r|flowResistance3.outlet.state.T|flowResistance3.outlet.state.X.[0-9,]+.|flowResistance3.outlet.state.p|flowResistance3.p_in|flowResistance3.p_min|flowResistance3.p_out|flowResistance3.perimeter|flowResistance3.perimeterInput|flowResistance3.r|flowResistance3.rho_in|flowResistance3.rho_min|flowResistance3.shape|sink1.L|der.sink1.inlet.m_flow.|sink1.inlet.m_flow|sink1.inlet.r|sink1.inlet.state.T|sink1.inlet.state.X.[0-9,]+.|sink1.inlet.state.p|sink1.p|sink1.p0|sink1.p0_par|sink1.r|source.L|source.T0|source.T0_par|source.Xi0.[0-9,]+.|source.Xi0_par.[0-9,]+.|source.h0|source.h0_par|der.source.outlet.m_flow.|source.outlet.m_flow|source.outlet.r|source.outlet.state.T|source.outlet.state.X.[0-9,]+.|source.outlet.state.p|source.p0|source.p0_par|source1.L|source1.T0|source1.T0_par|source1.Xi0.[0-9,]+.|source1.Xi0_par.[0-9,]+.|source1.h0|source1.h0_par|der.source1.outlet.m_flow.|source1.outlet.m_flow|source1.outlet.r|source1.outlet.state.T|source1.outlet.state.X.[0-9,]+.|source1.outlet.state.p|source1.p0|source1.p0_par|staticHead.L|staticHead.L_value|staticHead.Xi_in.[0-9,]+.|staticHead.Xi_out.[0-9,]+.|staticHead.clip_p_out|staticHead.displayPositions|staticHead.dp|staticHead.dr_corr|staticHead.fromPosition.[0-9,]+.|staticHead.h_in|staticHead.h_out|staticHead.initM_flow|der.staticHead.inlet.m_flow.|staticHead.inlet.m_flow|staticHead.inlet.r|staticHead.inlet.state.T|staticHead.inlet.state.X.[0-9,]+.|staticHead.inlet.state.p|staticHead.m_acceleration_0|staticHead.m_flow|staticHead.m_flowStateSelect|staticHead.m_flow_0|staticHead.outlet.m_flow|staticHead.outlet.r|staticHead.outlet.state.T|staticHead.outlet.state.X.[0-9,]+.|staticHead.outlet.state.p|staticHead.p_in|staticHead.p_min|staticHead.p_out|staticHead.rho_in|staticHead.rho_min|staticHead.staticHead|staticHead.staticHead_Pa_relative|staticHead.toPosition.[0-9,]+.|tank.A|tank.Area|tank.AxLimit|tank.AzLimit|tank.D|tank.D1|tank.D2|tank.D3|tank.D4|tank.K|tank.L|tank.M|tank.MXi.[0-9,]+.|tank.M_liq_start|tank.M_outlets|tank.N_inlets|tank.Q_flow|tank.T_heatPort|tank.T_start|tank.ThresholdEmpty|tank.ThresholdFull|tank.U|tank.U_med|tank.V|tank.V_liquid|tank.V_ref|tank.W_v|tank.Xi_0.[0-9,]+.|tank.Xi_in.[0-9,]+.|tank.Xi_out.[0-9,]+.|tank.centerOfMass.[0-9,]+.|tank.d|tank.density_derp_h|der.tank.M.|der.tank.MXi.[0-9,]+..|der.tank.U_med.|tank.eps_geometry|tank.fEmpty|tank.fFull|tank.gasDensity|tank.h_in.[0-9,]+.|tank.h_out.[0-9,]+.|tank.h_start|tank.initialize_LiquidMass|tank.initialize_Xi|tank.initialize_energy|tank.initialize_pressure|tank.inletPositions.[0-9,]+.|der.tank.inlet.[0-9,]+..m_flow.|tank.inlet.[0-9,]+..m_flow|tank.inlet.[0-9,]+..r|tank.inlet.[0-9,]+..state.T|tank.inlet.[0-9,]+..state.X.[0-9,]+.|tank.inlet.[0-9,]+..state.p|tank.k_volume_damping|tank.liquidDensity|tank.m_flow_assert|tank.m_flow_in.[0-9,]+.|tank.m_flow_out.[0-9,]+.|tank.medium.MM|tank.medium.R_s|tank.medium.T|tank.medium.T_degC|tank.medium.X.[0-9,]+.|tank.medium.Xi.[0-9,]+.|tank.medium.d|tank.medium.h|tank.medium.p|tank.medium.p_bar|tank.medium.preferredMediumStates|tank.medium.standardOrderComponents|tank.medium.state.T|tank.medium.state.X.[0-9,]+.|tank.medium.state.p|tank.medium.u|tank.normAcc.[0-9,]+.|tank.nx|tank.nz|tank.outletPositions.[0-9,]+.|tank.outletTransition|der.tank.outlet.[0-9,]+..m_flow.|tank.outlet.[0-9,]+..m_flow|tank.outlet.[0-9,]+..r|tank.outlet.[0-9,]+..state.T|tank.outlet.[0-9,]+..state.X.[0-9,]+.|tank.outlet.[0-9,]+..state.p|tank.p_in.[0-9,]+.|tank.p_ref|tank.p_start|tank.r.[0-9,]+.|tank.r_damping|tank.shiftOutlet.[0-9,]+.|tank.state_out.[0-9,]+..T|tank.state_out.[0-9,]+..X.[0-9,]+.|tank.state_out.[0-9,]+..p|tank.staticHeadInlets.[0-9,]+.|tank.staticHeadInlets_Pa_relative.[0-9,]+.|tank.staticHeadOutlets.[0-9,]+.|tank.staticHeadOutlets_Pa_relative.[0-9,]+.|tank.tankCenter.[0-9,]+.|tank.useHeatport|tank.usePreferredMediumStates|tank.use_hstart|tank.xLength|tank.yLength|tank.zLength|tank1.A|tank1.Area|tank1.AxLimit|tank1.AzLimit|tank1.D|tank1.D1|tank1.D2|tank1.D3|tank1.D4|tank1.K|tank1.L|tank1.M|tank1.MXi.[0-9,]+.|tank1.M_liq_start|tank1.M_outlets|tank1.N_inlets|tank1.Q_flow|tank1.T_heatPort|tank1.T_start|tank1.ThresholdEmpty|tank1.ThresholdFull|tank1.U|tank1.U_med|tank1.V|tank1.V_liquid|tank1.V_ref|tank1.W_v|tank1.Xi_0.[0-9,]+.|tank1.Xi_in.[0-9,]+.|tank1.Xi_out.[0-9,]+.|tank1.centerOfMass.[0-9,]+.|tank1.d|tank1.density_derp_h|der.tank1.M.|der.tank1.MXi.[0-9,]+..|der.tank1.U_med.|tank1.eps_geometry|tank1.fEmpty|tank1.fFull|tank1.gasDensity|tank1.h_in.[0-9,]+.|tank1.h_out.[0-9,]+.|tank1.h_start|tank1.heatPort.Q_flow|tank1.heatPort.T|tank1.initialize_LiquidMass|tank1.initialize_Xi|tank1.initialize_energy|tank1.initialize_pressure|tank1.inletPositions.[0-9,]+.|der.tank1.inlet.[0-9,]+..m_flow.|tank1.inlet.[0-9,]+..m_flow|tank1.inlet.[0-9,]+..r|tank1.inlet.[0-9,]+..state.T|tank1.inlet.[0-9,]+..state.X.[0-9,]+.|tank1.inlet.[0-9,]+..state.p|tank1.k_volume_damping|tank1.liquidDensity|tank1.m_flow_assert|tank1.m_flow_in.[0-9,]+.|tank1.m_flow_out.[0-9,]+.|tank1.medium.MM|tank1.medium.R_s|tank1.medium.T|tank1.medium.T_degC|tank1.medium.X.[0-9,]+.|tank1.medium.Xi.[0-9,]+.|tank1.medium.d|tank1.medium.h|tank1.medium.p|tank1.medium.p_bar|tank1.medium.preferredMediumStates|tank1.medium.standardOrderComponents|tank1.medium.state.T|tank1.medium.state.X.[0-9,]+.|tank1.medium.state.p|tank1.medium.u|tank1.normAcc.[0-9,]+.|tank1.nx|tank1.nz|tank1.outletPositions.[0-9,]+.|tank1.outletTransition|der.tank1.outlet.[0-9,]+..m_flow.|tank1.outlet.[0-9,]+..m_flow|tank1.outlet.[0-9,]+..r|tank1.outlet.[0-9,]+..state.T|tank1.outlet.[0-9,]+..state.X.[0-9,]+.|tank1.outlet.[0-9,]+..state.p|tank1.p_in.[0-9,]+.|tank1.p_ref|tank1.p_start|tank1.r.[0-9,]+.|tank1.r_damping|tank1.shiftOutlet.[0-9,]+.|tank1.state_out.[0-9,]+..T|tank1.state_out.[0-9,]+..X.[0-9,]+.|tank1.state_out.[0-9,]+..p|tank1.staticHeadInlets.[0-9,]+.|tank1.staticHeadInlets_Pa_relative.[0-9,]+.|tank1.staticHeadOutlets.[0-9,]+.|tank1.staticHeadOutlets_Pa_relative.[0-9,]+.|tank1.tankCenter.[0-9,]+.|tank1.useHeatport|tank1.usePreferredMediumStates|tank1.use_hstart|tank1.xLength|tank1.yLength|tank1.zLength",fileNamePrefix="ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating") translateModel(ThermofluidStream.Boundaries.Tests.TankHeating,tolerance=1e-06,outputFormat="mat",numberOfIntervals=2500,variableFilter="CPUtime|EventCounter|NonlinearSystems.simulation.[0-9,]+..Calls|NonlinearSystems.simulation.[0-9,]+..Iterations|NonlinearSystems.simulation.[0-9,]+..Jacobians|NonlinearSystems.simulation.[0-9,]+..Residues|Time|_GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.H0|_GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.Hf|_GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.MM|_GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.R_s|_GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.Tlimit|_GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.ahigh.[0-9,]+.|_GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.alow.[0-9,]+.|_GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.bhigh.[0-9,]+.|_GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.blow.[0-9,]+.|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.H0|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.Hf|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.MM|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.R_s|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.Tlimit|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.ahigh.[0-9,]+.|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.alow.[0-9,]+.|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.bhigh.[0-9,]+.|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.blow.[0-9,]+.|acceleration.a.[0-9,]+.|acceleration.ax|acceleration.ay|acceleration.az|acceleration.setFromInputs|dropOfCommons.L|dropOfCommons.assertionLevel|dropOfCommons.g|dropOfCommons.instanceNameColor.[0-9,]+.|dropOfCommons.k_volume_damping|dropOfCommons.m_flow_reg|dropOfCommons.omega_reg|dropOfCommons.p_min|dropOfCommons.rho_min|fixedHeatFlow.Q_flow|fixedHeatFlow.T_ref|fixedHeatFlow.alpha|fixedHeatFlow.port.Q_flow|fixedHeatFlow.port.T|flowResistance.D_h|flowResistance.L|flowResistance.L_value|flowResistance.Xi_in.[0-9,]+.|flowResistance.Xi_out.[0-9,]+.|flowResistance.a|flowResistance.areaCross|flowResistance.areaCrossInput|flowResistance.areaHydraulic|flowResistance.b|flowResistance.clip_p_out|flowResistance.dp|flowResistance.dr_corr|flowResistance.h_in|flowResistance.h_out|flowResistance.initM_flow|der.flowResistance.inlet.m_flow.|flowResistance.inlet.m_flow|flowResistance.inlet.r|flowResistance.inlet.state.T|flowResistance.inlet.state.X.[0-9,]+.|flowResistance.inlet.state.p|flowResistance.l|flowResistance.m_acceleration_0|flowResistance.m_flow|flowResistance.m_flowStateSelect|flowResistance.m_flow_0|flowResistance.mu_in|flowResistance.outlet.m_flow|flowResistance.outlet.r|flowResistance.outlet.state.T|flowResistance.outlet.state.X.[0-9,]+.|flowResistance.outlet.state.p|flowResistance.p_in|flowResistance.p_min|flowResistance.p_out|flowResistance.perimeter|flowResistance.perimeterInput|flowResistance.r|flowResistance.rho_in|flowResistance.rho_min|flowResistance.shape|flowResistance1.D_h|flowResistance1.L|flowResistance1.L_value|flowResistance1.Xi_in.[0-9,]+.|flowResistance1.Xi_out.[0-9,]+.|flowResistance1.a|flowResistance1.areaCross|flowResistance1.areaCrossInput|flowResistance1.areaHydraulic|flowResistance1.b|flowResistance1.clip_p_out|flowResistance1.dp|flowResistance1.dr_corr|flowResistance1.h_in|flowResistance1.h_out|flowResistance1.initM_flow|der.flowResistance1.inlet.m_flow.|flowResistance1.inlet.m_flow|flowResistance1.inlet.r|flowResistance1.inlet.state.T|flowResistance1.inlet.state.X.[0-9,]+.|flowResistance1.inlet.state.p|flowResistance1.l|flowResistance1.m_acceleration_0|flowResistance1.m_flow|flowResistance1.m_flowStateSelect|flowResistance1.m_flow_0|flowResistance1.mu_in|flowResistance1.outlet.m_flow|flowResistance1.outlet.r|flowResistance1.outlet.state.T|flowResistance1.outlet.state.X.[0-9,]+.|flowResistance1.outlet.state.p|flowResistance1.p_in|flowResistance1.p_min|flowResistance1.p_out|flowResistance1.perimeter|flowResistance1.perimeterInput|flowResistance1.r|flowResistance1.rho_in|flowResistance1.rho_min|flowResistance1.shape|flowResistance2.D_h|flowResistance2.L|flowResistance2.L_value|flowResistance2.Xi_in.[0-9,]+.|flowResistance2.Xi_out.[0-9,]+.|flowResistance2.a|flowResistance2.areaCross|flowResistance2.areaCrossInput|flowResistance2.areaHydraulic|flowResistance2.b|flowResistance2.clip_p_out|flowResistance2.dp|flowResistance2.dr_corr|flowResistance2.h_in|flowResistance2.h_out|flowResistance2.initM_flow|der.flowResistance2.inlet.m_flow.|flowResistance2.inlet.m_flow|flowResistance2.inlet.r|flowResistance2.inlet.state.T|flowResistance2.inlet.state.X.[0-9,]+.|flowResistance2.inlet.state.p|flowResistance2.l|flowResistance2.m_acceleration_0|flowResistance2.m_flow|flowResistance2.m_flowStateSelect|flowResistance2.m_flow_0|flowResistance2.mu_in|flowResistance2.outlet.m_flow|flowResistance2.outlet.r|flowResistance2.outlet.state.T|flowResistance2.outlet.state.X.[0-9,]+.|flowResistance2.outlet.state.p|flowResistance2.p_in|flowResistance2.p_min|flowResistance2.p_out|flowResistance2.perimeter|flowResistance2.perimeterInput|flowResistance2.r|flowResistance2.rho_in|flowResistance2.rho_min|flowResistance2.shape|flowResistance3.D_h|flowResistance3.L|flowResistance3.L_value|flowResistance3.Xi_in.[0-9,]+.|flowResistance3.Xi_out.[0-9,]+.|flowResistance3.a|flowResistance3.areaCross|flowResistance3.areaCrossInput|flowResistance3.areaHydraulic|flowResistance3.b|flowResistance3.clip_p_out|flowResistance3.dp|flowResistance3.dr_corr|flowResistance3.h_in|flowResistance3.h_out|flowResistance3.initM_flow|der.flowResistance3.inlet.m_flow.|flowResistance3.inlet.m_flow|flowResistance3.inlet.r|flowResistance3.inlet.state.T|flowResistance3.inlet.state.X.[0-9,]+.|flowResistance3.inlet.state.p|flowResistance3.l|flowResistance3.m_acceleration_0|flowResistance3.m_flow|flowResistance3.m_flowStateSelect|flowResistance3.m_flow_0|flowResistance3.mu_in|flowResistance3.outlet.m_flow|flowResistance3.outlet.r|flowResistance3.outlet.state.T|flowResistance3.outlet.state.X.[0-9,]+.|flowResistance3.outlet.state.p|flowResistance3.p_in|flowResistance3.p_min|flowResistance3.p_out|flowResistance3.perimeter|flowResistance3.perimeterInput|flowResistance3.r|flowResistance3.rho_in|flowResistance3.rho_min|flowResistance3.shape|sink1.L|der.sink1.inlet.m_flow.|sink1.inlet.m_flow|sink1.inlet.r|sink1.inlet.state.T|sink1.inlet.state.X.[0-9,]+.|sink1.inlet.state.p|sink1.p|sink1.p0|sink1.p0_par|sink1.r|source.L|source.T0|source.T0_par|source.Xi0.[0-9,]+.|source.Xi0_par.[0-9,]+.|source.h0|source.h0_par|der.source.outlet.m_flow.|source.outlet.m_flow|source.outlet.r|source.outlet.state.T|source.outlet.state.X.[0-9,]+.|source.outlet.state.p|source.p0|source.p0_par|source1.L|source1.T0|source1.T0_par|source1.Xi0.[0-9,]+.|source1.Xi0_par.[0-9,]+.|source1.h0|source1.h0_par|der.source1.outlet.m_flow.|source1.outlet.m_flow|source1.outlet.r|source1.outlet.state.T|source1.outlet.state.X.[0-9,]+.|source1.outlet.state.p|source1.p0|source1.p0_par|staticHead.L|staticHead.L_value|staticHead.Xi_in.[0-9,]+.|staticHead.Xi_out.[0-9,]+.|staticHead.clip_p_out|staticHead.displayPositions|staticHead.dp|staticHead.dr_corr|staticHead.fromPosition.[0-9,]+.|staticHead.h_in|staticHead.h_out|staticHead.initM_flow|der.staticHead.inlet.m_flow.|staticHead.inlet.m_flow|staticHead.inlet.r|staticHead.inlet.state.T|staticHead.inlet.state.X.[0-9,]+.|staticHead.inlet.state.p|staticHead.m_acceleration_0|staticHead.m_flow|staticHead.m_flowStateSelect|staticHead.m_flow_0|staticHead.outlet.m_flow|staticHead.outlet.r|staticHead.outlet.state.T|staticHead.outlet.state.X.[0-9,]+.|staticHead.outlet.state.p|staticHead.p_in|staticHead.p_min|staticHead.p_out|staticHead.rho_in|staticHead.rho_min|staticHead.staticHead|staticHead.staticHead_Pa_relative|staticHead.toPosition.[0-9,]+.|tank.A|tank.Area|tank.AxLimit|tank.AzLimit|tank.D|tank.D1|tank.D2|tank.D3|tank.D4|tank.K|tank.L|tank.M|tank.MXi.[0-9,]+.|tank.M_liq_start|tank.M_outlets|tank.N_inlets|tank.Q_flow|tank.T_heatPort|tank.T_start|tank.ThresholdEmpty|tank.ThresholdFull|tank.U|tank.U_med|tank.V|tank.V_liquid|tank.V_ref|tank.W_v|tank.Xi_0.[0-9,]+.|tank.Xi_in.[0-9,]+.|tank.Xi_out.[0-9,]+.|tank.centerOfMass.[0-9,]+.|tank.d|tank.density_derp_h|der.tank.M.|der.tank.MXi.[0-9,]+..|der.tank.U_med.|tank.eps_geometry|tank.fEmpty|tank.fFull|tank.gasDensity|tank.h_in.[0-9,]+.|tank.h_out.[0-9,]+.|tank.h_start|tank.initialize_LiquidMass|tank.initialize_Xi|tank.initialize_energy|tank.initialize_pressure|tank.inletPositions.[0-9,]+.|der.tank.inlet.[0-9,]+..m_flow.|tank.inlet.[0-9,]+..m_flow|tank.inlet.[0-9,]+..r|tank.inlet.[0-9,]+..state.T|tank.inlet.[0-9,]+..state.X.[0-9,]+.|tank.inlet.[0-9,]+..state.p|tank.k_volume_damping|tank.liquidDensity|tank.m_flow_assert|tank.m_flow_in.[0-9,]+.|tank.m_flow_out.[0-9,]+.|tank.medium.MM|tank.medium.R_s|tank.medium.T|tank.medium.T_degC|tank.medium.X.[0-9,]+.|tank.medium.Xi.[0-9,]+.|tank.medium.d|tank.medium.h|tank.medium.p|tank.medium.p_bar|tank.medium.preferredMediumStates|tank.medium.standardOrderComponents|tank.medium.state.T|tank.medium.state.X.[0-9,]+.|tank.medium.state.p|tank.medium.u|tank.normAcc.[0-9,]+.|tank.nx|tank.nz|tank.outletPositions.[0-9,]+.|tank.outletTransition|der.tank.outlet.[0-9,]+..m_flow.|tank.outlet.[0-9,]+..m_flow|tank.outlet.[0-9,]+..r|tank.outlet.[0-9,]+..state.T|tank.outlet.[0-9,]+..state.X.[0-9,]+.|tank.outlet.[0-9,]+..state.p|tank.p_in.[0-9,]+.|tank.p_ref|tank.p_start|tank.r.[0-9,]+.|tank.r_damping|tank.shiftOutlet.[0-9,]+.|tank.state_out.[0-9,]+..T|tank.state_out.[0-9,]+..X.[0-9,]+.|tank.state_out.[0-9,]+..p|tank.staticHeadInlets.[0-9,]+.|tank.staticHeadInlets_Pa_relative.[0-9,]+.|tank.staticHeadOutlets.[0-9,]+.|tank.staticHeadOutlets_Pa_relative.[0-9,]+.|tank.tankCenter.[0-9,]+.|tank.useHeatport|tank.usePreferredMediumStates|tank.use_hstart|tank.xLength|tank.yLength|tank.zLength|tank1.A|tank1.Area|tank1.AxLimit|tank1.AzLimit|tank1.D|tank1.D1|tank1.D2|tank1.D3|tank1.D4|tank1.K|tank1.L|tank1.M|tank1.MXi.[0-9,]+.|tank1.M_liq_start|tank1.M_outlets|tank1.N_inlets|tank1.Q_flow|tank1.T_heatPort|tank1.T_start|tank1.ThresholdEmpty|tank1.ThresholdFull|tank1.U|tank1.U_med|tank1.V|tank1.V_liquid|tank1.V_ref|tank1.W_v|tank1.Xi_0.[0-9,]+.|tank1.Xi_in.[0-9,]+.|tank1.Xi_out.[0-9,]+.|tank1.centerOfMass.[0-9,]+.|tank1.d|tank1.density_derp_h|der.tank1.M.|der.tank1.MXi.[0-9,]+..|der.tank1.U_med.|tank1.eps_geometry|tank1.fEmpty|tank1.fFull|tank1.gasDensity|tank1.h_in.[0-9,]+.|tank1.h_out.[0-9,]+.|tank1.h_start|tank1.heatPort.Q_flow|tank1.heatPort.T|tank1.initialize_LiquidMass|tank1.initialize_Xi|tank1.initialize_energy|tank1.initialize_pressure|tank1.inletPositions.[0-9,]+.|der.tank1.inlet.[0-9,]+..m_flow.|tank1.inlet.[0-9,]+..m_flow|tank1.inlet.[0-9,]+..r|tank1.inlet.[0-9,]+..state.T|tank1.inlet.[0-9,]+..state.X.[0-9,]+.|tank1.inlet.[0-9,]+..state.p|tank1.k_volume_damping|tank1.liquidDensity|tank1.m_flow_assert|tank1.m_flow_in.[0-9,]+.|tank1.m_flow_out.[0-9,]+.|tank1.medium.MM|tank1.medium.R_s|tank1.medium.T|tank1.medium.T_degC|tank1.medium.X.[0-9,]+.|tank1.medium.Xi.[0-9,]+.|tank1.medium.d|tank1.medium.h|tank1.medium.p|tank1.medium.p_bar|tank1.medium.preferredMediumStates|tank1.medium.standardOrderComponents|tank1.medium.state.T|tank1.medium.state.X.[0-9,]+.|tank1.medium.state.p|tank1.medium.u|tank1.normAcc.[0-9,]+.|tank1.nx|tank1.nz|tank1.outletPositions.[0-9,]+.|tank1.outletTransition|der.tank1.outlet.[0-9,]+..m_flow.|tank1.outlet.[0-9,]+..m_flow|tank1.outlet.[0-9,]+..r|tank1.outlet.[0-9,]+..state.T|tank1.outlet.[0-9,]+..state.X.[0-9,]+.|tank1.outlet.[0-9,]+..state.p|tank1.p_in.[0-9,]+.|tank1.p_ref|tank1.p_start|tank1.r.[0-9,]+.|tank1.r_damping|tank1.shiftOutlet.[0-9,]+.|tank1.state_out.[0-9,]+..T|tank1.state_out.[0-9,]+..X.[0-9,]+.|tank1.state_out.[0-9,]+..p|tank1.staticHeadInlets.[0-9,]+.|tank1.staticHeadInlets_Pa_relative.[0-9,]+.|tank1.staticHeadOutlets.[0-9,]+.|tank1.staticHeadOutlets_Pa_relative.[0-9,]+.|tank1.tankCenter.[0-9,]+.|tank1.useHeatport|tank1.usePreferredMediumStates|tank1.use_hstart|tank1.xLength|tank1.yLength|tank1.zLength",fileNamePrefix="ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating") [Timeout 660] "Notification: Performance of FrontEnd - loaded program: time 1.543e-06/1.543e-06, allocations: 0 / 483.6 MB, free: 8.16 MB / 410.7 MB Notification: Performance of FrontEnd - Absyn->SCode: time 2.09e-05/2.244e-05, allocations: 2.312 kB / 483.6 MB, free: 8.156 MB / 410.7 MB Notification: Performance of NFInst.instantiate(ThermofluidStream.Boundaries.Tests.TankHeating): time 0.1328/0.1328, allocations: 153.3 MB / 0.622 GB, free: 6.859 MB / 0.5417 GB Notification: Performance of NFInst.instExpressions: time 0.005431/0.1382, allocations: 3.869 MB / 0.6258 GB, free: 2.98 MB / 0.5417 GB Notification: Performance of NFInst.updateImplicitVariability: time 0.0008916/0.1391, allocations: 59.44 kB / 0.6258 GB, free: 2.922 MB / 0.5417 GB Notification: Performance of NFTyping.typeComponents: time 0.0008168/0.1399, allocations: 325.3 kB / 0.6261 GB, free: 2.602 MB / 0.5417 GB Notification: Performance of NFTyping.typeBindings: time 0.003694/0.1436, allocations: 2 MB / 0.6281 GB, free: 0.5898 MB / 0.5417 GB Notification: Performance of NFTyping.typeClassSections: time 0.0023/0.1459, allocations: 1.223 MB / 0.6293 GB, free: 15.36 MB / 0.5573 GB Notification: Performance of NFFlatten.flatten: time 0.003486/0.1494, allocations: 3.5 MB / 0.6327 GB, free: 11.85 MB / 0.5573 GB Notification: Performance of NFFlatten.resolveConnections: time 0.0004667/0.1499, allocations: 240.5 kB / 0.6329 GB, free: 11.59 MB / 0.5573 GB Notification: Performance of NFEvalConstants.evaluate: time 0.003589/0.1535, allocations: 2.085 MB / 0.635 GB, free: 9.5 MB / 0.5573 GB Notification: Performance of NFSimplifyModel.simplify: time 0.001678/0.1551, allocations: 1.422 MB / 0.6363 GB, free: 8.074 MB / 0.5573 GB Notification: Performance of NFPackage.collectConstants: time 0.000434/0.1556, allocations: 208 kB / 0.6365 GB, free: 7.871 MB / 0.5573 GB Notification: Performance of NFFlatten.collectFunctions: time 0.003086/0.1587, allocations: 1.83 MB / 0.6383 GB, free: 6.039 MB / 0.5573 GB Notification: Performance of NFScalarize.scalarize: time 0.0006533/0.1593, allocations: 0.8453 MB / 0.6392 GB, free: 5.191 MB / 0.5573 GB Notification: Performance of NFVerifyModel.verify: time 0.000989/0.1603, allocations: 0.8302 MB / 0.64 GB, free: 4.359 MB / 0.5573 GB Notification: Performance of NFConvertDAE.convert: time 0.0039/0.1642, allocations: 2.886 MB / 0.6428 GB, free: 1.465 MB / 0.5573 GB Notification: Performance of FrontEnd - DAE generated: time 3.947e-06/0.1642, allocations: 0 / 0.6428 GB, free: 1.465 MB / 0.5573 GB Notification: Performance of FrontEnd: time 1.343e-06/0.1642, allocations: 0 / 0.6428 GB, free: 1.465 MB / 0.5573 GB Notification: Performance of Transformations before backend: time 5.482e-05/0.1643, allocations: 0 / 0.6428 GB, free: 1.465 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: 350 * Number of variables: 350 Notification: Performance of Generate backend data structure: time 0.2304/0.3947, allocations: 3.034 MB / 0.6457 GB, free: 34.81 MB / 0.5573 GB Notification: Performance of prepare preOptimizeDAE: time 4.975e-05/0.3947, allocations: 11.97 kB / 0.6458 GB, free: 34.81 MB / 0.5573 GB Notification: Performance of preOpt normalInlineFunction (simulation): time 0.002136/0.3969, allocations: 0.638 MB / 0.6464 GB, free: 34.7 MB / 0.5573 GB Notification: Performance of preOpt evaluateParameters (simulation): time 0.002445/0.3993, allocations: 1.218 MB / 0.6476 GB, free: 34.38 MB / 0.5573 GB Notification: Performance of preOpt simplifyIfEquations (simulation): time 0.0005198/0.3998, allocations: 1.009 MB / 0.6486 GB, free: 33.38 MB / 0.5573 GB Notification: Performance of preOpt expandDerOperator (simulation): time 0.0003508/0.4002, allocations: 154.5 kB / 0.6487 GB, free: 33.37 MB / 0.5573 GB Notification: Performance of preOpt clockPartitioning (simulation): time 0.003248/0.4034, allocations: 2.106 MB / 0.6508 GB, free: 32.53 MB / 0.5573 GB Notification: Performance of preOpt findStateOrder (simulation): time 2.888e-05/0.4035, allocations: 3.938 kB / 0.6508 GB, free: 32.53 MB / 0.5573 GB Notification: Performance of preOpt replaceEdgeChange (simulation): time 0.0001443/0.4036, allocations: 55.98 kB / 0.6508 GB, free: 32.53 MB / 0.5573 GB Notification: Performance of preOpt inlineArrayEqn (simulation): time 0.0003547/0.404, allocations: 196.5 kB / 0.651 GB, free: 32.53 MB / 0.5573 GB Notification: Performance of preOpt removeEqualRHS (simulation): time 0.002026/0.406, allocations: 1.21 MB / 0.6522 GB, free: 32.5 MB / 0.5573 GB Notification: Performance of preOpt removeSimpleEquations (simulation): time 0.008959/0.415, allocations: 6.398 MB / 0.6584 GB, free: 30.35 MB / 0.5573 GB Notification: Performance of preOpt comSubExp (simulation): time 0.001809/0.4168, allocations: 1.035 MB / 0.6594 GB, free: 30.3 MB / 0.5573 GB Notification: Performance of preOpt resolveLoops (simulation): time 0.0009412/0.4177, allocations: 0.6084 MB / 0.66 GB, free: 30.29 MB / 0.5573 GB Notification: Performance of preOpt evalFunc (simulation): time 0.0003102/0.418, allocations: 117.5 kB / 0.6601 GB, free: 30.28 MB / 0.5573 GB Notification: Performance of preOpt encapsulateWhenConditions (simulation): time 4.812e-05/0.4181, allocations: 61.42 kB / 0.6602 GB, free: 30.24 MB / 0.5573 GB Notification: Performance of pre-optimization done (n=187): time 5.51e-06/0.4181, allocations: 0.9062 kB / 0.6602 GB, free: 30.24 MB / 0.5573 GB Notification: Performance of matching and sorting (n=187): time 0.004965/0.423, allocations: 2.456 MB / 0.6626 GB, free: 29.97 MB / 0.5573 GB Notification: Performance of inlineWhenForInitialization (initialization): time 3.464e-05/0.4231, allocations: 72.64 kB / 0.6627 GB, free: 29.91 MB / 0.5573 GB Notification: Performance of selectInitializationVariablesDAE (initialization): time 0.001079/0.4242, allocations: 0.9224 MB / 0.6636 GB, free: 29.7 MB / 0.5573 GB Notification: Performance of collectPreVariables (initialization): time 0.0002255/0.4244, allocations: 60.45 kB / 0.6636 GB, free: 29.67 MB / 0.5573 GB Notification: Performance of collectInitialEqns (initialization): time 0.0004254/0.4248, allocations: 0.6742 MB / 0.6643 GB, free: 29.44 MB / 0.5573 GB Notification: Performance of collectInitialBindings (initialization): time 0.0005085/0.4253, allocations: 0.6634 MB / 0.6649 GB, free: 29.08 MB / 0.5573 GB Notification: Performance of simplifyInitialFunctions (initialization): time 0.0006078/0.4259, allocations: 354.5 kB / 0.6653 GB, free: 29.05 MB / 0.5573 GB Notification: Performance of setup shared object (initialization): time 4.685e-05/0.426, allocations: 477.8 kB / 0.6657 GB, free: 28.59 MB / 0.5573 GB Notification: Performance of preBalanceInitialSystem (initialization): time 0.001005/0.427, allocations: 488.2 kB / 0.6662 GB, free: 28.58 MB / 0.5573 GB Notification: Performance of partitionIndependentBlocks (initialization): time 0.001307/0.4283, allocations: 1.215 MB / 0.6674 GB, free: 27.77 MB / 0.5573 GB Notification: Performance of analyzeInitialSystem (initialization): time 0.003126/0.4314, allocations: 1.685 MB / 0.669 GB, free: 27.59 MB / 0.5573 GB Notification: Performance of solveInitialSystemEqSystem (initialization): time 7.545e-06/0.4314, allocations: 1.312 kB / 0.669 GB, free: 27.59 MB / 0.5573 GB Notification: Performance of matching and sorting (n=210) (initialization): time 0.003566/0.435, allocations: 1.756 MB / 0.6707 GB, free: 27.36 MB / 0.5573 GB Notification: Performance of prepare postOptimizeDAE: time 2.717e-05/0.435, allocations: 6.719 kB / 0.6708 GB, free: 27.36 MB / 0.5573 GB Notification: Performance of postOpt simplifyComplexFunction (initialization): time 1.396e-05/0.435, allocations: 3.156 kB / 0.6708 GB, free: 27.36 MB / 0.5573 GB Notification: Performance of postOpt tearingSystem (initialization): time 0.000631/0.4356, allocations: 195.7 kB / 0.6709 GB, free: 27.3 MB / 0.5573 GB Notification: Performance of postOpt solveSimpleEquations (initialization): time 0.00116/0.4368, allocations: 380.5 kB / 0.6713 GB, free: 27.3 MB / 0.5573 GB Notification: Performance of postOpt calculateStrongComponentJacobians (initialization): time 0.003473/0.4403, allocations: 8.94 MB / 0.68 GB, free: 18.66 MB / 0.5573 GB Notification: Performance of postOpt simplifyAllExpressions (initialization): time 0.002113/0.4424, allocations: 359.9 kB / 0.6804 GB, free: 18.6 MB / 0.5573 GB Notification: Performance of postOpt collapseArrayExpressions (initialization): time 0.0003743/0.4428, allocations: 119.2 kB / 0.6805 GB, free: 18.6 MB / 0.5573 GB Warning: Assuming fixed start value for the following 4 variables: staticHead.inlet.m_flow:VARIABLE(flow=true min = -1e5 max = 1e5 unit = \"kg/s\" fixed = true ) \"Mass flow rate\" type: Real flowResistance3.inlet.m_flow:VARIABLE(flow=true min = -1e5 max = 1e5 unit = \"kg/s\" fixed = true ) \"Mass flow rate\" type: Real flowResistance1.inlet.m_flow:VARIABLE(flow=true min = -1e5 max = 1e5 unit = \"kg/s\" fixed = true ) \"Mass flow rate\" type: Real flowResistance.inlet.m_flow:VARIABLE(flow=true min = -1e5 max = 1e5 unit = \"kg/s\" fixed = true ) \"Mass flow rate\" type: Real Notification: Model statistics after passing the back-end for initialization: * Number of independent subsystems: 10 * Number of states: 0 () * Number of discrete variables: 4 (tank1.fEmpty,tank1.fFull,tank.fEmpty,tank.fFull) * Number of discrete states: 0 () * Number of clocked states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for initialization (179): * Single equations (assignments): 163 * Array equations: 7 * Algorithm blocks: 0 * Record equations: 4 * When equations: 0 * If-equations: 0 * Equation systems (not torn): 0 * Torn equation systems: 5 * Mixed (continuous/discrete) equation systems: 0 Notification: Torn system details for strict tearing set: * Linear torn systems (#iteration vars, #inner vars, density): 5 systems {(1,3,100.0%), (1,2,100.0%), (1,2,100.0%), (1,2,100.0%), (1,1,100.0%)} * Non-linear torn systems (#iteration vars, #inner vars): 0 systems Notification: Performance of prepare postOptimizeDAE: time 0.0008692/0.4436, allocations: 260.7 kB / 0.6807 GB, free: 18.44 MB / 0.5573 GB Notification: Performance of postOpt lateInlineFunction (simulation): time 0.0005149/0.4442, allocations: 220.5 kB / 0.681 GB, free: 18.35 MB / 0.5573 GB Notification: Performance of postOpt wrapFunctionCalls (simulation): time 0.003919/0.4481, allocations: 2.962 MB / 0.6838 GB, free: 17.98 MB / 0.5573 GB Notification: Performance of postOpt inlineArrayEqn (simulation): time 0.002327/0.4504, allocations: 1.532 MB / 0.6853 GB, free: 17.82 MB / 0.5573 GB Notification: Performance of postOpt constantLinearSystem (simulation): time 1.04e-05/0.4504, allocations: 3.5 kB / 0.6853 GB, free: 17.82 MB / 0.5573 GB Notification: Performance of postOpt simplifysemiLinear (simulation): time 1.479e-05/0.4504, allocations: 9.672 kB / 0.6854 GB, free: 17.82 MB / 0.5573 GB Notification: Performance of postOpt removeSimpleEquations (simulation): time 0.006008/0.4564, allocations: 3.739 MB / 0.689 GB, free: 17.25 MB / 0.5573 GB Notification: Performance of postOpt simplifyComplexFunction (simulation): time 7.014e-06/0.4564, allocations: 0 / 0.689 GB, free: 17.25 MB / 0.5573 GB Notification: Performance of postOpt solveSimpleEquations (simulation): time 0.0009854/0.4574, allocations: 365.5 kB / 0.6894 GB, free: 17.24 MB / 0.5573 GB Notification: Performance of postOpt tearingSystem (simulation): time 0.001109/0.4585, allocations: 414.7 kB / 0.6897 GB, free: 17.15 MB / 0.5573 GB Notification: Performance of postOpt inputDerivativesUsed (simulation): time 0.0001801/0.4587, allocations: 79.22 kB / 0.6898 GB, free: 17.15 MB / 0.5573 GB Notification: Performance of postOpt calculateStrongComponentJacobians (simulation): time 0.003422/0.4621, allocations: 10.6 MB / 0.7002 GB, free: 22.89 MB / 0.573 GB Notification: Performance of postOpt calculateStateSetsJacobians (simulation): time 2.645e-06/0.4621, allocations: 1.781 kB / 0.7002 GB, free: 22.89 MB / 0.573 GB Notification: Performance of postOpt symbolicJacobian (simulation): time 0.004461/0.4666, allocations: 2.604 MB / 0.7027 GB, free: 22.46 MB / 0.573 GB Notification: Performance of postOpt removeConstants (simulation): time 0.0008904/0.4675, allocations: 474.1 kB / 0.7032 GB, free: 22.33 MB / 0.573 GB Notification: Performance of postOpt simplifyTimeIndepFuncCalls (simulation): time 0.0002194/0.4677, allocations: 44.89 kB / 0.7032 GB, free: 22.33 MB / 0.573 GB Notification: Performance of postOpt simplifyAllExpressions (simulation): time 0.0009232/0.4686, allocations: 140.9 kB / 0.7033 GB, free: 22.33 MB / 0.573 GB Notification: Performance of postOpt findZeroCrossings (simulation): time 0.0003774/0.469, allocations: 242.8 kB / 0.7036 GB, free: 22.33 MB / 0.573 GB Notification: Performance of postOpt collapseArrayExpressions (simulation): time 0.0001936/0.4692, allocations: 119.3 kB / 0.7037 GB, free: 22.33 MB / 0.573 GB Notification: Performance of sorting global known variables: time 0.0006014/0.4698, allocations: 0.6094 MB / 0.7043 GB, free: 22.18 MB / 0.573 GB Notification: Performance of sort global known variables: time 9e-08/0.4698, allocations: 0.8438 kB / 0.7043 GB, free: 22.18 MB / 0.573 GB Notification: Performance of remove unused functions: time 0.001837/0.4716, allocations: 0.7694 MB / 0.705 GB, free: 22.09 MB / 0.573 GB Notification: Model statistics after passing the back-end for simulation: * Number of independent subsystems: 1 * Number of states: 12 (tank.M,tank.MXi[1],tank.MXi[2],tank.U_med,flowResistance.inlet.m_flow,flowResistance1.inlet.m_flow,tank1.M,tank1.MXi[1],tank1.MXi[2],tank1.U_med,flowResistance3.inlet.m_flow,staticHead.inlet.m_flow) * Number of discrete variables: 4 (tank.fFull,tank.fEmpty,tank1.fFull,tank1.fEmpty) * Number of discrete states: 0 () * Number of clocked states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for simulation (171): * Single equations (assignments): 153 * Array equations: 7 * Algorithm blocks: 0 * Record equations: 4 * When equations: 0 * If-equations: 0 * Equation systems (not torn): 0 * Torn equation systems: 7 * Mixed (continuous/discrete) equation systems: 0 Notification: Torn system details for strict tearing set: * Linear torn systems (#iteration vars, #inner vars, density): 5 systems {(1,2,100.0%), (1,2,100.0%), (1,3,100.0%), (1,2,100.0%), (1,1,100.0%)} * Non-linear torn systems (#iteration vars, #inner vars): 2 systems {(2,3), (2,3)} Notification: Performance of Backend phase and start with SimCode phase: time 0.0009045/0.4725, allocations: 478 kB / 0.7055 GB, free: 21.96 MB / 0.573 GB Notification: Performance of simCode: created initialization part: time 0.003531/0.4761, allocations: 2.412 MB / 0.7079 GB, free: 20.99 MB / 0.573 GB Notification: Performance of simCode: created event and clocks part: time 5.139e-06/0.4761, allocations: 1.094 kB / 0.7079 GB, free: 20.99 MB / 0.573 GB Notification: Performance of simCode: created simulation system equations: time 0.001959/0.478, allocations: 1.883 MB / 0.7097 GB, free: 20.03 MB / 0.573 GB Notification: Performance of simCode: created of all other equations (e.g. parameter, nominal, assert, etc): time 0.00223/0.4803, allocations: 0.799 MB / 0.7105 GB, free: 19.95 MB / 0.573 GB Notification: Performance of simCode: created linear, non-linear and system jacobian parts: time 0.005432/0.4857, allocations: 3.665 MB / 0.7141 GB, free: 18.56 MB / 0.573 GB Notification: Performance of simCode: some other stuff during SimCode phase: time 0.0003592/0.4861, allocations: 412.6 kB / 0.7144 GB, free: 18.45 MB / 0.573 GB Notification: Performance of simCode: alias equations: time 0.001777/0.4878, allocations: 0.5583 MB / 0.715 GB, free: 18.3 MB / 0.573 GB Notification: Performance of simCode: all other stuff during SimCode phase: time 0.0006455/0.4885, allocations: 225.5 kB / 0.7152 GB, free: 18.29 MB / 0.573 GB Notification: Performance of SimCode: time 1.783e-06/0.4885, allocations: 0 / 0.7152 GB, free: 18.29 MB / 0.573 GB Notification: Performance of Templates: time 0.05416/0.5426, allocations: 48.46 MB / 0.7625 GB, free: 0.9453 MB / 0.5886 GB " [Timeout remaining time 659] make -j1 -f ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating.makefile [Timeout 660] (rm -f ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating.pipe ; mkfifo ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating.pipe ; head -c 1048576 < ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating.pipe >> ../files/ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating.sim & ./ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating -abortSlowSimulation -alarm=240 -emit_protected -lv LOG_STATS > ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating.pipe 2>&1) [Timeout 240] diffSimulationResults("ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat","/mnt/ReferenceFiles/ThermofluidStream-main-regression/ReferenceData/ThermofluidStream.Boundaries.Tests.TankHeating_ref.mat","",relTol=0.003,relTolDiffMinMax=0.003,rangeDelta=0.001) [Timeout 660] "Error: Could not read variable CPUtime in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat. Warning: Get data of variable CPUtime from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat failed! Error: Could not read variable EventCounter in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat. Warning: Get data of variable EventCounter from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat failed! Error: Could not read variable NonlinearSystems.simulation[1].Calls in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat. Warning: Get data of variable NonlinearSystems.simulation[1].Calls from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat failed! Error: Could not read variable NonlinearSystems.simulation[1].Iterations in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat. Warning: Get data of variable NonlinearSystems.simulation[1].Iterations from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat failed! Error: Could not read variable NonlinearSystems.simulation[1].Jacobians in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat. Warning: Get data of variable NonlinearSystems.simulation[1].Jacobians from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat failed! Error: Could not read variable NonlinearSystems.simulation[1].Residues in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat. Warning: Get data of variable NonlinearSystems.simulation[1].Residues from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat failed! Error: Could not read variable NonlinearSystems.simulation[2].Calls in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat. Warning: Get data of variable NonlinearSystems.simulation[2].Calls from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat failed! Error: Could not read variable NonlinearSystems.simulation[2].Iterations in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat. Warning: Get data of variable NonlinearSystems.simulation[2].Iterations from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat failed! Error: Could not read variable NonlinearSystems.simulation[2].Jacobians in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat. Warning: Get data of variable NonlinearSystems.simulation[2].Jacobians from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat failed! Error: Could not read variable NonlinearSystems.simulation[2].Residues in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat. Warning: Get data of variable NonlinearSystems.simulation[2].Residues from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat failed! Error: Could not read variable _GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.H0 in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat. Warning: Get data of variable _GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.H0 from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat failed! Error: Could not read variable _GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.Hf in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat. Warning: Get data of variable _GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.Hf from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat failed! Error: Could not read variable _GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.MM in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat. Warning: Get data of variable _GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.MM from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat failed! Error: Could not read variable _GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.R_s in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat. Warning: Get data of variable _GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.R_s from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat failed! Error: Could not read variable _GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.Tlimit in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat. Warning: Get data of variable _GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.Tlimit from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat failed! Error: Could not read variable _GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.ahigh[1] in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat. Warning: Get data of variable _GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.ahigh[1] from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat failed! Error: Could not read variable _GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.ahigh[2] in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat. Warning: Get data of variable _GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.ahigh[2] from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat failed! Error: Could not read variable _GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.ahigh[3] in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat. Warning: Get data of variable _GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.ahigh[3] from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat failed! Error: Could not read variable _GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.ahigh[4] in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat. Warning: Get data of variable _GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.ahigh[4] from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat failed! Error: Could not read variable _GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.ahigh[5] in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat. Warning: Get data of variable _GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.ahigh[5] from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat failed! Error: Could not read variable _GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.ahigh[6] in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat. Warning: Get data of variable _GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.ahigh[6] from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat failed! Error: Could not read variable _GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.ahigh[7] in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat. Warning: Get data of variable _GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.ahigh[7] from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat failed! Error: Could not read variable _GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.alow[1] in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat. Warning: Get data of variable _GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.alow[1] from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat failed! Error: Could not read variable _GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.alow[2] in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat. Warning: Get data of variable _GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.alow[2] from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat failed! Error: Could not read variable _GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.alow[3] in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat. Warning: Get data of variable _GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.alow[3] from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat failed! Error: Could not read variable _GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.alow[4] in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat. Warning: Get data of variable _GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.alow[4] from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat failed! Error: Could not read variable _GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.alow[5] in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat. Warning: Get data of variable _GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.alow[5] from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat failed! Error: Could not read variable _GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.alow[6] in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat. Warning: Get data of variable _GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.alow[6] from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat failed! Error: Could not read variable _GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.alow[7] in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat. Warning: Get data of variable _GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.alow[7] from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat failed! Error: Could not read variable _GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.bhigh[1] in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat. Warning: Get data of variable _GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.bhigh[1] from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat failed! Error: Could not read variable _GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.bhigh[2] in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat. Warning: Get data of variable _GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.bhigh[2] from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat failed! Error: Could not read variable _GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.blow[1] in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat. Warning: Get data of variable _GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.blow[1] from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat failed! Error: Could not read variable _GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.blow[2] in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat. Warning: Get data of variable _GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.blow[2] from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat failed! Error: Could not read variable _GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.H0 in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat. Warning: Get data of variable _GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.H0 from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat failed! Error: Could not read variable _GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.Hf in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat. Warning: Get data of variable _GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.Hf from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat failed! Error: Could not read variable _GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.MM in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat. Warning: Get data of variable _GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.MM from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat failed! Error: Could not read variable _GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.R_s in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat. Warning: Get data of variable _GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.R_s from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat failed! Error: Could not read variable _GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.Tlimit in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat. Warning: Get data of variable _GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.Tlimit from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat failed! Error: Could not read variable _GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.ahigh[1] in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat. Warning: Get data of variable _GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.ahigh[1] from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat failed! Error: Could not read variable _GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.ahigh[2] in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat. Warning: Get data of variable _GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.ahigh[2] from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat failed! Error: Could not read variable _GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.ahigh[3] in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat. Warning: Get data of variable _GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.ahigh[3] from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat failed! Error: Could not read variable _GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.ahigh[4] in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat. Warning: Get data of variable _GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.ahigh[4] from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat failed! Error: Could not read variable _GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.ahigh[5] in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat. Warning: Get data of variable _GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.ahigh[5] from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat failed! Error: Could not read variable _GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.ahigh[6] in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat. Warning: Get data of variable _GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.ahigh[6] from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat failed! Error: Could not read variable _GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.ahigh[7] in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat. Warning: Get data of variable _GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.ahigh[7] from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat failed! Error: Could not read variable _GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.alow[1] in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat. Warning: Get data of variable _GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.alow[1] from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat failed! Error: Could not read variable _GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.alow[2] in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat. Warning: Get data of variable _GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.alow[2] from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat failed! Error: Could not read variable _GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.alow[3] in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat. Warning: Get data of variable _GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.alow[3] from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat failed! Error: Could not read variable _GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.alow[4] in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat. Warning: Get data of variable _GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.alow[4] from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat failed! Error: Could not read variable _GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.alow[5] in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat. Warning: Get data of variable _GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.alow[5] from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat failed! Error: Could not read variable _GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.alow[6] in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat. Warning: Get data of variable _GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.alow[6] from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat failed! Error: Could not read variable _GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.alow[7] in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat. Warning: Get data of variable _GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.alow[7] from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat failed! Error: Could not read variable _GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.bhigh[1] in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat. Warning: Get data of variable _GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.bhigh[1] from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat failed! Error: Could not read variable _GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.bhigh[2] in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat. Warning: Get data of variable _GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.bhigh[2] from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat failed! Error: Could not read variable _GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.blow[1] in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat. Warning: Get data of variable _GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.blow[1] from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat failed! Error: Could not read variable _GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.blow[2] in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat. Warning: Get data of variable _GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.blow[2] from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat failed! Error: Could not read variable dropOfCommons.instanceNameColor[1] in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat. Warning: Get data of variable dropOfCommons.instanceNameColor[1] from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat failed! Error: Could not read variable dropOfCommons.instanceNameColor[2] in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat. Warning: Get data of variable dropOfCommons.instanceNameColor[2] from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat failed! Error: Could not read variable dropOfCommons.instanceNameColor[3] in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat. Warning: Get data of variable dropOfCommons.instanceNameColor[3] from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat failed! Error: Could not read variable tank.inlet[1].der(m_flow) in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat. Warning: Get data of variable tank.inlet[1].der(m_flow) from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat failed! Error: Could not read variable tank.inlet[2].der(m_flow) in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat. Warning: Get data of variable tank.inlet[2].der(m_flow) from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat failed! Error: Could not read variable tank.outlet[1].der(m_flow) in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat. Warning: Get data of variable tank.outlet[1].der(m_flow) from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat failed! Error: Could not read variable tank1.outlet[1].der(m_flow) in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat. Warning: Get data of variable tank1.outlet[1].der(m_flow) from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat failed! " [Timeout remaining time 660] "" Variables in the reference:CPUtime,EventCounter,NonlinearSystems.simulation[1].Calls,NonlinearSystems.simulation[1].Iterations,NonlinearSystems.simulation[1].Jacobians,NonlinearSystems.simulation[1].Residues,NonlinearSystems.simulation[2].Calls,NonlinearSystems.simulation[2].Iterations,NonlinearSystems.simulation[2].Jacobians,NonlinearSystems.simulation[2].Residues,Time,_GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.H0,_GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.Hf,_GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.MM,_GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.R_s,_GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.Tlimit,_GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.ahigh[1],_GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.ahigh[2],_GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.ahigh[3],_GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.ahigh[4],_GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.ahigh[5],_GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.ahigh[6],_GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.ahigh[7],_GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.alow[1],_GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.alow[2],_GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.alow[3],_GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.alow[4],_GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.alow[5],_GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.alow[6],_GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.alow[7],_GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.bhigh[1],_GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.bhigh[2],_GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.blow[1],_GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.blow[2],_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.H0,_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.Hf,_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.MM,_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.R_s,_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.Tlimit,_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.ahigh[1],_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.ahigh[2],_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.ahigh[3],_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.ahigh[4],_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.ahigh[5],_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.ahigh[6],_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.ahigh[7],_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.alow[1],_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.alow[2],_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.alow[3],_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.alow[4],_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.alow[5],_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.alow[6],_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.alow[7],_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.bhigh[1],_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.bhigh[2],_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.blow[1],_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.blow[2],acceleration.a[1],acceleration.a[2],acceleration.a[3],acceleration.ax,acceleration.ay,acceleration.az,acceleration.setFromInputs,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,fixedHeatFlow.Q_flow,fixedHeatFlow.T_ref,fixedHeatFlow.alpha,fixedHeatFlow.port.Q_flow,fixedHeatFlow.port.T,flowResistance.D_h,flowResistance.L,flowResistance.L_value,flowResistance.Xi_in[1],flowResistance.Xi_in[2],flowResistance.Xi_out[1],flowResistance.Xi_out[2],flowResistance.a,flowResistance.areaCross,flowResistance.areaCrossInput,flowResistance.areaHydraulic,flowResistance.b,flowResistance.clip_p_out,flowResistance.dp,flowResistance.dr_corr,flowResistance.h_in,flowResistance.h_out,flowResistance.initM_flow,der(flowResistance.inlet.m_flow),flowResistance.inlet.m_flow,flowResistance.inlet.r,flowResistance.inlet.state.T,flowResistance.inlet.state.X[1],flowResistance.inlet.state.X[2],flowResistance.inlet.state.p,flowResistance.l,flowResistance.m_acceleration_0,flowResistance.m_flow,flowResistance.m_flowStateSelect,flowResistance.m_flow_0,flowResistance.mu_in,flowResistance.outlet.m_flow,flowResistance.outlet.r,flowResistance.outlet.state.T,flowResistance.outlet.state.X[1],flowResistance.outlet.state.X[2],flowResistance.outlet.state.p,flowResistance.p_in,flowResistance.p_min,flowResistance.p_out,flowResistance.perimeter,flowResistance.perimeterInput,flowResistance.r,flowResistance.rho_in,flowResistance.rho_min,flowResistance.shape,flowResistance1.D_h,flowResistance1.L,flowResistance1.L_value,flowResistance1.Xi_in[1],flowResistance1.Xi_in[2],flowResistance1.Xi_out[1],flowResistance1.Xi_out[2],flowResistance1.a,flowResistance1.areaCross,flowResistance1.areaCrossInput,flowResistance1.areaHydraulic,flowResistance1.b,flowResistance1.clip_p_out,flowResistance1.dp,flowResistance1.dr_corr,flowResistance1.h_in,flowResistance1.h_out,flowResistance1.initM_flow,der(flowResistance1.inlet.m_flow),flowResistance1.inlet.m_flow,flowResistance1.inlet.r,flowResistance1.inlet.state.T,flowResistance1.inlet.state.X[1],flowResistance1.inlet.state.X[2],flowResistance1.inlet.state.p,flowResistance1.l,flowResistance1.m_acceleration_0,flowResistance1.m_flow,flowResistance1.m_flowStateSelect,flowResistance1.m_flow_0,flowResistance1.mu_in,flowResistance1.outlet.m_flow,flowResistance1.outlet.r,flowResistance1.outlet.state.T,flowResistance1.outlet.state.X[1],flowResistance1.outlet.state.X[2],flowResistance1.outlet.state.p,flowResistance1.p_in,flowResistance1.p_min,flowResistance1.p_out,flowResistance1.perimeter,flowResistance1.perimeterInput,flowResistance1.r,flowResistance1.rho_in,flowResistance1.rho_min,flowResistance1.shape,flowResistance2.D_h,flowResistance2.L,flowResistance2.L_value,flowResistance2.Xi_in[1],flowResistance2.Xi_in[2],flowResistance2.Xi_out[1],flowResistance2.Xi_out[2],flowResistance2.a,flowResistance2.areaCross,flowResistance2.areaCrossInput,flowResistance2.areaHydraulic,flowResistance2.b,flowResistance2.clip_p_out,flowResistance2.dp,flowResistance2.dr_corr,flowResistance2.h_in,flowResistance2.h_out,flowResistance2.initM_flow,der(flowResistance2.inlet.m_flow),flowResistance2.inlet.m_flow,flowResistance2.inlet.r,flowResistance2.inlet.state.T,flowResistance2.inlet.state.X[1],flowResistance2.inlet.state.X[2],flowResistance2.inlet.state.p,flowResistance2.l,flowResistance2.m_acceleration_0,flowResistance2.m_flow,flowResistance2.m_flowStateSelect,flowResistance2.m_flow_0,flowResistance2.mu_in,flowResistance2.outlet.m_flow,flowResistance2.outlet.r,flowResistance2.outlet.state.T,flowResistance2.outlet.state.X[1],flowResistance2.outlet.state.X[2],flowResistance2.outlet.state.p,flowResistance2.p_in,flowResistance2.p_min,flowResistance2.p_out,flowResistance2.perimeter,flowResistance2.perimeterInput,flowResistance2.r,flowResistance2.rho_in,flowResistance2.rho_min,flowResistance2.shape,flowResistance3.D_h,flowResistance3.L,flowResistance3.L_value,flowResistance3.Xi_in[1],flowResistance3.Xi_in[2],flowResistance3.Xi_out[1],flowResistance3.Xi_out[2],flowResistance3.a,flowResistance3.areaCross,flowResistance3.areaCrossInput,flowResistance3.areaHydraulic,flowResistance3.b,flowResistance3.clip_p_out,flowResistance3.dp,flowResistance3.dr_corr,flowResistance3.h_in,flowResistance3.h_out,flowResistance3.initM_flow,der(flowResistance3.inlet.m_flow),flowResistance3.inlet.m_flow,flowResistance3.inlet.r,flowResistance3.inlet.state.T,flowResistance3.inlet.state.X[1],flowResistance3.inlet.state.X[2],flowResistance3.inlet.state.p,flowResistance3.l,flowResistance3.m_acceleration_0,flowResistance3.m_flow,flowResistance3.m_flowStateSelect,flowResistance3.m_flow_0,flowResistance3.mu_in,flowResistance3.outlet.m_flow,flowResistance3.outlet.r,flowResistance3.outlet.state.T,flowResistance3.outlet.state.X[1],flowResistance3.outlet.state.X[2],flowResistance3.outlet.state.p,flowResistance3.p_in,flowResistance3.p_min,flowResistance3.p_out,flowResistance3.perimeter,flowResistance3.perimeterInput,flowResistance3.r,flowResistance3.rho_in,flowResistance3.rho_min,flowResistance3.shape,sink1.L,der(sink1.inlet.m_flow),sink1.inlet.m_flow,sink1.inlet.r,sink1.inlet.state.T,sink1.inlet.state.X[1],sink1.inlet.state.X[2],sink1.inlet.state.p,sink1.p,sink1.p0,sink1.p0_par,sink1.r,source.L,source.T0,source.T0_par,source.Xi0[1],source.Xi0[2],source.Xi0_par[1],source.Xi0_par[2],source.h0,source.h0_par,der(source.outlet.m_flow),source.outlet.m_flow,source.outlet.r,source.outlet.state.T,source.outlet.state.X[1],source.outlet.state.X[2],source.outlet.state.p,source.p0,source.p0_par,source1.L,source1.T0,source1.T0_par,source1.Xi0[1],source1.Xi0[2],source1.Xi0_par[1],source1.Xi0_par[2],source1.h0,source1.h0_par,der(source1.outlet.m_flow),source1.outlet.m_flow,source1.outlet.r,source1.outlet.state.T,source1.outlet.state.X[1],source1.outlet.state.X[2],source1.outlet.state.p,source1.p0,source1.p0_par,staticHead.L,staticHead.L_value,staticHead.Xi_in[1],staticHead.Xi_in[2],staticHead.Xi_out[1],staticHead.Xi_out[2],staticHead.clip_p_out,staticHead.displayPositions,staticHead.dp,staticHead.dr_corr,staticHead.fromPosition[1],staticHead.fromPosition[2],staticHead.fromPosition[3],staticHead.h_in,staticHead.h_out,staticHead.initM_flow,der(staticHead.inlet.m_flow),staticHead.inlet.m_flow,staticHead.inlet.r,staticHead.inlet.state.T,staticHead.inlet.state.X[1],staticHead.inlet.state.X[2],staticHead.inlet.state.p,staticHead.m_acceleration_0,staticHead.m_flow,staticHead.m_flowStateSelect,staticHead.m_flow_0,staticHead.outlet.m_flow,staticHead.outlet.r,staticHead.outlet.state.T,staticHead.outlet.state.X[1],staticHead.outlet.state.X[2],staticHead.outlet.state.p,staticHead.p_in,staticHead.p_min,staticHead.p_out,staticHead.rho_in,staticHead.rho_min,staticHead.staticHead,staticHead.staticHead_Pa_relative,staticHead.toPosition[1],staticHead.toPosition[2],staticHead.toPosition[3],tank.A,tank.Area,tank.AxLimit,tank.AzLimit,tank.D,tank.D1,tank.D2,tank.D3,tank.D4,tank.K,tank.L,tank.M,tank.MXi[1],tank.MXi[2],tank.M_liq_start,tank.M_outlets,tank.N_inlets,tank.Q_flow,tank.T_heatPort,tank.T_start,tank.ThresholdEmpty,tank.ThresholdFull,tank.U,tank.U_med,tank.V,tank.V_liquid,tank.V_ref,tank.W_v,tank.Xi_0[1],tank.Xi_0[2],tank.Xi_in[1,1],tank.Xi_in[1,2],tank.Xi_in[2,1],tank.Xi_in[2,2],tank.Xi_out[1,1],tank.Xi_out[2,1],tank.centerOfMass[1],tank.centerOfMass[2],tank.centerOfMass[3],tank.d,tank.density_derp_h,der(tank.M),der(tank.MXi[1]),der(tank.MXi[2]),der(tank.U_med),tank.eps_geometry,tank.fEmpty,tank.fFull,tank.gasDensity,tank.h_in[1],tank.h_in[2],tank.h_out[1],tank.h_start,tank.initialize_LiquidMass,tank.initialize_Xi,tank.initialize_energy,tank.initialize_pressure,tank.inletPositions[1,1],tank.inletPositions[1,2],tank.inletPositions[1,3],tank.inletPositions[2,1],tank.inletPositions[2,2],tank.inletPositions[2,3],der(tank.inlet[1].m_flow),tank.inlet[1].m_flow,tank.inlet[1].r,tank.inlet[1].state.T,tank.inlet[1].state.X[1],tank.inlet[1].state.X[2],tank.inlet[1].state.p,der(tank.inlet[2].m_flow),tank.inlet[2].m_flow,tank.inlet[2].r,tank.inlet[2].state.T,tank.inlet[2].state.X[1],tank.inlet[2].state.X[2],tank.inlet[2].state.p,tank.k_volume_damping,tank.liquidDensity,tank.m_flow_assert,tank.m_flow_in[1],tank.m_flow_in[2],tank.m_flow_out[1],tank.medium.MM,tank.medium.R_s,tank.medium.T,tank.medium.T_degC,tank.medium.X[1],tank.medium.X[2],tank.medium.Xi[1],tank.medium.Xi[2],tank.medium.d,tank.medium.h,tank.medium.p,tank.medium.p_bar,tank.medium.preferredMediumStates,tank.medium.standardOrderComponents,tank.medium.state.T,tank.medium.state.X[1],tank.medium.state.X[2],tank.medium.state.p,tank.medium.u,tank.normAcc[1],tank.normAcc[2],tank.normAcc[3],tank.nx,tank.nz,tank.outletPositions[1,1],tank.outletPositions[1,2],tank.outletPositions[1,3],tank.outletTransition,der(tank.outlet[1].m_flow),tank.outlet[1].m_flow,tank.outlet[1].r,tank.outlet[1].state.T,tank.outlet[1].state.X[1],tank.outlet[1].state.X[2],tank.outlet[1].state.p,tank.p_in[1],tank.p_in[2],tank.p_ref,tank.p_start,tank.r[1],tank.r[2],tank.r_damping,tank.shiftOutlet[1],tank.state_out[1].T,tank.state_out[1].X[1],tank.state_out[1].X[2],tank.state_out[1].p,tank.staticHeadInlets[1],tank.staticHeadInlets[2],tank.staticHeadInlets_Pa_relative[1],tank.staticHeadInlets_Pa_relative[2],tank.staticHeadOutlets[1],tank.staticHeadOutlets_Pa_relative[1],tank.tankCenter[1],tank.tankCenter[2],tank.tankCenter[3],tank.useHeatport,tank.usePreferredMediumStates,tank.use_hstart,tank.xLength,tank.yLength,tank.zLength,tank1.A,tank1.Area,tank1.AxLimit,tank1.AzLimit,tank1.D,tank1.D1,tank1.D2,tank1.D3,tank1.D4,tank1.K,tank1.L,tank1.M,tank1.MXi[1],tank1.MXi[2],tank1.M_liq_start,tank1.M_outlets,tank1.N_inlets,tank1.Q_flow,tank1.T_heatPort,tank1.T_start,tank1.ThresholdEmpty,tank1.ThresholdFull,tank1.U,tank1.U_med,tank1.V,tank1.V_liquid,tank1.V_ref,tank1.W_v,tank1.Xi_0[1],tank1.Xi_0[2],tank1.Xi_in[1,1],tank1.Xi_in[2,1],tank1.Xi_out[1,1],tank1.Xi_out[2,1],tank1.centerOfMass[1],tank1.centerOfMass[2],tank1.centerOfMass[3],tank1.d,tank1.density_derp_h,der(tank1.M),der(tank1.MXi[1]),der(tank1.MXi[2]),der(tank1.U_med),tank1.eps_geometry,tank1.fEmpty,tank1.fFull,tank1.gasDensity,tank1.h_in[1],tank1.h_out[1],tank1.h_start,tank1.heatPort.Q_flow,tank1.heatPort.T,tank1.initialize_LiquidMass,tank1.initialize_Xi,tank1.initialize_energy,tank1.initialize_pressure,tank1.inletPositions[1,1],tank1.inletPositions[1,2],tank1.inletPositions[1,3],der(tank1.inlet[1].m_flow),tank1.inlet[1].m_flow,tank1.inlet[1].r,tank1.inlet[1].state.T,tank1.inlet[1].state.X[1],tank1.inlet[1].state.X[2],tank1.inlet[1].state.p,tank1.k_volume_damping,tank1.liquidDensity,tank1.m_flow_assert,tank1.m_flow_in[1],tank1.m_flow_out[1],tank1.medium.MM,tank1.medium.R_s,tank1.medium.T,tank1.medium.T_degC,tank1.medium.X[1],tank1.medium.X[2],tank1.medium.Xi[1],tank1.medium.Xi[2],tank1.medium.d,tank1.medium.h,tank1.medium.p,tank1.medium.p_bar,tank1.medium.preferredMediumStates,tank1.medium.standardOrderComponents,tank1.medium.state.T,tank1.medium.state.X[1],tank1.medium.state.X[2],tank1.medium.state.p,tank1.medium.u,tank1.normAcc[1],tank1.normAcc[2],tank1.normAcc[3],tank1.nx,tank1.nz,tank1.outletPositions[1,1],tank1.outletPositions[1,2],tank1.outletPositions[1,3],tank1.outletTransition,der(tank1.outlet[1].m_flow),tank1.outlet[1].m_flow,tank1.outlet[1].r,tank1.outlet[1].state.T,tank1.outlet[1].state.X[1],tank1.outlet[1].state.X[2],tank1.outlet[1].state.p,tank1.p_in[1],tank1.p_ref,tank1.p_start,tank1.r[1],tank1.r_damping,tank1.shiftOutlet[1],tank1.state_out[1].T,tank1.state_out[1].X[1],tank1.state_out[1].X[2],tank1.state_out[1].p,tank1.staticHeadInlets[1],tank1.staticHeadInlets_Pa_relative[1],tank1.staticHeadOutlets[1],tank1.staticHeadOutlets_Pa_relative[1],tank1.tankCenter[1],tank1.tankCenter[2],tank1.tankCenter[3],tank1.useHeatport,tank1.usePreferredMediumStates,tank1.use_hstart,tank1.xLength,tank1.yLength,tank1.zLength Variables in the result:$cse3.T,$cse3.p,$cse9.T,$cse9.p,acceleration.a[1],acceleration.a[2],acceleration.a[3],acceleration.ax,acceleration.ay,acceleration.az,acceleration.setFromInputs,der(flowResistance.inlet.m_flow),der(flowResistance1.inlet.m_flow),der(flowResistance3.inlet.m_flow),der(staticHead.inlet.m_flow),der(tank.M),der(tank.MXi[1]),der(tank.MXi[2]),der(tank.U_med),der(tank1.M),der(tank1.MXi[1]),der(tank1.MXi[2]),der(tank1.U_med),dropOfCommons.L,dropOfCommons.assertionLevel,dropOfCommons.g,dropOfCommons.k_volume_damping,dropOfCommons.m_flow_reg,dropOfCommons.omega_reg,dropOfCommons.p_min,dropOfCommons.rho_min,fixedHeatFlow.Q_flow,fixedHeatFlow.T_ref,fixedHeatFlow.alpha,fixedHeatFlow.port.Q_flow,fixedHeatFlow.port.T,flowResistance.D_h,flowResistance.L,flowResistance.L_value,flowResistance.Xi_in[1],flowResistance.Xi_in[2],flowResistance.Xi_out[1],flowResistance.Xi_out[2],flowResistance.a,flowResistance.areaCross,flowResistance.areaCrossInput,flowResistance.areaHydraulic,flowResistance.b,flowResistance.clip_p_out,flowResistance.dp,flowResistance.dp_ref_color,flowResistance.dr_corr,flowResistance.h_in,flowResistance.h_out,flowResistance.initM_flow,flowResistance.inlet.m_flow,flowResistance.inlet.r,flowResistance.inlet.state.T,flowResistance.inlet.state.X[1],flowResistance.inlet.state.X[2],flowResistance.inlet.state.p,flowResistance.l,flowResistance.m_acceleration_0,flowResistance.m_flow,flowResistance.m_flowStateSelect,flowResistance.m_flow_0,flowResistance.mu_in,flowResistance.outlet.m_flow,flowResistance.outlet.r,flowResistance.outlet.state.T,flowResistance.outlet.state.X[1],flowResistance.outlet.state.X[2],flowResistance.outlet.state.p,flowResistance.p_in,flowResistance.p_min,flowResistance.p_out,flowResistance.perimeter,flowResistance.perimeterInput,flowResistance.pressureDropSignificantDigits,flowResistance.r,flowResistance.rho_in,flowResistance.rho_min,flowResistance.shape,flowResistance1.D_h,flowResistance1.L,flowResistance1.L_value,flowResistance1.Xi_in[1],flowResistance1.Xi_in[2],flowResistance1.Xi_out[1],flowResistance1.Xi_out[2],flowResistance1.a,flowResistance1.areaCross,flowResistance1.areaCrossInput,flowResistance1.areaHydraulic,flowResistance1.b,flowResistance1.clip_p_out,flowResistance1.dp,flowResistance1.dp_ref_color,flowResistance1.dr_corr,flowResistance1.h_in,flowResistance1.h_out,flowResistance1.initM_flow,flowResistance1.inlet.m_flow,flowResistance1.inlet.r,flowResistance1.inlet.state.T,flowResistance1.inlet.state.X[1],flowResistance1.inlet.state.X[2],flowResistance1.inlet.state.p,flowResistance1.l,flowResistance1.m_acceleration_0,flowResistance1.m_flow,flowResistance1.m_flowStateSelect,flowResistance1.m_flow_0,flowResistance1.mu_in,flowResistance1.outlet.m_flow,flowResistance1.outlet.r,flowResistance1.outlet.state.T,flowResistance1.outlet.state.X[1],flowResistance1.outlet.state.X[2],flowResistance1.outlet.state.p,flowResistance1.p_in,flowResistance1.p_min,flowResistance1.p_out,flowResistance1.perimeter,flowResistance1.perimeterInput,flowResistance1.pressureDropSignificantDigits,flowResistance1.r,flowResistance1.rho_in,flowResistance1.rho_min,flowResistance1.shape,flowResistance2.D_h,flowResistance2.L,flowResistance2.L_value,flowResistance2.Xi_in[1],flowResistance2.Xi_in[2],flowResistance2.Xi_out[1],flowResistance2.Xi_out[2],flowResistance2.a,flowResistance2.areaCross,flowResistance2.areaCrossInput,flowResistance2.areaHydraulic,flowResistance2.b,flowResistance2.clip_p_out,flowResistance2.dp,flowResistance2.dp_ref_color,flowResistance2.dr_corr,flowResistance2.h_in,flowResistance2.h_out,flowResistance2.initM_flow,flowResistance2.inlet.m_flow,flowResistance2.inlet.r,flowResistance2.inlet.state.T,flowResistance2.inlet.state.X[1],flowResistance2.inlet.state.X[2],flowResistance2.inlet.state.p,flowResistance2.l,flowResistance2.m_acceleration_0,flowResistance2.m_flow,flowResistance2.m_flowStateSelect,flowResistance2.m_flow_0,flowResistance2.mu_in,flowResistance2.outlet.m_flow,flowResistance2.outlet.r,flowResistance2.outlet.state.T,flowResistance2.outlet.state.X[1],flowResistance2.outlet.state.X[2],flowResistance2.outlet.state.p,flowResistance2.p_in,flowResistance2.p_min,flowResistance2.p_out,flowResistance2.perimeter,flowResistance2.perimeterInput,flowResistance2.pressureDropSignificantDigits,flowResistance2.r,flowResistance2.rho_in,flowResistance2.rho_min,flowResistance2.shape,flowResistance3.D_h,flowResistance3.L,flowResistance3.L_value,flowResistance3.Xi_in[1],flowResistance3.Xi_in[2],flowResistance3.Xi_out[1],flowResistance3.Xi_out[2],flowResistance3.a,flowResistance3.areaCross,flowResistance3.areaCrossInput,flowResistance3.areaHydraulic,flowResistance3.b,flowResistance3.clip_p_out,flowResistance3.dp,flowResistance3.dp_ref_color,flowResistance3.dr_corr,flowResistance3.h_in,flowResistance3.h_out,flowResistance3.initM_flow,flowResistance3.inlet.m_flow,flowResistance3.inlet.r,flowResistance3.inlet.state.T,flowResistance3.inlet.state.X[1],flowResistance3.inlet.state.X[2],flowResistance3.inlet.state.p,flowResistance3.l,flowResistance3.m_acceleration_0,flowResistance3.m_flow,flowResistance3.m_flowStateSelect,flowResistance3.m_flow_0,flowResistance3.mu_in,flowResistance3.outlet.m_flow,flowResistance3.outlet.r,flowResistance3.outlet.state.T,flowResistance3.outlet.state.X[1],flowResistance3.outlet.state.X[2],flowResistance3.outlet.state.p,flowResistance3.p_in,flowResistance3.p_min,flowResistance3.p_out,flowResistance3.perimeter,flowResistance3.perimeterInput,flowResistance3.pressureDropSignificantDigits,flowResistance3.r,flowResistance3.rho_in,flowResistance3.rho_min,flowResistance3.shape,sink1.L,sink1.inlet.m_flow,sink1.inlet.r,sink1.inlet.state.T,sink1.inlet.state.X[1],sink1.inlet.state.X[2],sink1.inlet.state.p,sink1.p,sink1.p0,sink1.p0_par,sink1.r,source.L,source.T0,source.T0_par,source.Xi0[1],source.Xi0[2],source.Xi0_par[1],source.Xi0_par[2],source.h0,source.h0_par,source.outlet.m_flow,source.outlet.r,source.outlet.state.T,source.outlet.state.X[1],source.outlet.state.X[2],source.outlet.state.p,source.p0,source.p0_par,source1.L,source1.T0,source1.T0_par,source1.Xi0[1],source1.Xi0[2],source1.Xi0_par[1],source1.Xi0_par[2],source1.h0,source1.h0_par,source1.outlet.m_flow,source1.outlet.r,source1.outlet.state.T,source1.outlet.state.X[1],source1.outlet.state.X[2],source1.outlet.state.p,source1.p0,source1.p0_par,staticHead.L,staticHead.L_value,staticHead.Xi_in[1],staticHead.Xi_in[2],staticHead.Xi_out[1],staticHead.Xi_out[2],staticHead.clip_p_out,staticHead.displayPositions,staticHead.dp,staticHead.dr_corr,staticHead.fromPosition[1],staticHead.fromPosition[2],staticHead.fromPosition[3],staticHead.h_in,staticHead.h_out,staticHead.initM_flow,staticHead.inlet.m_flow,staticHead.inlet.r,staticHead.inlet.state.T,staticHead.inlet.state.X[1],staticHead.inlet.state.X[2],staticHead.inlet.state.p,staticHead.m_acceleration_0,staticHead.m_flow,staticHead.m_flowStateSelect,staticHead.m_flow_0,staticHead.outlet.m_flow,staticHead.outlet.r,staticHead.outlet.state.T,staticHead.outlet.state.X[1],staticHead.outlet.state.X[2],staticHead.outlet.state.p,staticHead.p_in,staticHead.p_min,staticHead.p_out,staticHead.rho_in,staticHead.rho_min,staticHead.staticHead,staticHead.staticHead_Pa_relative,staticHead.toPosition[1],staticHead.toPosition[2],staticHead.toPosition[3],tank.A,tank.Area,tank.AxLimit,tank.AzLimit,tank.D,tank.D1,tank.D2,tank.D3,tank.D4,tank.K,tank.L,tank.M,tank.MXi[1],tank.MXi[2],tank.M_liq_start,tank.M_outlets,tank.N_inlets,tank.Q_flow,tank.T_heatPort,tank.T_start,tank.ThresholdEmpty,tank.ThresholdFull,tank.U,tank.U_med,tank.V,tank.V_liquid,tank.V_ref,tank.W_v,tank.Xi_0[1],tank.Xi_0[2],tank.Xi_in[1,1],tank.Xi_in[1,2],tank.Xi_in[2,1],tank.Xi_in[2,2],tank.Xi_out[1,1],tank.Xi_out[2,1],tank.centerOfMass[1],tank.centerOfMass[2],tank.centerOfMass[3],tank.d,tank.density_derp_h,tank.eps_geometry,tank.fEmpty,tank.fFull,tank.gasDensity,tank.h_in[1],tank.h_in[2],tank.h_out[1],tank.h_start,tank.initialize_LiquidMass,tank.initialize_Xi,tank.initialize_energy,tank.initialize_pressure,tank.inletPositions[1,1],tank.inletPositions[1,2],tank.inletPositions[1,3],tank.inletPositions[2,1],tank.inletPositions[2,2],tank.inletPositions[2,3],tank.inlet[1].m_flow,tank.inlet[1].r,tank.inlet[1].state.T,tank.inlet[1].state.X[1],tank.inlet[1].state.X[2],tank.inlet[1].state.p,tank.inlet[2].m_flow,tank.inlet[2].r,tank.inlet[2].state.T,tank.inlet[2].state.X[1],tank.inlet[2].state.X[2],tank.inlet[2].state.p,tank.k_volume_damping,tank.liquidDensity,tank.m_flow_assert,tank.m_flow_in[1],tank.m_flow_in[2],tank.m_flow_out[1],tank.medium.MM,tank.medium.R_s,tank.medium.T,tank.medium.T_degC,tank.medium.X[1],tank.medium.X[2],tank.medium.Xi[1],tank.medium.Xi[2],tank.medium.d,tank.medium.h,tank.medium.p,tank.medium.p_bar,tank.medium.preferredMediumStates,tank.medium.standardOrderComponents,tank.medium.state.T,tank.medium.state.X[1],tank.medium.state.X[2],tank.medium.state.p,tank.medium.u,tank.normAcc[1],tank.normAcc[2],tank.normAcc[3],tank.nx,tank.nz,tank.outletPositions[1,1],tank.outletPositions[1,2],tank.outletPositions[1,3],tank.outletTransition,tank.outlet[1].m_flow,tank.outlet[1].r,tank.outlet[1].state.T,tank.outlet[1].state.X[1],tank.outlet[1].state.X[2],tank.outlet[1].state.p,tank.p_in[1],tank.p_in[2],tank.p_ref,tank.p_start,tank.r[1],tank.r[2],tank.r_damping,tank.shiftOutlet[1],tank.state_out[1].T,tank.state_out[1].X[1],tank.state_out[1].X[2],tank.state_out[1].p,tank.staticHeadInlets[1],tank.staticHeadInlets[2],tank.staticHeadInlets_Pa_relative[1],tank.staticHeadInlets_Pa_relative[2],tank.staticHeadOutlets[1],tank.staticHeadOutlets_Pa_relative[1],tank.tankCenter[1],tank.tankCenter[2],tank.tankCenter[3],tank.useHeatport,tank.usePreferredMediumStates,tank.use_hstart,tank.xLength,tank.yLength,tank.zLength,tank1.A,tank1.Area,tank1.AxLimit,tank1.AzLimit,tank1.D,tank1.D1,tank1.D2,tank1.D3,tank1.D4,tank1.K,tank1.L,tank1.M,tank1.MXi[1],tank1.MXi[2],tank1.M_liq_start,tank1.M_outlets,tank1.N_inlets,tank1.Q_flow,tank1.T_heatPort,tank1.T_start,tank1.ThresholdEmpty,tank1.ThresholdFull,tank1.U,tank1.U_med,tank1.V,tank1.V_liquid,tank1.V_ref,tank1.W_v,tank1.Xi_0[1],tank1.Xi_0[2],tank1.Xi_in[1,1],tank1.Xi_in[2,1],tank1.Xi_out[1,1],tank1.Xi_out[2,1],tank1.centerOfMass[1],tank1.centerOfMass[2],tank1.centerOfMass[3],tank1.d,tank1.density_derp_h,tank1.eps_geometry,tank1.fEmpty,tank1.fFull,tank1.gasDensity,tank1.h_in[1],tank1.h_out[1],tank1.h_start,tank1.heatPort.Q_flow,tank1.heatPort.T,tank1.initialize_LiquidMass,tank1.initialize_Xi,tank1.initialize_energy,tank1.initialize_pressure,tank1.inletPositions[1,1],tank1.inletPositions[1,2],tank1.inletPositions[1,3],tank1.inlet[1].m_flow,tank1.inlet[1].r,tank1.inlet[1].state.T,tank1.inlet[1].state.X[1],tank1.inlet[1].state.X[2],tank1.inlet[1].state.p,tank1.k_volume_damping,tank1.liquidDensity,tank1.m_flow_assert,tank1.m_flow_in[1],tank1.m_flow_out[1],tank1.medium.MM,tank1.medium.R_s,tank1.medium.T,tank1.medium.T_degC,tank1.medium.X[1],tank1.medium.X[2],tank1.medium.Xi[1],tank1.medium.Xi[2],tank1.medium.d,tank1.medium.h,tank1.medium.p,tank1.medium.p_bar,tank1.medium.preferredMediumStates,tank1.medium.standardOrderComponents,tank1.medium.state.T,tank1.medium.state.X[1],tank1.medium.state.X[2],tank1.medium.state.p,tank1.medium.u,tank1.normAcc[1],tank1.normAcc[2],tank1.normAcc[3],tank1.nx,tank1.nz,tank1.outletPositions[1,1],tank1.outletPositions[1,2],tank1.outletPositions[1,3],tank1.outletTransition,tank1.outlet[1].m_flow,tank1.outlet[1].r,tank1.outlet[1].state.T,tank1.outlet[1].state.X[1],tank1.outlet[1].state.X[2],tank1.outlet[1].state.p,tank1.p_in[1],tank1.p_ref,tank1.p_start,tank1.r[1],tank1.r_damping,tank1.shiftOutlet[1],tank1.state_out[1].T,tank1.state_out[1].X[1],tank1.state_out[1].X[2],tank1.state_out[1].p,tank1.staticHeadInlets[1],tank1.staticHeadInlets_Pa_relative[1],tank1.staticHeadOutlets[1],tank1.staticHeadOutlets_Pa_relative[1],tank1.tankCenter[1],tank1.tankCenter[2],tank1.tankCenter[3],tank1.useHeatport,tank1.usePreferredMediumStates,tank1.use_hstart,tank1.xLength,tank1.yLength,tank1.zLength,time filterSimulationResults("ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat", "/var/lib/jenkins/ws/OpenModelicaLibraryTestingWork/OpenModelicaLibraryTesting/files/ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating.diff.mat", vars={"tank1.inlet[1].state.X[1]", "tank1.der(MXi[1])", "tank1.Xi_in[1, 1]", "tank.state_out[1].X[1]", "tank.m_flow_in[1]", "tank.der(MXi[1])", "tank.Xi_out[1, 1]", "staticHead.inlet.state.X[1]", "staticHead.Xi_out[1]", "flowResistance2.inlet.state.X[1]", "flowResistance2.Xi_out[1]"}, removeDescription=false) [Timeout 660] "" [Timeout remaining time 660] filterSimulationResults("/mnt/ReferenceFiles/ThermofluidStream-main-regression/ReferenceData/ThermofluidStream.Boundaries.Tests.TankHeating_ref.mat", "/var/lib/jenkins/ws/OpenModelicaLibraryTestingWork/OpenModelicaLibraryTesting/files/ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating.diff.ref.mat", vars={"tank1.inlet[1].state.X[1]", "tank1.der(MXi[1])", "tank1.Xi_in[1, 1]", "tank.state_out[1].X[1]", "tank.m_flow_in[1]", "tank.der(MXi[1])", "tank.Xi_out[1, 1]", "staticHead.inlet.state.X[1]", "staticHead.Xi_out[1]", "flowResistance2.inlet.state.X[1]", "flowResistance2.Xi_out[1]"}, removeDescription=false) [Timeout 660] "" [Timeout remaining time 660] [Calling sys.exit(0), Time elapsed: 5.623051593080163]