Running: ./testmodel.py --libraries=/home/hudson/saved_omc/libraries/.openmodelica/libraries --ompython_omhome=/usr ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankFillingClosedTank.conf.json
loadFile("/home/hudson/saved_omc/libraries/.openmodelica/libraries/ModelicaServices 4.1.0+maint.om/package.mo", uses=false) [Timeout 180]
"[<interactive>:1:22-1:33:writable] Warning: Modelica only supports 32-bit signed integers! Transforming: 13743895347 into a real
[<interactive>:1:1-1:33:writable] Error: Class GC_set_max_heap_size not found in scope <global scope> (looking for a function or record).
Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/ModelicaServices 4.1.0+maint.om/package.mo): time 0.0005611/0.0005611, allocations: 0 / 0, free: 0 / 0
"
[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 0.0006861/0.0006861, allocations: 0 / 0, free: 0 / 0
"
[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 0.4307/0.4307, allocations: 0 / 0, free: 0 / 0
"
[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 0.2754/0.2754, allocations: 0 / 0, free: 0 / 0
"
[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: simulate(ThermofluidStream.Boundaries.Tests.TankFillingClosedTank,startTime=0,stopTime=20,tolerance=1e-06,numberOfIntervals=2500,outputFormat="mat",variableFilter="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|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|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|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.|staticHead1.L|staticHead1.L_value|staticHead1.Xi_in.1.|staticHead1.Xi_in.2.|staticHead1.Xi_out.1.|staticHead1.Xi_out.2.|staticHead1.clip_p_out|staticHead1.displayPositions|staticHead1.dp|staticHead1.dr_corr|staticHead1.fromPosition.1.|staticHead1.fromPosition.2.|staticHead1.fromPosition.3.|staticHead1.h_in|staticHead1.h_out|staticHead1.initM_flow|der.staticHead1.inlet.m_flow.|staticHead1.inlet.m_flow|staticHead1.inlet.r|staticHead1.inlet.state.T|staticHead1.inlet.state.X.1.|staticHead1.inlet.state.X.2.|staticHead1.inlet.state.p|staticHead1.m_acceleration_0|staticHead1.m_flow|staticHead1.m_flowStateSelect|staticHead1.m_flow_0|staticHead1.outlet.m_flow|staticHead1.outlet.r|staticHead1.outlet.state.T|staticHead1.outlet.state.X.1.|staticHead1.outlet.state.X.2.|staticHead1.outlet.state.p|staticHead1.p_in|staticHead1.p_min|staticHead1.p_out|staticHead1.rho_in|staticHead1.rho_min|staticHead1.staticHead|staticHead1.staticHead_Pa_relative|staticHead1.toPosition.1.|staticHead1.toPosition.2.|staticHead1.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.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",fileNamePrefix="ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankFillingClosedTank",simflags="-alarm=1200  -emit_protected -lv LOG_STATS")
simulate(ThermofluidStream.Boundaries.Tests.TankFillingClosedTank,startTime=0,stopTime=20,tolerance=1e-06,numberOfIntervals=2500,outputFormat="mat",variableFilter="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|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|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|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.|staticHead1.L|staticHead1.L_value|staticHead1.Xi_in.1.|staticHead1.Xi_in.2.|staticHead1.Xi_out.1.|staticHead1.Xi_out.2.|staticHead1.clip_p_out|staticHead1.displayPositions|staticHead1.dp|staticHead1.dr_corr|staticHead1.fromPosition.1.|staticHead1.fromPosition.2.|staticHead1.fromPosition.3.|staticHead1.h_in|staticHead1.h_out|staticHead1.initM_flow|der.staticHead1.inlet.m_flow.|staticHead1.inlet.m_flow|staticHead1.inlet.r|staticHead1.inlet.state.T|staticHead1.inlet.state.X.1.|staticHead1.inlet.state.X.2.|staticHead1.inlet.state.p|staticHead1.m_acceleration_0|staticHead1.m_flow|staticHead1.m_flowStateSelect|staticHead1.m_flow_0|staticHead1.outlet.m_flow|staticHead1.outlet.r|staticHead1.outlet.state.T|staticHead1.outlet.state.X.1.|staticHead1.outlet.state.X.2.|staticHead1.outlet.state.p|staticHead1.p_in|staticHead1.p_min|staticHead1.p_out|staticHead1.rho_in|staticHead1.rho_min|staticHead1.staticHead|staticHead1.staticHead_Pa_relative|staticHead1.toPosition.1.|staticHead1.toPosition.2.|staticHead1.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.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",fileNamePrefix="ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankFillingClosedTank",simflags="-alarm=1200  -emit_protected -lv LOG_STATS") [Timeout 1860]
"Notification: Performance of FrontEnd - loaded program: time 1.072e-06/1.072e-06, allocations: 0 / 0, free: 0 / 0
Notification: Performance of FrontEnd - Absyn->SCode: time 3.405e-05/3.513e-05, allocations: 0 / 0, free: 0 / 0
Notification: Performance of NFInst.instantiate(ThermofluidStream.Boundaries.Tests.TankFillingClosedTank): time 0.6743/0.6744, allocations: 0 / 0, free: 0 / 0
Notification: Performance of NFInst.instExpressions: time 0.02336/0.6977, allocations: 0 / 0, free: 0 / 0
Notification: Performance of NFInst.updateImplicitVariability: time 0.002254/0.7, allocations: 0 / 0, free: 0 / 0
Notification: Performance of NFTyping.typeComponents: time 0.005338/0.7053, allocations: 0 / 0, free: 0 / 0
Notification: Performance of NFTyping.typeBindings: time 0.02312/0.7284, allocations: 0 / 0, free: 0 / 0
Notification: Performance of NFTyping.typeClassSections: time 0.0129/0.7413, allocations: 0 / 0, free: 0 / 0
Notification: Performance of NFFlatten.flatten: time 0.007182/0.7485, allocations: 0 / 0, free: 0 / 0
Notification: Performance of NFFlatten.resolveConnections: time 0.00102/0.7495, allocations: 0 / 0, free: 0 / 0
Notification: Performance of NFEvalConstants.evaluate: time 0.01319/0.7627, allocations: 0 / 0, free: 0 / 0
Notification: Performance of NFSimplifyModel.simplify: time 0.0053/0.768, allocations: 0 / 0, free: 0 / 0
Notification: Performance of NFPackage.collectConstants: time 0.0009505/0.769, allocations: 0 / 0, free: 0 / 0
Notification: Performance of NFFlatten.collectFunctions: time 0.03233/0.8013, allocations: 0 / 0, free: 0 / 0
Notification: Performance of NFScalarize.scalarize: time 0.003037/0.8043, allocations: 0 / 0, free: 0 / 0
Notification: Performance of NFVerifyModel.verify: time 0.003613/0.8079, allocations: 0 / 0, free: 0 / 0
Notification: Performance of NFConvertDAE.convert: time 0.02343/0.8314, allocations: 0 / 0, free: 0 / 0
Notification: Performance of FrontEnd - DAE generated: time 0.001439/0.8328, allocations: 0 / 0, free: 0 / 0
Notification: Performance of FrontEnd: time 5.44e-06/0.8328, allocations: 0 / 0, free: 0 / 0
Notification: Performance of Transformations before backend: time 9.166e-05/0.8329, allocations: 0 / 0, free: 0 / 0
Notification: Model statistics after passing the front-end and creating the data structures used by the back-end:
 * Number of equations: 326
 * Number of variables: 326
Notification: Performance of Generate backend data structure: time 0.02634/0.8593, allocations: 0 / 0, free: 0 / 0
Notification: Performance of prepare preOptimizeDAE: time 0.0004314/0.8597, allocations: 0 / 0, free: 0 / 0
Notification: Performance of preOpt normalInlineFunction (simulation): time 0.01097/0.8707, allocations: 0 / 0, free: 0 / 0
Notification: Performance of preOpt evaluateParameters (simulation): time 0.008007/0.8787, allocations: 0 / 0, free: 0 / 0
Notification: Performance of preOpt simplifyIfEquations (simulation): time 0.002037/0.8807, allocations: 0 / 0, free: 0 / 0
Notification: Performance of preOpt expandDerOperator (simulation): time 0.001255/0.882, allocations: 0 / 0, free: 0 / 0
Notification: Performance of preOpt clockPartitioning (simulation): time 0.0183/0.9003, allocations: 0 / 0, free: 0 / 0
Notification: Performance of preOpt findStateOrder (simulation): time 8.216e-05/0.9003, allocations: 0 / 0, free: 0 / 0
Notification: Performance of preOpt replaceEdgeChange (simulation): time 0.0007576/0.9011, allocations: 0 / 0, free: 0 / 0
Notification: Performance of preOpt inlineArrayEqn (simulation): time 0.001232/0.9023, allocations: 0 / 0, free: 0 / 0
Notification: Performance of preOpt removeEqualRHS (simulation): time 0.02014/0.9225, allocations: 0 / 0, free: 0 / 0
Notification: Performance of preOpt removeSimpleEquations (simulation): time 0.04539/0.9679, allocations: 0 / 0, free: 0 / 0
Notification: Performance of preOpt comSubExp (simulation): time 0.01232/0.9802, allocations: 0 / 0, free: 0 / 0
Notification: Performance of preOpt resolveLoops (simulation): time 0.008684/0.9889, allocations: 0 / 0, free: 0 / 0
Notification: Performance of preOpt evalFunc (simulation): time 0.002304/0.9912, allocations: 0 / 0, free: 0 / 0
Notification: Performance of preOpt encapsulateWhenConditions (simulation): time 0.0001641/0.9913, allocations: 0 / 0, free: 0 / 0
Notification: Performance of pre-optimization done (n=178): time 0.0004398/0.9918, allocations: 0 / 0, free: 0 / 0
Notification: Performance of matching and sorting (n=178): time 0.03362/1.025, allocations: 0 / 0, free: 0 / 0
Notification: Performance of inlineWhenForInitialization (initialization): time 0.0001574/1.026, allocations: 0 / 0, free: 0 / 0
Notification: Performance of selectInitializationVariablesDAE (initialization): time 0.004312/1.03, allocations: 0 / 0, free: 0 / 0
Notification: Performance of collectPreVariables (initialization): time 0.001511/1.031, allocations: 0 / 0, free: 0 / 0
Notification: Performance of collectInitialEqns (initialization): time 0.001221/1.033, allocations: 0 / 0, free: 0 / 0
Notification: Performance of collectInitialBindings (initialization): time 0.001578/1.034, allocations: 0 / 0, free: 0 / 0
Notification: Performance of simplifyInitialFunctions (initialization): time 0.003524/1.038, allocations: 0 / 0, free: 0 / 0
Notification: Performance of setup shared object (initialization): time 0.0002086/1.038, allocations: 0 / 0, free: 0 / 0
Notification: Performance of preBalanceInitialSystem (initialization): time 0.008354/1.046, allocations: 0 / 0, free: 0 / 0
Notification: Performance of partitionIndependentBlocks (initialization): time 0.009966/1.056, allocations: 0 / 0, free: 0 / 0
Notification: Performance of analyzeInitialSystem (initialization): time 0.1609/1.217, allocations: 0 / 0, free: 0 / 0
Notification: Performance of solveInitialSystemEqSystem (initialization): time 3.33e-05/1.217, allocations: 0 / 0, free: 0 / 0
Notification: Performance of matching and sorting (n=200) (initialization): time 0.02452/1.242, allocations: 0 / 0, free: 0 / 0
Notification: Performance of prepare postOptimizeDAE: time 7.667e-05/1.242, allocations: 0 / 0, free: 0 / 0
Notification: Performance of postOpt simplifyComplexFunction (initialization): time 3.288e-05/1.242, allocations: 0 / 0, free: 0 / 0
Notification: Performance of postOpt tearingSystem (initialization): time 0.0015/1.243, allocations: 0 / 0, free: 0 / 0
Notification: Performance of postOpt solveSimpleEquations (initialization): time 0.004659/1.248, allocations: 0 / 0, free: 0 / 0
Notification: Performance of postOpt calculateStrongComponentJacobians (initialization): time 0.01213/1.26, allocations: 0 / 0, free: 0 / 0
Notification: Performance of postOpt simplifyAllExpressions (initialization): time 0.004522/1.265, allocations: 0 / 0, free: 0 / 0
Notification: Performance of postOpt collapseArrayExpressions (initialization): time 0.001208/1.266, allocations: 0 / 0, free: 0 / 0
Warning: Assuming fixed start value for the following 3 variables:
         staticHead1.inlet.m_flow:VARIABLE(flow=true min = -1e5 max = 1e5 unit = \"kg/s\" fixed = true )  \"Mass flow rate\" type: Real
         staticHead.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 (174):
 * Single equations (assignments): 161
 * Array equations: 7
 * Algorithm blocks: 0
 * Record equations: 3
 * When equations: 0
 * If-equations: 0
 * Equation systems (not torn): 0
 * Torn equation systems: 3
 * Mixed (continuous/discrete) equation systems: 0
Notification: Torn system details for strict tearing set:
 * Linear torn systems (#iteration vars, #inner vars, density): 3 systems
   {(1,3,100.0%), (1,2,100.0%), (1,3,100.0%)}
 * Non-linear torn systems (#iteration vars, #inner vars): 0 systems
Notification: Performance of prepare postOptimizeDAE: time 0.004095/1.27, allocations: 0 / 0, free: 0 / 0
Notification: Performance of postOpt lateInlineFunction (simulation): time 0.002438/1.272, allocations: 0 / 0, free: 0 / 0
Notification: Performance of postOpt wrapFunctionCalls (simulation): time 0.02903/1.301, allocations: 0 / 0, free: 0 / 0
Notification: Performance of postOpt inlineArrayEqn (simulation): time 0.02189/1.323, allocations: 0 / 0, free: 0 / 0
Notification: Performance of postOpt constantLinearSystem (simulation): time 3.064e-05/1.323, allocations: 0 / 0, free: 0 / 0
Notification: Performance of postOpt simplifysemiLinear (simulation): time 5.004e-05/1.323, allocations: 0 / 0, free: 0 / 0
Notification: Performance of postOpt removeSimpleEquations (simulation): time 0.03964/1.363, allocations: 0 / 0, free: 0 / 0
Notification: Performance of postOpt simplifyComplexFunction (simulation): time 3.025e-05/1.363, allocations: 0 / 0, free: 0 / 0
Notification: Performance of postOpt solveSimpleEquations (simulation): time 0.004495/1.367, allocations: 0 / 0, free: 0 / 0
Notification: Performance of postOpt tearingSystem (simulation): time 0.005841/1.373, allocations: 0 / 0, free: 0 / 0
Notification: Performance of postOpt inputDerivativesUsed (simulation): time 0.001248/1.375, allocations: 0 / 0, free: 0 / 0
Notification: Performance of postOpt calculateStrongComponentJacobians (simulation): time 0.01496/1.39, allocations: 0 / 0, free: 0 / 0
Notification: Performance of postOpt calculateStateSetsJacobians (simulation): time 5.049e-06/1.39, allocations: 0 / 0, free: 0 / 0
Notification: Performance of postOpt symbolicJacobian (simulation): time 0.03397/1.424, allocations: 0 / 0, free: 0 / 0
Notification: Performance of postOpt removeConstants (simulation): time 0.005014/1.429, allocations: 0 / 0, free: 0 / 0
Notification: Performance of postOpt simplifyTimeIndepFuncCalls (simulation): time 0.001377/1.43, allocations: 0 / 0, free: 0 / 0
Notification: Performance of postOpt simplifyAllExpressions (simulation): time 0.003431/1.433, allocations: 0 / 0, free: 0 / 0
Notification: Performance of postOpt findZeroCrossings (simulation): time 0.003616/1.437, allocations: 0 / 0, free: 0 / 0
Notification: Performance of postOpt collapseArrayExpressions (simulation): time 0.001175/1.438, allocations: 0 / 0, free: 0 / 0
Notification: Performance of sorting global known variables: time 0.002977/1.441, allocations: 0 / 0, free: 0 / 0
Notification: Performance of sort global known variables: time 8.029e-05/1.441, allocations: 0 / 0, free: 0 / 0
Notification: Performance of remove unused functions: time 0.009143/1.45, allocations: 0 / 0, free: 0 / 0
Notification: Model statistics after passing the back-end for simulation:
 * Number of independent subsystems: 1
 * Number of states: 11 (tank.M,tank.MXi[1],tank.MXi[2],tank.U_med,flowResistance.inlet.m_flow,tank1.M,tank1.MXi[1],tank1.MXi[2],tank1.U_med,staticHead.inlet.m_flow,staticHead1.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 (168):
 * Single equations (assignments): 152
 * 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): 3 systems
   {(1,2,100.0%), (1,3,100.0%), (1,3,100.0%)}
 * 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 0.01059/1.461, allocations: 0 / 0, free: 0 / 0
Notification: Performance of simCode: created initialization part: time 0.02078/1.482, allocations: 0 / 0, free: 0 / 0
Notification: Performance of simCode: created event and clocks part: time 1.658e-05/1.482, allocations: 0 / 0, free: 0 / 0
Notification: Performance of simCode: created simulation system equations: time 0.01188/1.494, allocations: 0 / 0, free: 0 / 0
Notification: Performance of simCode: created of all other equations (e.g. parameter, nominal, assert, etc): time 0.009383/1.503, allocations: 0 / 0, free: 0 / 0
Notification: Performance of simCode: created linear, non-linear and system jacobian parts: time 0.02432/1.527, allocations: 0 / 0, free: 0 / 0
Notification: Performance of simCode: some other stuff during SimCode phase: time 0.003287/1.531, allocations: 0 / 0, free: 0 / 0
Notification: Performance of simCode: alias equations: time 0.005438/1.536, allocations: 0 / 0, free: 0 / 0
Notification: Performance of simCode: all other stuff during SimCode phase: time 0.006485/1.543, allocations: 0 / 0, free: 0 / 0
Notification: Performance of SimCode: time 0.002083/1.545, allocations: 0 / 0, free: 0 / 0
Notification: Performance of Templates: time 0.03383/1.578, allocations: 0 / 0, free: 0 / 0
"
[Timeout remaining time 1858]
diffSimulationResults("ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankFillingClosedTank_res.mat","/mnt/ReferenceFiles/ThermofluidStream-main-regression/ReferenceData/ThermofluidStream.Boundaries.Tests.TankFillingClosedTank_ref.mat","/var/lib/jenkins/ws/OpenModelicaLibraryTestingWork/OpenModelicaLibraryTesting/files/ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankFillingClosedTank.diff",relTol=0.003,relTolDiffMinMax=0.003,rangeDelta=0.001) [Timeout 660]
"Error: Could not read variable CPUtime in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankFillingClosedTank_res.mat.
Warning: Get data of variable CPUtime from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankFillingClosedTank_res.mat failed!
Error: Could not read variable EventCounter in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankFillingClosedTank_res.mat.
Warning: Get data of variable EventCounter from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankFillingClosedTank_res.mat failed!
Error: Could not read variable NonlinearSystems.simulation[1].Calls in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankFillingClosedTank_res.mat.
Warning: Get data of variable NonlinearSystems.simulation[1].Calls from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankFillingClosedTank_res.mat failed!
Error: Could not read variable NonlinearSystems.simulation[1].Iterations in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankFillingClosedTank_res.mat.
Warning: Get data of variable NonlinearSystems.simulation[1].Iterations from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankFillingClosedTank_res.mat failed!
Error: Could not read variable NonlinearSystems.simulation[1].Jacobians in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankFillingClosedTank_res.mat.
Warning: Get data of variable NonlinearSystems.simulation[1].Jacobians from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankFillingClosedTank_res.mat failed!
Error: Could not read variable NonlinearSystems.simulation[1].Residues in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankFillingClosedTank_res.mat.
Warning: Get data of variable NonlinearSystems.simulation[1].Residues from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankFillingClosedTank_res.mat failed!
Error: Could not read variable NonlinearSystems.simulation[2].Calls in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankFillingClosedTank_res.mat.
Warning: Get data of variable NonlinearSystems.simulation[2].Calls from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankFillingClosedTank_res.mat failed!
Error: Could not read variable NonlinearSystems.simulation[2].Iterations in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankFillingClosedTank_res.mat.
Warning: Get data of variable NonlinearSystems.simulation[2].Iterations from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankFillingClosedTank_res.mat failed!
Error: Could not read variable NonlinearSystems.simulation[2].Jacobians in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankFillingClosedTank_res.mat.
Warning: Get data of variable NonlinearSystems.simulation[2].Jacobians from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankFillingClosedTank_res.mat failed!
Error: Could not read variable NonlinearSystems.simulation[2].Residues in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankFillingClosedTank_res.mat.
Warning: Get data of variable NonlinearSystems.simulation[2].Residues from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankFillingClosedTank_res.mat failed!
Error: Could not read variable _GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.H0 in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankFillingClosedTank_res.mat.
Warning: Get data of variable _GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.H0 from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankFillingClosedTank_res.mat failed!
Error: Could not read variable _GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.Hf in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankFillingClosedTank_res.mat.
Warning: Get data of variable _GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.Hf from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankFillingClosedTank_res.mat failed!
Error: Could not read variable _GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.MM in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankFillingClosedTank_res.mat.
Warning: Get data of variable _GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.MM from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankFillingClosedTank_res.mat failed!
Error: Could not read variable _GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.R_s in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankFillingClosedTank_res.mat.
Warning: Get data of variable _GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.R_s from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankFillingClosedTank_res.mat failed!
Error: Could not read variable _GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.Tlimit in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankFillingClosedTank_res.mat.
Warning: Get data of variable _GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.Tlimit from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankFillingClosedTank_res.mat failed!
Error: Could not read variable _GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.ahigh[1] in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankFillingClosedTank_res.mat.
Warning: Get data of variable _GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.ahigh[1] from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankFillingClosedTank_res.mat failed!
Error: Could not read variable _GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.ahigh[2] in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankFillingClosedTank_res.mat.
Warning: Get data of variable _GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.ahigh[2] from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankFillingClosedTank_res.mat failed!
Error: Could not read variable _GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.ahigh[3] in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankFillingClosedTank_res.mat.
Warning: Get data of variable _GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.ahigh[3] from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankFillingClosedTank_res.mat failed!
Error: Could not read variable _GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.ahigh[4] in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankFillingClosedTank_res.mat.
Warning: Get data of variable _GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.ahigh[4] from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankFillingClosedTank_res.mat failed!
Error: Could not read variable _GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.ahigh[5] in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankFillingClosedTank_res.mat.
Warning: Get data of variable _GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.ahigh[5] from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankFillingClosedTank_res.mat failed!
Error: Could not read variable _GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.ahigh[6] in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankFillingClosedTank_res.mat.
Warning: Get data of variable _GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.ahigh[6] from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankFillingClosedTank_res.mat failed!
Error: Could not read variable _GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.ahigh[7] in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankFillingClosedTank_res.mat.
Warning: Get data of variable _GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.ahigh[7] from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankFillingClosedTank_res.mat failed!
Error: Could not read variable _GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.alow[1] in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankFillingClosedTank_res.mat.
Warning: Get data of variable _GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.alow[1] from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankFillingClosedTank_res.mat failed!
Error: Could not read variable _GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.alow[2] in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankFillingClosedTank_res.mat.
Warning: Get data of variable _GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.alow[2] from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankFillingClosedTank_res.mat failed!
Error: Could not read variable _GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.alow[3] in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankFillingClosedTank_res.mat.
Warning: Get data of variable _GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.alow[3] from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankFillingClosedTank_res.mat failed!
Error: Could not read variable _GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.alow[4] in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankFillingClosedTank_res.mat.
Warning: Get data of variable _GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.alow[4] from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankFillingClosedTank_res.mat failed!
Error: Could not read variable _GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.alow[5] in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankFillingClosedTank_res.mat.
Warning: Get data of variable _GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.alow[5] from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankFillingClosedTank_res.mat failed!
Error: Could not read variable _GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.alow[6] in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankFillingClosedTank_res.mat.
Warning: Get data of variable _GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.alow[6] from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankFillingClosedTank_res.mat failed!
Error: Could not read variable _GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.alow[7] in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankFillingClosedTank_res.mat.
Warning: Get data of variable _GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.alow[7] from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankFillingClosedTank_res.mat failed!
Error: Could not read variable _GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.bhigh[1] in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankFillingClosedTank_res.mat.
Warning: Get data of variable _GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.bhigh[1] from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankFillingClosedTank_res.mat failed!
Error: Could not read variable _GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.bhigh[2] in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankFillingClosedTank_res.mat.
Warning: Get data of variable _GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.bhigh[2] from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankFillingClosedTank_res.mat failed!
Error: Could not read variable _GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.blow[1] in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankFillingClosedTank_res.mat.
Warning: Get data of variable _GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.blow[1] from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankFillingClosedTank_res.mat failed!
Error: Could not read variable _GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.blow[2] in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankFillingClosedTank_res.mat.
Warning: Get data of variable _GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.blow[2] from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankFillingClosedTank_res.mat failed!
Error: Could not read variable _GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.H0 in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankFillingClosedTank_res.mat.
Warning: Get data of variable _GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.H0 from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankFillingClosedTank_res.mat failed!
Error: Could not read variable _GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.Hf in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankFillingClosedTank_res.mat.
Warning: Get data of variable _GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.Hf from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankFillingClosedTank_res.mat failed!
Error: Could not read variable _GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.MM in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankFillingClosedTank_res.mat.
Warning: Get data of variable _GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.MM from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankFillingClosedTank_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.TankFillingClosedTank_res.mat.
Warning: Get data of variable _GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.R_s from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankFillingClosedTank_res.mat failed!
Error: Could not read variable _GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.Tlimit in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankFillingClosedTank_res.mat.
Warning: Get data of variable _GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.Tlimit from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankFillingClosedTank_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.TankFillingClosedTank_res.mat.
Warning: Get data of variable _GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.ahigh[1] from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankFillingClosedTank_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.TankFillingClosedTank_res.mat.
Warning: Get data of variable _GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.ahigh[2] from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankFillingClosedTank_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.TankFillingClosedTank_res.mat.
Warning: Get data of variable _GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.ahigh[3] from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankFillingClosedTank_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.TankFillingClosedTank_res.mat.
Warning: Get data of variable _GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.ahigh[4] from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankFillingClosedTank_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.TankFillingClosedTank_res.mat.
Warning: Get data of variable _GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.ahigh[5] from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankFillingClosedTank_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.TankFillingClosedTank_res.mat.
Warning: Get data of variable _GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.ahigh[6] from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankFillingClosedTank_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.TankFillingClosedTank_res.mat.
Warning: Get data of variable _GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.ahigh[7] from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankFillingClosedTank_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.TankFillingClosedTank_res.mat.
Warning: Get data of variable _GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.alow[1] from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankFillingClosedTank_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.TankFillingClosedTank_res.mat.
Warning: Get data of variable _GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.alow[2] from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankFillingClosedTank_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.TankFillingClosedTank_res.mat.
Warning: Get data of variable _GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.alow[3] from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankFillingClosedTank_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.TankFillingClosedTank_res.mat.
Warning: Get data of variable _GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.alow[4] from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankFillingClosedTank_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.TankFillingClosedTank_res.mat.
Warning: Get data of variable _GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.alow[5] from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankFillingClosedTank_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.TankFillingClosedTank_res.mat.
Warning: Get data of variable _GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.alow[6] from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankFillingClosedTank_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.TankFillingClosedTank_res.mat.
Warning: Get data of variable _GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.alow[7] from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankFillingClosedTank_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.TankFillingClosedTank_res.mat.
Warning: Get data of variable _GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.bhigh[1] from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankFillingClosedTank_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.TankFillingClosedTank_res.mat.
Warning: Get data of variable _GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.bhigh[2] from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankFillingClosedTank_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.TankFillingClosedTank_res.mat.
Warning: Get data of variable _GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.blow[1] from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankFillingClosedTank_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.TankFillingClosedTank_res.mat.
Warning: Get data of variable _GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.blow[2] from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankFillingClosedTank_res.mat failed!
Error: Could not read variable tank.inlet[1].der(m_flow) in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankFillingClosedTank_res.mat.
Warning: Get data of variable tank.inlet[1].der(m_flow) from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankFillingClosedTank_res.mat failed!
Error: Could not read variable tank.inlet[2].der(m_flow) in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankFillingClosedTank_res.mat.
Warning: Get data of variable tank.inlet[2].der(m_flow) from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankFillingClosedTank_res.mat failed!
Error: Could not read variable tank.outlet[1].der(m_flow) in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankFillingClosedTank_res.mat.
Warning: Get data of variable tank.outlet[1].der(m_flow) from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankFillingClosedTank_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,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,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,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],staticHead1.L,staticHead1.L_value,staticHead1.Xi_in[1],staticHead1.Xi_in[2],staticHead1.Xi_out[1],staticHead1.Xi_out[2],staticHead1.clip_p_out,staticHead1.displayPositions,staticHead1.dp,staticHead1.dr_corr,staticHead1.fromPosition[1],staticHead1.fromPosition[2],staticHead1.fromPosition[3],staticHead1.h_in,staticHead1.h_out,staticHead1.initM_flow,der(staticHead1.inlet.m_flow),staticHead1.inlet.m_flow,staticHead1.inlet.r,staticHead1.inlet.state.T,staticHead1.inlet.state.X[1],staticHead1.inlet.state.X[2],staticHead1.inlet.state.p,staticHead1.m_acceleration_0,staticHead1.m_flow,staticHead1.m_flowStateSelect,staticHead1.m_flow_0,staticHead1.outlet.m_flow,staticHead1.outlet.r,staticHead1.outlet.state.T,staticHead1.outlet.state.X[1],staticHead1.outlet.state.X[2],staticHead1.outlet.state.p,staticHead1.p_in,staticHead1.p_min,staticHead1.p_out,staticHead1.rho_in,staticHead1.rho_min,staticHead1.staticHead,staticHead1.staticHead_Pa_relative,staticHead1.toPosition[1],staticHead1.toPosition[2],staticHead1.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.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:acceleration.a[1],acceleration.a[2],acceleration.a[3],acceleration.ax,acceleration.ay,acceleration.az,acceleration.setFromInputs,der(flowResistance.inlet.m_flow),der(staticHead.inlet.m_flow),der(staticHead1.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.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,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,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,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],staticHead1.L,staticHead1.L_value,staticHead1.Xi_in[1],staticHead1.Xi_in[2],staticHead1.Xi_out[1],staticHead1.Xi_out[2],staticHead1.clip_p_out,staticHead1.displayPositions,staticHead1.dp,staticHead1.dr_corr,staticHead1.fromPosition[1],staticHead1.fromPosition[2],staticHead1.fromPosition[3],staticHead1.h_in,staticHead1.h_out,staticHead1.initM_flow,staticHead1.inlet.m_flow,staticHead1.inlet.r,staticHead1.inlet.state.T,staticHead1.inlet.state.X[1],staticHead1.inlet.state.X[2],staticHead1.inlet.state.p,staticHead1.m_acceleration_0,staticHead1.m_flow,staticHead1.m_flowStateSelect,staticHead1.m_flow_0,staticHead1.outlet.m_flow,staticHead1.outlet.r,staticHead1.outlet.state.T,staticHead1.outlet.state.X[1],staticHead1.outlet.state.X[2],staticHead1.outlet.state.p,staticHead1.p_in,staticHead1.p_min,staticHead1.p_out,staticHead1.rho_in,staticHead1.rho_min,staticHead1.staticHead,staticHead1.staticHead_Pa_relative,staticHead1.toPosition[1],staticHead1.toPosition[2],staticHead1.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.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
[Calling sys.exit(0), Time elapsed: 3.9295748559998174]