Running: ./testmodel.py --libraries=/home/hudson/saved_omc/libraries/.openmodelica/libraries --ompython_omhome=/usr ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankOverfilling.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 0.0004078/0.0004078, 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 0.0005252/0.0005252, 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 0.4181/0.4181, 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 0.2689/0.2689, 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.TankOverfilling,startTime=0,stopTime=1000,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|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|checkValve.L|checkValve.Xi_in.1.|checkValve.Xi_in.2.|checkValve.Xi_out.1.|checkValve.Xi_out.2.|checkValve.clip_p_out|checkValve.dp|checkValve.dr_corr|checkValve.h_in|checkValve.h_out|checkValve.initM_flow|der.checkValve.inlet.m_flow.|checkValve.inlet.m_flow|checkValve.inlet.r|checkValve.inlet.state.T|checkValve.inlet.state.X.1.|checkValve.inlet.state.X.2.|checkValve.inlet.state.p|checkValve.m_acceleration_0|checkValve.m_flow|checkValve.m_flowStateSelect|checkValve.m_flow_0|checkValve.m_flow_ref|checkValve.outlet.m_flow|checkValve.outlet.r|checkValve.outlet.state.T|checkValve.outlet.state.X.1.|checkValve.outlet.state.X.2.|checkValve.outlet.state.p|checkValve.p_in|checkValve.p_min|checkValve.p_out|checkValve.p_ref|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|flowResistance2.D_h|flowResistance2.L|flowResistance2.L_value|flowResistance2.Xi_in.1.|flowResistance2.Xi_in.2.|flowResistance2.Xi_out.1.|flowResistance2.Xi_out.2.|flowResistance2.a|flowResistance2.areaCross|flowResistance2.areaCrossInput|flowResistance2.areaHydraulic|flowResistance2.b|flowResistance2.clip_p_out|flowResistance2.dp|flowResistance2.dr_corr|flowResistance2.h_in|flowResistance2.h_out|flowResistance2.initM_flow|der.flowResistance2.inlet.m_flow.|flowResistance2.inlet.m_flow|flowResistance2.inlet.r|flowResistance2.inlet.state.T|flowResistance2.inlet.state.X.1.|flowResistance2.inlet.state.X.2.|flowResistance2.inlet.state.p|flowResistance2.l|flowResistance2.m_acceleration_0|flowResistance2.m_flow|flowResistance2.m_flowStateSelect|flowResistance2.m_flow_0|flowResistance2.mu_in|flowResistance2.outlet.m_flow|flowResistance2.outlet.r|flowResistance2.outlet.state.T|flowResistance2.outlet.state.X.1.|flowResistance2.outlet.state.X.2.|flowResistance2.outlet.state.p|flowResistance2.p_in|flowResistance2.p_min|flowResistance2.p_out|flowResistance2.perimeter|flowResistance2.perimeterInput|flowResistance2.r|flowResistance2.rho_in|flowResistance2.rho_min|flowResistance2.shape|flowResistance3.D_h|flowResistance3.L|flowResistance3.L_value|flowResistance3.Xi_in.1.|flowResistance3.Xi_in.2.|flowResistance3.Xi_out.1.|flowResistance3.Xi_out.2.|flowResistance3.a|flowResistance3.areaCross|flowResistance3.areaCrossInput|flowResistance3.areaHydraulic|flowResistance3.b|flowResistance3.clip_p_out|flowResistance3.dp|flowResistance3.dr_corr|flowResistance3.h_in|flowResistance3.h_out|flowResistance3.initM_flow|der.flowResistance3.inlet.m_flow.|flowResistance3.inlet.m_flow|flowResistance3.inlet.r|flowResistance3.inlet.state.T|flowResistance3.inlet.state.X.1.|flowResistance3.inlet.state.X.2.|flowResistance3.inlet.state.p|flowResistance3.l|flowResistance3.m_acceleration_0|flowResistance3.m_flow|flowResistance3.m_flowStateSelect|flowResistance3.m_flow_0|flowResistance3.mu_in|flowResistance3.outlet.m_flow|flowResistance3.outlet.r|flowResistance3.outlet.state.T|flowResistance3.outlet.state.X.1.|flowResistance3.outlet.state.X.2.|flowResistance3.outlet.state.p|flowResistance3.p_in|flowResistance3.p_min|flowResistance3.p_out|flowResistance3.perimeter|flowResistance3.perimeterInput|flowResistance3.r|flowResistance3.rho_in|flowResistance3.rho_min|flowResistance3.shape|sink.L|der.sink.inlet.m_flow.|sink.inlet.m_flow|sink.inlet.r|sink.inlet.state.T|sink.inlet.state.X.1.|sink.inlet.state.X.2.|sink.inlet.state.p|sink.p|sink.p0|sink.p0_par|sink.r|source.L|source.T0|source.T0_par|source.Xi0.1.|source.Xi0.2.|source.Xi0_par.1.|source.Xi0_par.2.|source.h0|source.h0_par|der.source.outlet.m_flow.|source.outlet.m_flow|source.outlet.r|source.outlet.state.T|source.outlet.state.X.1.|source.outlet.state.X.2.|source.outlet.state.p|source.p0|source.p0_par|source1.L|source1.T0|source1.T0_par|source1.Xi0.1.|source1.Xi0.2.|source1.Xi0_par.1.|source1.Xi0_par.2.|source1.h0|source1.h0_par|der.source1.outlet.m_flow.|source1.outlet.m_flow|source1.outlet.r|source1.outlet.state.T|source1.outlet.state.X.1.|source1.outlet.state.X.2.|source1.outlet.state.p|source1.p0|source1.p0_par|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.1,2.|tank1.Xi_in.2,1.|tank1.Xi_in.2,2.|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_in.2.|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.inletPositions.2,1.|tank1.inletPositions.2,2.|tank1.inletPositions.2,3.|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|der.tank1.inlet.2..m_flow.|tank1.inlet.2..m_flow|tank1.inlet.2..r|tank1.inlet.2..state.T|tank1.inlet.2..state.X.1.|tank1.inlet.2..state.X.2.|tank1.inlet.2..state.p|tank1.k_volume_damping|tank1.liquidDensity|tank1.m_flow_assert|tank1.m_flow_in.1.|tank1.m_flow_in.2.|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_in.2.|tank1.p_ref|tank1.p_start|tank1.r.1.|tank1.r.2.|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.2.|tank1.staticHeadInlets_Pa_relative.1.|tank1.staticHeadInlets_Pa_relative.2.|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.TankOverfilling",simflags="-alarm=1200  -emit_protected -lv LOG_STATS")
simulate(ThermofluidStream.Boundaries.Tests.TankOverfilling,startTime=0,stopTime=1000,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|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|checkValve.L|checkValve.Xi_in.1.|checkValve.Xi_in.2.|checkValve.Xi_out.1.|checkValve.Xi_out.2.|checkValve.clip_p_out|checkValve.dp|checkValve.dr_corr|checkValve.h_in|checkValve.h_out|checkValve.initM_flow|der.checkValve.inlet.m_flow.|checkValve.inlet.m_flow|checkValve.inlet.r|checkValve.inlet.state.T|checkValve.inlet.state.X.1.|checkValve.inlet.state.X.2.|checkValve.inlet.state.p|checkValve.m_acceleration_0|checkValve.m_flow|checkValve.m_flowStateSelect|checkValve.m_flow_0|checkValve.m_flow_ref|checkValve.outlet.m_flow|checkValve.outlet.r|checkValve.outlet.state.T|checkValve.outlet.state.X.1.|checkValve.outlet.state.X.2.|checkValve.outlet.state.p|checkValve.p_in|checkValve.p_min|checkValve.p_out|checkValve.p_ref|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|flowResistance2.D_h|flowResistance2.L|flowResistance2.L_value|flowResistance2.Xi_in.1.|flowResistance2.Xi_in.2.|flowResistance2.Xi_out.1.|flowResistance2.Xi_out.2.|flowResistance2.a|flowResistance2.areaCross|flowResistance2.areaCrossInput|flowResistance2.areaHydraulic|flowResistance2.b|flowResistance2.clip_p_out|flowResistance2.dp|flowResistance2.dr_corr|flowResistance2.h_in|flowResistance2.h_out|flowResistance2.initM_flow|der.flowResistance2.inlet.m_flow.|flowResistance2.inlet.m_flow|flowResistance2.inlet.r|flowResistance2.inlet.state.T|flowResistance2.inlet.state.X.1.|flowResistance2.inlet.state.X.2.|flowResistance2.inlet.state.p|flowResistance2.l|flowResistance2.m_acceleration_0|flowResistance2.m_flow|flowResistance2.m_flowStateSelect|flowResistance2.m_flow_0|flowResistance2.mu_in|flowResistance2.outlet.m_flow|flowResistance2.outlet.r|flowResistance2.outlet.state.T|flowResistance2.outlet.state.X.1.|flowResistance2.outlet.state.X.2.|flowResistance2.outlet.state.p|flowResistance2.p_in|flowResistance2.p_min|flowResistance2.p_out|flowResistance2.perimeter|flowResistance2.perimeterInput|flowResistance2.r|flowResistance2.rho_in|flowResistance2.rho_min|flowResistance2.shape|flowResistance3.D_h|flowResistance3.L|flowResistance3.L_value|flowResistance3.Xi_in.1.|flowResistance3.Xi_in.2.|flowResistance3.Xi_out.1.|flowResistance3.Xi_out.2.|flowResistance3.a|flowResistance3.areaCross|flowResistance3.areaCrossInput|flowResistance3.areaHydraulic|flowResistance3.b|flowResistance3.clip_p_out|flowResistance3.dp|flowResistance3.dr_corr|flowResistance3.h_in|flowResistance3.h_out|flowResistance3.initM_flow|der.flowResistance3.inlet.m_flow.|flowResistance3.inlet.m_flow|flowResistance3.inlet.r|flowResistance3.inlet.state.T|flowResistance3.inlet.state.X.1.|flowResistance3.inlet.state.X.2.|flowResistance3.inlet.state.p|flowResistance3.l|flowResistance3.m_acceleration_0|flowResistance3.m_flow|flowResistance3.m_flowStateSelect|flowResistance3.m_flow_0|flowResistance3.mu_in|flowResistance3.outlet.m_flow|flowResistance3.outlet.r|flowResistance3.outlet.state.T|flowResistance3.outlet.state.X.1.|flowResistance3.outlet.state.X.2.|flowResistance3.outlet.state.p|flowResistance3.p_in|flowResistance3.p_min|flowResistance3.p_out|flowResistance3.perimeter|flowResistance3.perimeterInput|flowResistance3.r|flowResistance3.rho_in|flowResistance3.rho_min|flowResistance3.shape|sink.L|der.sink.inlet.m_flow.|sink.inlet.m_flow|sink.inlet.r|sink.inlet.state.T|sink.inlet.state.X.1.|sink.inlet.state.X.2.|sink.inlet.state.p|sink.p|sink.p0|sink.p0_par|sink.r|source.L|source.T0|source.T0_par|source.Xi0.1.|source.Xi0.2.|source.Xi0_par.1.|source.Xi0_par.2.|source.h0|source.h0_par|der.source.outlet.m_flow.|source.outlet.m_flow|source.outlet.r|source.outlet.state.T|source.outlet.state.X.1.|source.outlet.state.X.2.|source.outlet.state.p|source.p0|source.p0_par|source1.L|source1.T0|source1.T0_par|source1.Xi0.1.|source1.Xi0.2.|source1.Xi0_par.1.|source1.Xi0_par.2.|source1.h0|source1.h0_par|der.source1.outlet.m_flow.|source1.outlet.m_flow|source1.outlet.r|source1.outlet.state.T|source1.outlet.state.X.1.|source1.outlet.state.X.2.|source1.outlet.state.p|source1.p0|source1.p0_par|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.1,2.|tank1.Xi_in.2,1.|tank1.Xi_in.2,2.|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_in.2.|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.inletPositions.2,1.|tank1.inletPositions.2,2.|tank1.inletPositions.2,3.|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|der.tank1.inlet.2..m_flow.|tank1.inlet.2..m_flow|tank1.inlet.2..r|tank1.inlet.2..state.T|tank1.inlet.2..state.X.1.|tank1.inlet.2..state.X.2.|tank1.inlet.2..state.p|tank1.k_volume_damping|tank1.liquidDensity|tank1.m_flow_assert|tank1.m_flow_in.1.|tank1.m_flow_in.2.|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_in.2.|tank1.p_ref|tank1.p_start|tank1.r.1.|tank1.r.2.|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.2.|tank1.staticHeadInlets_Pa_relative.1.|tank1.staticHeadInlets_Pa_relative.2.|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.TankOverfilling",simflags="-alarm=1200  -emit_protected -lv LOG_STATS") [Timeout 1860]
"Notification: Performance of FrontEnd - loaded program: time 7.82e-07/7.82e-07, allocations: 0 / 0, free: 0 / 0
Notification: Performance of FrontEnd - Absyn->SCode: time 2.477e-05/2.555e-05, allocations: 0 / 0, free: 0 / 0
Notification: Performance of NFInst.instantiate(ThermofluidStream.Boundaries.Tests.TankOverfilling): time 0.6172/0.6172, allocations: 0 / 0, free: 0 / 0
Notification: Performance of NFInst.instExpressions: time 0.01671/0.634, allocations: 0 / 0, free: 0 / 0
Notification: Performance of NFInst.updateImplicitVariability: time 0.001408/0.6354, allocations: 0 / 0, free: 0 / 0
Notification: Performance of NFTyping.typeComponents: time 0.004133/0.6395, allocations: 0 / 0, free: 0 / 0
Notification: Performance of NFTyping.typeBindings: time 0.01776/0.6572, allocations: 0 / 0, free: 0 / 0
Notification: Performance of NFTyping.typeClassSections: time 0.009687/0.6669, allocations: 0 / 0, free: 0 / 0
Notification: Performance of NFFlatten.flatten: time 0.004296/0.6712, allocations: 0 / 0, free: 0 / 0
Notification: Performance of NFFlatten.resolveConnections: time 0.0007946/0.672, allocations: 0 / 0, free: 0 / 0
Notification: Performance of NFEvalConstants.evaluate: time 0.01105/0.6831, allocations: 0 / 0, free: 0 / 0
Notification: Performance of NFSimplifyModel.simplify: time 0.002984/0.6861, allocations: 0 / 0, free: 0 / 0
Notification: Performance of NFPackage.collectConstants: time 0.0004869/0.6866, allocations: 0 / 0, free: 0 / 0
Notification: Performance of NFFlatten.collectFunctions: time 0.02367/0.7102, allocations: 0 / 0, free: 0 / 0
Notification: Performance of NFScalarize.scalarize: time 0.001403/0.7116, allocations: 0 / 0, free: 0 / 0
Notification: Performance of NFVerifyModel.verify: time 0.00204/0.7137, allocations: 0 / 0, free: 0 / 0
Notification: Performance of NFConvertDAE.convert: time 0.01421/0.7279, allocations: 0 / 0, free: 0 / 0
Notification: Performance of FrontEnd - DAE generated: time 0.0005626/0.7284, allocations: 0 / 0, free: 0 / 0
Notification: Performance of FrontEnd: time 4.639e-06/0.7284, allocations: 0 / 0, free: 0 / 0
Notification: Performance of Transformations before backend: time 2.73e-05/0.7285, 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: 236
 * Number of variables: 236
Notification: Performance of Generate backend data structure: time 0.01673/0.7452, allocations: 0 / 0, free: 0 / 0
Notification: Performance of prepare preOptimizeDAE: time 0.0001835/0.7454, allocations: 0 / 0, free: 0 / 0
Notification: Performance of preOpt normalInlineFunction (simulation): time 0.005361/0.7507, allocations: 0 / 0, free: 0 / 0
Notification: Performance of preOpt evaluateParameters (simulation): time 0.00567/0.7564, allocations: 0 / 0, free: 0 / 0
Notification: Performance of preOpt simplifyIfEquations (simulation): time 0.001099/0.7575, allocations: 0 / 0, free: 0 / 0
Notification: Performance of preOpt expandDerOperator (simulation): time 0.0006641/0.7582, allocations: 0 / 0, free: 0 / 0
Notification: Performance of preOpt clockPartitioning (simulation): time 0.01061/0.7688, allocations: 0 / 0, free: 0 / 0
Notification: Performance of preOpt findStateOrder (simulation): time 5.897e-05/0.7688, allocations: 0 / 0, free: 0 / 0
Notification: Performance of preOpt replaceEdgeChange (simulation): time 0.0004384/0.7693, allocations: 0 / 0, free: 0 / 0
Notification: Performance of preOpt inlineArrayEqn (simulation): time 0.0007384/0.77, allocations: 0 / 0, free: 0 / 0
Notification: Performance of preOpt removeEqualRHS (simulation): time 0.01106/0.7811, allocations: 0 / 0, free: 0 / 0
Notification: Performance of preOpt removeSimpleEquations (simulation): time 0.02724/0.8083, allocations: 0 / 0, free: 0 / 0
Notification: Performance of preOpt comSubExp (simulation): time 0.006455/0.8148, allocations: 0 / 0, free: 0 / 0
Notification: Performance of preOpt resolveLoops (simulation): time 0.004889/0.8197, allocations: 0 / 0, free: 0 / 0
Notification: Performance of preOpt evalFunc (simulation): time 0.001629/0.8213, allocations: 0 / 0, free: 0 / 0
Notification: Performance of preOpt encapsulateWhenConditions (simulation): time 0.000111/0.8214, allocations: 0 / 0, free: 0 / 0
Notification: Performance of pre-optimization done (n=116): time 0.0001965/0.8216, allocations: 0 / 0, free: 0 / 0
Notification: Performance of matching and sorting (n=116): time 0.01961/0.8412, allocations: 0 / 0, free: 0 / 0
Notification: Performance of inlineWhenForInitialization (initialization): time 0.0001172/0.8413, allocations: 0 / 0, free: 0 / 0
Notification: Performance of selectInitializationVariablesDAE (initialization): time 0.003532/0.8448, allocations: 0 / 0, free: 0 / 0
Notification: Performance of collectPreVariables (initialization): time 0.0007891/0.8456, allocations: 0 / 0, free: 0 / 0
Notification: Performance of collectInitialEqns (initialization): time 0.0009469/0.8466, allocations: 0 / 0, free: 0 / 0
Notification: Performance of collectInitialBindings (initialization): time 0.0009126/0.8475, allocations: 0 / 0, free: 0 / 0
Notification: Performance of simplifyInitialFunctions (initialization): time 0.00201/0.8495, allocations: 0 / 0, free: 0 / 0
Notification: Performance of setup shared object (initialization): time 0.0003067/0.8498, allocations: 0 / 0, free: 0 / 0
Notification: Performance of preBalanceInitialSystem (initialization): time 0.004733/0.8545, allocations: 0 / 0, free: 0 / 0
Notification: Performance of partitionIndependentBlocks (initialization): time 0.005642/0.8602, allocations: 0 / 0, free: 0 / 0
Notification: Performance of analyzeInitialSystem (initialization): time 0.116/0.9762, allocations: 0 / 0, free: 0 / 0
Notification: Performance of solveInitialSystemEqSystem (initialization): time 2.344e-05/0.9762, allocations: 0 / 0, free: 0 / 0
Notification: Performance of matching and sorting (n=132) (initialization): time 0.01441/0.9906, allocations: 0 / 0, free: 0 / 0
Notification: Performance of prepare postOptimizeDAE: time 5.77e-05/0.9907, allocations: 0 / 0, free: 0 / 0
Notification: Performance of postOpt simplifyComplexFunction (initialization): time 2.342e-05/0.9907, allocations: 0 / 0, free: 0 / 0
Notification: Performance of postOpt tearingSystem (initialization): time 0.001212/0.9919, allocations: 0 / 0, free: 0 / 0
Notification: Performance of postOpt solveSimpleEquations (initialization): time 0.002618/0.9945, allocations: 0 / 0, free: 0 / 0
Notification: Performance of postOpt calculateStrongComponentJacobians (initialization): time 0.0113/1.006, allocations: 0 / 0, free: 0 / 0
Notification: Performance of postOpt simplifyAllExpressions (initialization): time 0.002593/1.008, allocations: 0 / 0, free: 0 / 0
Notification: Performance of postOpt collapseArrayExpressions (initialization): time 0.0006458/1.009, allocations: 0 / 0, free: 0 / 0
Warning: Assuming fixed start value for the following 3 variables:
         checkValve.inlet.m_flow:VARIABLE(flow=true min = -1e5 max = 1e5 unit = \"kg/s\" fixed = true )  \"Mass flow rate\" type: Real
         flowResistance3.inlet.m_flow:VARIABLE(flow=true min = -1e5 max = 1e5 unit = \"kg/s\" fixed = true )  \"Mass flow rate\" type: Real
         flowResistance2.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: 9
 * Number of states: 0 ()
 * Number of discrete variables: 2 (tank1.fEmpty,tank1.fFull)
 * Number of discrete states: 0 ()
 * Number of clocked states: 0 ()
 * Top-level inputs: 0
Notification: Strong component statistics for initialization (110):
 * Single equations (assignments): 99
 * Array equations: 5
 * 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
   {(1,2,100.0%), (1,2,100.0%), (1,3,100.0%)}
 * Non-linear torn systems (#iteration vars, #inner vars): 0 systems
Notification: Performance of prepare postOptimizeDAE: time 0.002566/1.012, allocations: 0 / 0, free: 0 / 0
Notification: Performance of postOpt lateInlineFunction (simulation): time 0.001546/1.013, allocations: 0 / 0, free: 0 / 0
Notification: Performance of postOpt wrapFunctionCalls (simulation): time 0.01747/1.031, allocations: 0 / 0, free: 0 / 0
Notification: Performance of postOpt inlineArrayEqn (simulation): time 0.01237/1.043, allocations: 0 / 0, free: 0 / 0
Notification: Performance of postOpt constantLinearSystem (simulation): time 2.063e-05/1.043, allocations: 0 / 0, free: 0 / 0
Notification: Performance of postOpt simplifysemiLinear (simulation): time 2.839e-05/1.043, allocations: 0 / 0, free: 0 / 0
Notification: Performance of postOpt removeSimpleEquations (simulation): time 0.02304/1.066, allocations: 0 / 0, free: 0 / 0
Notification: Performance of postOpt simplifyComplexFunction (simulation): time 1.856e-05/1.066, allocations: 0 / 0, free: 0 / 0
Notification: Performance of postOpt solveSimpleEquations (simulation): time 0.002553/1.069, allocations: 0 / 0, free: 0 / 0
Notification: Performance of postOpt tearingSystem (simulation): time 0.00335/1.072, allocations: 0 / 0, free: 0 / 0
Notification: Performance of postOpt inputDerivativesUsed (simulation): time 0.0006293/1.073, allocations: 0 / 0, free: 0 / 0
Notification: Performance of postOpt calculateStrongComponentJacobians (simulation): time 0.01207/1.085, allocations: 0 / 0, free: 0 / 0
Notification: Performance of postOpt calculateStateSetsJacobians (simulation): time 3.978e-06/1.085, allocations: 0 / 0, free: 0 / 0
Notification: Performance of postOpt symbolicJacobian (simulation): time 0.01934/1.104, allocations: 0 / 0, free: 0 / 0
Notification: Performance of postOpt removeConstants (simulation): time 0.003152/1.107, allocations: 0 / 0, free: 0 / 0
Notification: Performance of postOpt simplifyTimeIndepFuncCalls (simulation): time 0.0008681/1.108, allocations: 0 / 0, free: 0 / 0
Notification: Performance of postOpt simplifyAllExpressions (simulation): time 0.001971/1.11, allocations: 0 / 0, free: 0 / 0
Notification: Performance of postOpt findZeroCrossings (simulation): time 0.00205/1.112, allocations: 0 / 0, free: 0 / 0
Notification: Performance of postOpt collapseArrayExpressions (simulation): time 0.0006469/1.113, allocations: 0 / 0, free: 0 / 0
Notification: Performance of sorting global known variables: time 0.002573/1.115, allocations: 0 / 0, free: 0 / 0
Notification: Performance of sort global known variables: time 6.589e-05/1.115, allocations: 0 / 0, free: 0 / 0
Notification: Performance of remove unused functions: time 0.006407/1.122, allocations: 0 / 0, free: 0 / 0
Notification: Model statistics after passing the back-end for simulation:
 * Number of independent subsystems: 1
 * Number of states: 7 (flowResistance2.inlet.m_flow,tank1.M,tank1.MXi[1],tank1.MXi[2],tank1.U_med,flowResistance3.inlet.m_flow,checkValve.inlet.m_flow)
 * Number of discrete variables: 2 (tank1.fFull,tank1.fEmpty)
 * Number of discrete states: 0 ()
 * Number of clocked states: 0 ()
 * Top-level inputs: 0
Notification: Strong component statistics for simulation (102):
 * Single equations (assignments): 91
 * Array equations: 5
 * Algorithm blocks: 0
 * Record equations: 2
 * When equations: 0
 * If-equations: 0
 * Equation systems (not torn): 0
 * Torn equation systems: 4
 * 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%), (1,2,100.0%)}
 * Non-linear torn systems (#iteration vars, #inner vars): 1 system
   {(2,3)}
Notification: Performance of Backend phase and start with SimCode phase: time 0.007116/1.129, allocations: 0 / 0, free: 0 / 0
Notification: Performance of simCode: created initialization part: time 0.01182/1.141, allocations: 0 / 0, free: 0 / 0
Notification: Performance of simCode: created event and clocks part: time 9.257e-06/1.141, allocations: 0 / 0, free: 0 / 0
Notification: Performance of simCode: created simulation system equations: time 0.006678/1.147, allocations: 0 / 0, free: 0 / 0
Notification: Performance of simCode: created of all other equations (e.g. parameter, nominal, assert, etc): time 0.006968/1.154, allocations: 0 / 0, free: 0 / 0
Notification: Performance of simCode: created linear, non-linear and system jacobian parts: time 0.0162/1.171, allocations: 0 / 0, free: 0 / 0
Notification: Performance of simCode: some other stuff during SimCode phase: time 0.002265/1.173, allocations: 0 / 0, free: 0 / 0
Notification: Performance of simCode: alias equations: time 0.003177/1.176, allocations: 0 / 0, free: 0 / 0
Notification: Performance of simCode: all other stuff during SimCode phase: time 0.003671/1.18, allocations: 0 / 0, free: 0 / 0
Notification: Performance of SimCode: time 0.001571/1.181, allocations: 0 / 0, free: 0 / 0
Notification: Performance of Templates: time 0.01987/1.201, allocations: 0 / 0, free: 0 / 0
"
[Timeout remaining time 1858]
diffSimulationResults("ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankOverfilling_res.mat","/mnt/ReferenceFiles/ThermofluidStream-main-regression/ReferenceData/ThermofluidStream.Boundaries.Tests.TankOverfilling_ref.mat","/var/lib/jenkins/ws/OpenModelicaLibraryTestingWork/OpenModelicaLibraryTesting/files/ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankOverfilling.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.TankOverfilling_res.mat.
Warning: Get data of variable CPUtime from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankOverfilling_res.mat failed!
Error: Could not read variable EventCounter in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankOverfilling_res.mat.
Warning: Get data of variable EventCounter from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankOverfilling_res.mat failed!
Error: Could not read variable NonlinearSystems.simulation[1].Calls in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankOverfilling_res.mat.
Warning: Get data of variable NonlinearSystems.simulation[1].Calls from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankOverfilling_res.mat failed!
Error: Could not read variable NonlinearSystems.simulation[1].Iterations in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankOverfilling_res.mat.
Warning: Get data of variable NonlinearSystems.simulation[1].Iterations from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankOverfilling_res.mat failed!
Error: Could not read variable NonlinearSystems.simulation[1].Jacobians in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankOverfilling_res.mat.
Warning: Get data of variable NonlinearSystems.simulation[1].Jacobians from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankOverfilling_res.mat failed!
Error: Could not read variable NonlinearSystems.simulation[1].Residues in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankOverfilling_res.mat.
Warning: Get data of variable NonlinearSystems.simulation[1].Residues from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankOverfilling_res.mat failed!
Error: Could not read variable _GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.H0 in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankOverfilling_res.mat.
Warning: Get data of variable _GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.H0 from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankOverfilling_res.mat failed!
Error: Could not read variable _GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.Hf in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankOverfilling_res.mat.
Warning: Get data of variable _GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.Hf from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankOverfilling_res.mat failed!
Error: Could not read variable _GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.MM in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankOverfilling_res.mat.
Warning: Get data of variable _GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.MM from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankOverfilling_res.mat failed!
Error: Could not read variable _GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.R_s in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankOverfilling_res.mat.
Warning: Get data of variable _GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.R_s from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankOverfilling_res.mat failed!
Error: Could not read variable _GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.Tlimit in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankOverfilling_res.mat.
Warning: Get data of variable _GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.Tlimit from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankOverfilling_res.mat failed!
Error: Could not read variable _GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.ahigh[1] in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankOverfilling_res.mat.
Warning: Get data of variable _GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.ahigh[1] from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankOverfilling_res.mat failed!
Error: Could not read variable _GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.ahigh[2] in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankOverfilling_res.mat.
Warning: Get data of variable _GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.ahigh[2] from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankOverfilling_res.mat failed!
Error: Could not read variable _GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.ahigh[3] in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankOverfilling_res.mat.
Warning: Get data of variable _GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.ahigh[3] from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankOverfilling_res.mat failed!
Error: Could not read variable _GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.ahigh[4] in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankOverfilling_res.mat.
Warning: Get data of variable _GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.ahigh[4] from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankOverfilling_res.mat failed!
Error: Could not read variable _GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.ahigh[5] in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankOverfilling_res.mat.
Warning: Get data of variable _GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.ahigh[5] from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankOverfilling_res.mat failed!
Error: Could not read variable _GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.ahigh[6] in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankOverfilling_res.mat.
Warning: Get data of variable _GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.ahigh[6] from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankOverfilling_res.mat failed!
Error: Could not read variable _GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.ahigh[7] in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankOverfilling_res.mat.
Warning: Get data of variable _GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.ahigh[7] from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankOverfilling_res.mat failed!
Error: Could not read variable _GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.alow[1] in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankOverfilling_res.mat.
Warning: Get data of variable _GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.alow[1] from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankOverfilling_res.mat failed!
Error: Could not read variable _GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.alow[2] in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankOverfilling_res.mat.
Warning: Get data of variable _GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.alow[2] from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankOverfilling_res.mat failed!
Error: Could not read variable _GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.alow[3] in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankOverfilling_res.mat.
Warning: Get data of variable _GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.alow[3] from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankOverfilling_res.mat failed!
Error: Could not read variable _GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.alow[4] in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankOverfilling_res.mat.
Warning: Get data of variable _GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.alow[4] from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankOverfilling_res.mat failed!
Error: Could not read variable _GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.alow[5] in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankOverfilling_res.mat.
Warning: Get data of variable _GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.alow[5] from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankOverfilling_res.mat failed!
Error: Could not read variable _GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.alow[6] in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankOverfilling_res.mat.
Warning: Get data of variable _GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.alow[6] from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankOverfilling_res.mat failed!
Error: Could not read variable _GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.alow[7] in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankOverfilling_res.mat.
Warning: Get data of variable _GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.alow[7] from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankOverfilling_res.mat failed!
Error: Could not read variable _GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.bhigh[1] in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankOverfilling_res.mat.
Warning: Get data of variable _GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.bhigh[1] from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankOverfilling_res.mat failed!
Error: Could not read variable _GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.bhigh[2] in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankOverfilling_res.mat.
Warning: Get data of variable _GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.bhigh[2] from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankOverfilling_res.mat failed!
Error: Could not read variable _GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.blow[1] in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankOverfilling_res.mat.
Warning: Get data of variable _GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.blow[1] from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankOverfilling_res.mat failed!
Error: Could not read variable _GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.blow[2] in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankOverfilling_res.mat.
Warning: Get data of variable _GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.blow[2] from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankOverfilling_res.mat failed!
Error: Could not read variable _GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.H0 in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankOverfilling_res.mat.
Warning: Get data of variable _GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.H0 from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankOverfilling_res.mat failed!
Error: Could not read variable _GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.Hf in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankOverfilling_res.mat.
Warning: Get data of variable _GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.Hf from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankOverfilling_res.mat failed!
Error: Could not read variable _GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.MM in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankOverfilling_res.mat.
Warning: Get data of variable _GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.MM from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankOverfilling_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.TankOverfilling_res.mat.
Warning: Get data of variable _GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.R_s from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankOverfilling_res.mat failed!
Error: Could not read variable _GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.Tlimit in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankOverfilling_res.mat.
Warning: Get data of variable _GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.Tlimit from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankOverfilling_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.TankOverfilling_res.mat.
Warning: Get data of variable _GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.ahigh[1] from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankOverfilling_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.TankOverfilling_res.mat.
Warning: Get data of variable _GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.ahigh[2] from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankOverfilling_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.TankOverfilling_res.mat.
Warning: Get data of variable _GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.ahigh[3] from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankOverfilling_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.TankOverfilling_res.mat.
Warning: Get data of variable _GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.ahigh[4] from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankOverfilling_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.TankOverfilling_res.mat.
Warning: Get data of variable _GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.ahigh[5] from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankOverfilling_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.TankOverfilling_res.mat.
Warning: Get data of variable _GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.ahigh[6] from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankOverfilling_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.TankOverfilling_res.mat.
Warning: Get data of variable _GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.ahigh[7] from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankOverfilling_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.TankOverfilling_res.mat.
Warning: Get data of variable _GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.alow[1] from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankOverfilling_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.TankOverfilling_res.mat.
Warning: Get data of variable _GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.alow[2] from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankOverfilling_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.TankOverfilling_res.mat.
Warning: Get data of variable _GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.alow[3] from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankOverfilling_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.TankOverfilling_res.mat.
Warning: Get data of variable _GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.alow[4] from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankOverfilling_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.TankOverfilling_res.mat.
Warning: Get data of variable _GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.alow[5] from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankOverfilling_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.TankOverfilling_res.mat.
Warning: Get data of variable _GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.alow[6] from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankOverfilling_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.TankOverfilling_res.mat.
Warning: Get data of variable _GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.alow[7] from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankOverfilling_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.TankOverfilling_res.mat.
Warning: Get data of variable _GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.bhigh[1] from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankOverfilling_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.TankOverfilling_res.mat.
Warning: Get data of variable _GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.bhigh[2] from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankOverfilling_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.TankOverfilling_res.mat.
Warning: Get data of variable _GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.blow[1] from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankOverfilling_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.TankOverfilling_res.mat.
Warning: Get data of variable _GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.blow[2] from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankOverfilling_res.mat failed!
Error: Could not read variable source.outlet.der(m_flow) in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankOverfilling_res.mat.
Warning: Get data of variable source.outlet.der(m_flow) from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankOverfilling_res.mat failed!
Error: Could not read variable tank1.inlet[1].der(m_flow) in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankOverfilling_res.mat.
Warning: Get data of variable tank1.inlet[1].der(m_flow) from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankOverfilling_res.mat failed!
Error: Could not read variable tank1.outlet[1].der(m_flow) in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankOverfilling_res.mat.
Warning: Get data of variable tank1.outlet[1].der(m_flow) from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankOverfilling_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,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,checkValve.L,checkValve.Xi_in[1],checkValve.Xi_in[2],checkValve.Xi_out[1],checkValve.Xi_out[2],checkValve.clip_p_out,checkValve.dp,checkValve.dr_corr,checkValve.h_in,checkValve.h_out,checkValve.initM_flow,der(checkValve.inlet.m_flow),checkValve.inlet.m_flow,checkValve.inlet.r,checkValve.inlet.state.T,checkValve.inlet.state.X[1],checkValve.inlet.state.X[2],checkValve.inlet.state.p,checkValve.m_acceleration_0,checkValve.m_flow,checkValve.m_flowStateSelect,checkValve.m_flow_0,checkValve.m_flow_ref,checkValve.outlet.m_flow,checkValve.outlet.r,checkValve.outlet.state.T,checkValve.outlet.state.X[1],checkValve.outlet.state.X[2],checkValve.outlet.state.p,checkValve.p_in,checkValve.p_min,checkValve.p_out,checkValve.p_ref,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,flowResistance2.D_h,flowResistance2.L,flowResistance2.L_value,flowResistance2.Xi_in[1],flowResistance2.Xi_in[2],flowResistance2.Xi_out[1],flowResistance2.Xi_out[2],flowResistance2.a,flowResistance2.areaCross,flowResistance2.areaCrossInput,flowResistance2.areaHydraulic,flowResistance2.b,flowResistance2.clip_p_out,flowResistance2.dp,flowResistance2.dr_corr,flowResistance2.h_in,flowResistance2.h_out,flowResistance2.initM_flow,der(flowResistance2.inlet.m_flow),flowResistance2.inlet.m_flow,flowResistance2.inlet.r,flowResistance2.inlet.state.T,flowResistance2.inlet.state.X[1],flowResistance2.inlet.state.X[2],flowResistance2.inlet.state.p,flowResistance2.l,flowResistance2.m_acceleration_0,flowResistance2.m_flow,flowResistance2.m_flowStateSelect,flowResistance2.m_flow_0,flowResistance2.mu_in,flowResistance2.outlet.m_flow,flowResistance2.outlet.r,flowResistance2.outlet.state.T,flowResistance2.outlet.state.X[1],flowResistance2.outlet.state.X[2],flowResistance2.outlet.state.p,flowResistance2.p_in,flowResistance2.p_min,flowResistance2.p_out,flowResistance2.perimeter,flowResistance2.perimeterInput,flowResistance2.r,flowResistance2.rho_in,flowResistance2.rho_min,flowResistance2.shape,flowResistance3.D_h,flowResistance3.L,flowResistance3.L_value,flowResistance3.Xi_in[1],flowResistance3.Xi_in[2],flowResistance3.Xi_out[1],flowResistance3.Xi_out[2],flowResistance3.a,flowResistance3.areaCross,flowResistance3.areaCrossInput,flowResistance3.areaHydraulic,flowResistance3.b,flowResistance3.clip_p_out,flowResistance3.dp,flowResistance3.dr_corr,flowResistance3.h_in,flowResistance3.h_out,flowResistance3.initM_flow,der(flowResistance3.inlet.m_flow),flowResistance3.inlet.m_flow,flowResistance3.inlet.r,flowResistance3.inlet.state.T,flowResistance3.inlet.state.X[1],flowResistance3.inlet.state.X[2],flowResistance3.inlet.state.p,flowResistance3.l,flowResistance3.m_acceleration_0,flowResistance3.m_flow,flowResistance3.m_flowStateSelect,flowResistance3.m_flow_0,flowResistance3.mu_in,flowResistance3.outlet.m_flow,flowResistance3.outlet.r,flowResistance3.outlet.state.T,flowResistance3.outlet.state.X[1],flowResistance3.outlet.state.X[2],flowResistance3.outlet.state.p,flowResistance3.p_in,flowResistance3.p_min,flowResistance3.p_out,flowResistance3.perimeter,flowResistance3.perimeterInput,flowResistance3.r,flowResistance3.rho_in,flowResistance3.rho_min,flowResistance3.shape,sink.L,der(sink.inlet.m_flow),sink.inlet.m_flow,sink.inlet.r,sink.inlet.state.T,sink.inlet.state.X[1],sink.inlet.state.X[2],sink.inlet.state.p,sink.p,sink.p0,sink.p0_par,sink.r,source.L,source.T0,source.T0_par,source.Xi0[1],source.Xi0[2],source.Xi0_par[1],source.Xi0_par[2],source.h0,source.h0_par,der(source.outlet.m_flow),source.outlet.m_flow,source.outlet.r,source.outlet.state.T,source.outlet.state.X[1],source.outlet.state.X[2],source.outlet.state.p,source.p0,source.p0_par,source1.L,source1.T0,source1.T0_par,source1.Xi0[1],source1.Xi0[2],source1.Xi0_par[1],source1.Xi0_par[2],source1.h0,source1.h0_par,der(source1.outlet.m_flow),source1.outlet.m_flow,source1.outlet.r,source1.outlet.state.T,source1.outlet.state.X[1],source1.outlet.state.X[2],source1.outlet.state.p,source1.p0,source1.p0_par,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[1,2],tank1.Xi_in[2,1],tank1.Xi_in[2,2],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_in[2],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.inletPositions[2,1],tank1.inletPositions[2,2],tank1.inletPositions[2,3],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,der(tank1.inlet[2].m_flow),tank1.inlet[2].m_flow,tank1.inlet[2].r,tank1.inlet[2].state.T,tank1.inlet[2].state.X[1],tank1.inlet[2].state.X[2],tank1.inlet[2].state.p,tank1.k_volume_damping,tank1.liquidDensity,tank1.m_flow_assert,tank1.m_flow_in[1],tank1.m_flow_in[2],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_in[2],tank1.p_ref,tank1.p_start,tank1.r[1],tank1.r[2],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[2],tank1.staticHeadInlets_Pa_relative[1],tank1.staticHeadInlets_Pa_relative[2],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,checkValve.L,checkValve.Xi_in[1],checkValve.Xi_in[2],checkValve.Xi_out[1],checkValve.Xi_out[2],checkValve.clip_p_out,checkValve.dp,checkValve.dr_corr,checkValve.h_in,checkValve.h_out,checkValve.initM_flow,checkValve.inlet.m_flow,checkValve.inlet.r,checkValve.inlet.state.T,checkValve.inlet.state.X[1],checkValve.inlet.state.X[2],checkValve.inlet.state.p,checkValve.m_acceleration_0,checkValve.m_flow,checkValve.m_flowStateSelect,checkValve.m_flow_0,checkValve.m_flow_ref,checkValve.outlet.m_flow,checkValve.outlet.r,checkValve.outlet.state.T,checkValve.outlet.state.X[1],checkValve.outlet.state.X[2],checkValve.outlet.state.p,checkValve.p_in,checkValve.p_min,checkValve.p_out,checkValve.p_ref,der(checkValve.inlet.m_flow),der(flowResistance2.inlet.m_flow),der(flowResistance3.inlet.m_flow),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,flowResistance2.D_h,flowResistance2.L,flowResistance2.L_value,flowResistance2.Xi_in[1],flowResistance2.Xi_in[2],flowResistance2.Xi_out[1],flowResistance2.Xi_out[2],flowResistance2.a,flowResistance2.areaCross,flowResistance2.areaCrossInput,flowResistance2.areaHydraulic,flowResistance2.b,flowResistance2.clip_p_out,flowResistance2.dp,flowResistance2.dp_ref_color,flowResistance2.dr_corr,flowResistance2.h_in,flowResistance2.h_out,flowResistance2.initM_flow,flowResistance2.inlet.m_flow,flowResistance2.inlet.r,flowResistance2.inlet.state.T,flowResistance2.inlet.state.X[1],flowResistance2.inlet.state.X[2],flowResistance2.inlet.state.p,flowResistance2.l,flowResistance2.m_acceleration_0,flowResistance2.m_flow,flowResistance2.m_flowStateSelect,flowResistance2.m_flow_0,flowResistance2.mu_in,flowResistance2.outlet.m_flow,flowResistance2.outlet.r,flowResistance2.outlet.state.T,flowResistance2.outlet.state.X[1],flowResistance2.outlet.state.X[2],flowResistance2.outlet.state.p,flowResistance2.p_in,flowResistance2.p_min,flowResistance2.p_out,flowResistance2.perimeter,flowResistance2.perimeterInput,flowResistance2.pressureDropSignificantDigits,flowResistance2.r,flowResistance2.rho_in,flowResistance2.rho_min,flowResistance2.shape,flowResistance3.D_h,flowResistance3.L,flowResistance3.L_value,flowResistance3.Xi_in[1],flowResistance3.Xi_in[2],flowResistance3.Xi_out[1],flowResistance3.Xi_out[2],flowResistance3.a,flowResistance3.areaCross,flowResistance3.areaCrossInput,flowResistance3.areaHydraulic,flowResistance3.b,flowResistance3.clip_p_out,flowResistance3.dp,flowResistance3.dp_ref_color,flowResistance3.dr_corr,flowResistance3.h_in,flowResistance3.h_out,flowResistance3.initM_flow,flowResistance3.inlet.m_flow,flowResistance3.inlet.r,flowResistance3.inlet.state.T,flowResistance3.inlet.state.X[1],flowResistance3.inlet.state.X[2],flowResistance3.inlet.state.p,flowResistance3.l,flowResistance3.m_acceleration_0,flowResistance3.m_flow,flowResistance3.m_flowStateSelect,flowResistance3.m_flow_0,flowResistance3.mu_in,flowResistance3.outlet.m_flow,flowResistance3.outlet.r,flowResistance3.outlet.state.T,flowResistance3.outlet.state.X[1],flowResistance3.outlet.state.X[2],flowResistance3.outlet.state.p,flowResistance3.p_in,flowResistance3.p_min,flowResistance3.p_out,flowResistance3.perimeter,flowResistance3.perimeterInput,flowResistance3.pressureDropSignificantDigits,flowResistance3.r,flowResistance3.rho_in,flowResistance3.rho_min,flowResistance3.shape,sink.L,sink.inlet.m_flow,sink.inlet.r,sink.inlet.state.T,sink.inlet.state.X[1],sink.inlet.state.X[2],sink.inlet.state.p,sink.p,sink.p0,sink.p0_par,sink.r,source.L,source.T0,source.T0_par,source.Xi0[1],source.Xi0[2],source.Xi0_par[1],source.Xi0_par[2],source.h0,source.h0_par,source.outlet.m_flow,source.outlet.r,source.outlet.state.T,source.outlet.state.X[1],source.outlet.state.X[2],source.outlet.state.p,source.p0,source.p0_par,source1.L,source1.T0,source1.T0_par,source1.Xi0[1],source1.Xi0[2],source1.Xi0_par[1],source1.Xi0_par[2],source1.h0,source1.h0_par,source1.outlet.m_flow,source1.outlet.r,source1.outlet.state.T,source1.outlet.state.X[1],source1.outlet.state.X[2],source1.outlet.state.p,source1.p0,source1.p0_par,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[1,2],tank1.Xi_in[2,1],tank1.Xi_in[2,2],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_in[2],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.inletPositions[2,1],tank1.inletPositions[2,2],tank1.inletPositions[2,3],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.inlet[2].m_flow,tank1.inlet[2].r,tank1.inlet[2].state.T,tank1.inlet[2].state.X[1],tank1.inlet[2].state.X[2],tank1.inlet[2].state.p,tank1.k_volume_damping,tank1.liquidDensity,tank1.m_flow_assert,tank1.m_flow_in[1],tank1.m_flow_in[2],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_in[2],tank1.p_ref,tank1.p_start,tank1.r[1],tank1.r[2],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[2],tank1.staticHeadInlets_Pa_relative[1],tank1.staticHeadInlets_Pa_relative[2],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: 3.620471381000243]