Running: ./testmodel.py --libraries=/home/hudson/saved_omc/libraries/.openmodelica/libraries --ompython_omhome=/usr ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating.conf.json
loadFile("/home/hudson/saved_omc/libraries/.openmodelica/libraries/ModelicaServices 4.1.0+maint.om/package.mo", uses=false) [Timeout 180]
"Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/ModelicaServices 4.1.0+maint.om/package.mo): time 0.0009059/0.0009059, allocations: 93.06 kB / 19.65 MB, free: 280 kB / 13.93 MB
"
[Timeout remaining time 180]
loadFile("/home/hudson/saved_omc/libraries/.openmodelica/libraries/Complex 4.1.0+maint.om/package.mo", uses=false) [Timeout 180]
"Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/Complex 4.1.0+maint.om/package.mo): time 0.001037/0.001037, allocations: 173.3 kB / 23.03 MB, free: 1.547 MB / 18.57 MB
"
[Timeout remaining time 180]
loadFile("/home/hudson/saved_omc/libraries/.openmodelica/libraries/Modelica 4.1.0+maint.om/package.mo", uses=false) [Timeout 180]
"Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/Modelica 4.1.0+maint.om/package.mo): time 0.9474/0.9474, allocations: 177.1 MB / 203.4 MB, free: 5.637 MB / 186.7 MB
"
[Timeout remaining time 179]
loadFile("/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermofluidStream main/package.mo", uses=false) [Timeout 180]
"Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermofluidStream main/package.mo): time 0.6287/0.6287, allocations: 118.6 MB / 378.6 MB, free: 1.496 MB / 346.7 MB
"
[Timeout remaining time 179]
Using package ThermofluidStream with version 1.4.0 (/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermofluidStream main/package.mo)
Using package Modelica with version 4.1.0 (/home/hudson/saved_omc/libraries/.openmodelica/libraries/Modelica 4.1.0+maint.om/package.mo)
Using package Complex with version 4.1.0 (/home/hudson/saved_omc/libraries/.openmodelica/libraries/Complex 4.1.0+maint.om/package.mo)
Using package ModelicaServices with version 4.1.0 (/home/hudson/saved_omc/libraries/.openmodelica/libraries/ModelicaServices 4.1.0+maint.om/package.mo)
Running command: translateModel(ThermofluidStream.Boundaries.Tests.TankHeating,tolerance=1e-06,outputFormat="mat",numberOfIntervals=2500,variableFilter="CPUtime|EventCounter|NonlinearSystems.simulation.[0-9,]+..Calls|NonlinearSystems.simulation.[0-9,]+..Iterations|NonlinearSystems.simulation.[0-9,]+..Jacobians|NonlinearSystems.simulation.[0-9,]+..Residues|Time|_GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.H0|_GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.Hf|_GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.MM|_GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.R_s|_GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.Tlimit|_GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.ahigh.[0-9,]+.|_GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.alow.[0-9,]+.|_GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.bhigh.[0-9,]+.|_GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.blow.[0-9,]+.|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.H0|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.Hf|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.MM|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.R_s|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.Tlimit|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.ahigh.[0-9,]+.|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.alow.[0-9,]+.|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.bhigh.[0-9,]+.|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.blow.[0-9,]+.|acceleration.a.[0-9,]+.|acceleration.ax|acceleration.ay|acceleration.az|acceleration.setFromInputs|dropOfCommons.L|dropOfCommons.assertionLevel|dropOfCommons.g|dropOfCommons.instanceNameColor.[0-9,]+.|dropOfCommons.k_volume_damping|dropOfCommons.m_flow_reg|dropOfCommons.omega_reg|dropOfCommons.p_min|dropOfCommons.rho_min|fixedHeatFlow.Q_flow|fixedHeatFlow.T_ref|fixedHeatFlow.alpha|fixedHeatFlow.port.Q_flow|fixedHeatFlow.port.T|flowResistance.D_h|flowResistance.L|flowResistance.L_value|flowResistance.Xi_in.[0-9,]+.|flowResistance.Xi_out.[0-9,]+.|flowResistance.a|flowResistance.areaCross|flowResistance.areaCrossInput|flowResistance.areaHydraulic|flowResistance.b|flowResistance.clip_p_out|flowResistance.dp|flowResistance.dr_corr|flowResistance.h_in|flowResistance.h_out|flowResistance.initM_flow|der.flowResistance.inlet.m_flow.|flowResistance.inlet.m_flow|flowResistance.inlet.r|flowResistance.inlet.state.T|flowResistance.inlet.state.X.[0-9,]+.|flowResistance.inlet.state.p|flowResistance.l|flowResistance.m_acceleration_0|flowResistance.m_flow|flowResistance.m_flowStateSelect|flowResistance.m_flow_0|flowResistance.mu_in|flowResistance.outlet.m_flow|flowResistance.outlet.r|flowResistance.outlet.state.T|flowResistance.outlet.state.X.[0-9,]+.|flowResistance.outlet.state.p|flowResistance.p_in|flowResistance.p_min|flowResistance.p_out|flowResistance.perimeter|flowResistance.perimeterInput|flowResistance.r|flowResistance.rho_in|flowResistance.rho_min|flowResistance.shape|flowResistance1.D_h|flowResistance1.L|flowResistance1.L_value|flowResistance1.Xi_in.[0-9,]+.|flowResistance1.Xi_out.[0-9,]+.|flowResistance1.a|flowResistance1.areaCross|flowResistance1.areaCrossInput|flowResistance1.areaHydraulic|flowResistance1.b|flowResistance1.clip_p_out|flowResistance1.dp|flowResistance1.dr_corr|flowResistance1.h_in|flowResistance1.h_out|flowResistance1.initM_flow|der.flowResistance1.inlet.m_flow.|flowResistance1.inlet.m_flow|flowResistance1.inlet.r|flowResistance1.inlet.state.T|flowResistance1.inlet.state.X.[0-9,]+.|flowResistance1.inlet.state.p|flowResistance1.l|flowResistance1.m_acceleration_0|flowResistance1.m_flow|flowResistance1.m_flowStateSelect|flowResistance1.m_flow_0|flowResistance1.mu_in|flowResistance1.outlet.m_flow|flowResistance1.outlet.r|flowResistance1.outlet.state.T|flowResistance1.outlet.state.X.[0-9,]+.|flowResistance1.outlet.state.p|flowResistance1.p_in|flowResistance1.p_min|flowResistance1.p_out|flowResistance1.perimeter|flowResistance1.perimeterInput|flowResistance1.r|flowResistance1.rho_in|flowResistance1.rho_min|flowResistance1.shape|flowResistance2.D_h|flowResistance2.L|flowResistance2.L_value|flowResistance2.Xi_in.[0-9,]+.|flowResistance2.Xi_out.[0-9,]+.|flowResistance2.a|flowResistance2.areaCross|flowResistance2.areaCrossInput|flowResistance2.areaHydraulic|flowResistance2.b|flowResistance2.clip_p_out|flowResistance2.dp|flowResistance2.dr_corr|flowResistance2.h_in|flowResistance2.h_out|flowResistance2.initM_flow|der.flowResistance2.inlet.m_flow.|flowResistance2.inlet.m_flow|flowResistance2.inlet.r|flowResistance2.inlet.state.T|flowResistance2.inlet.state.X.[0-9,]+.|flowResistance2.inlet.state.p|flowResistanc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translateModel(ThermofluidStream.Boundaries.Tests.TankHeating,tolerance=1e-06,outputFormat="mat",numberOfIntervals=2500,variableFilter="CPUtime|EventCounter|NonlinearSystems.simulation.[0-9,]+..Calls|NonlinearSystems.simulation.[0-9,]+..Iterations|NonlinearSystems.simulation.[0-9,]+..Jacobians|NonlinearSystems.simulation.[0-9,]+..Residues|Time|_GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.H0|_GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.Hf|_GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.MM|_GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.R_s|_GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.Tlimit|_GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.ahigh.[0-9,]+.|_GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.alow.[0-9,]+.|_GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.bhigh.[0-9,]+.|_GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.blow.[0-9,]+.|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.H0|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.Hf|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.MM|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.R_s|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.Tlimit|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.ahigh.[0-9,]+.|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.alow.[0-9,]+.|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.bhigh.[0-9,]+.|_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.blow.[0-9,]+.|acceleration.a.[0-9,]+.|acceleration.ax|acceleration.ay|acceleration.az|acceleration.setFromInputs|dropOfCommons.L|dropOfCommons.assertionLevel|dropOfCommons.g|dropOfCommons.instanceNameColor.[0-9,]+.|dropOfCommons.k_volume_damping|dropOfCommons.m_flow_reg|dropOfCommons.omega_reg|dropOfCommons.p_min|dropOfCommons.rho_min|fixedHeatFlow.Q_flow|fixedHeatFlow.T_ref|fixedHeatFlow.alpha|fixedHeatFlow.port.Q_flow|fixedHeatFlow.port.T|flowResistance.D_h|flowResistance.L|flowResistance.L_value|flowResistance.Xi_in.[0-9,]+.|flowResistance.Xi_out.[0-9,]+.|flowResistance.a|flowResistance.areaCross|flowResistance.areaCrossInput|flowResistance.areaHydraulic|flowResistance.b|flowResistance.clip_p_out|flowResistance.dp|flowResistance.dr_corr|flowResistance.h_in|flowResistance.h_out|flowResistance.initM_flow|der.flowResistance.inlet.m_flow.|flowResistance.inlet.m_flow|flowResistance.inlet.r|flowResistance.inlet.state.T|flowResistance.inlet.state.X.[0-9,]+.|flowResistance.inlet.state.p|flowResistance.l|flowResistance.m_acceleration_0|flowResistance.m_flow|flowResistance.m_flowStateSelect|flowResistance.m_flow_0|flowResistance.mu_in|flowResistance.outlet.m_flow|flowResistance.outlet.r|flowResistance.outlet.state.T|flowResistance.outlet.state.X.[0-9,]+.|flowResistance.outlet.state.p|flowResistance.p_in|flowResistance.p_min|flowResistance.p_out|flowResistance.perimeter|flowResistance.perimeterInput|flowResistance.r|flowResistance.rho_in|flowResistance.rho_min|flowResistance.shape|flowResistance1.D_h|flowResistance1.L|flowResistance1.L_value|flowResistance1.Xi_in.[0-9,]+.|flowResistance1.Xi_out.[0-9,]+.|flowResistance1.a|flowResistance1.areaCross|flowResistance1.areaCrossInput|flowResistance1.areaHydraulic|flowResistance1.b|flowResistance1.clip_p_out|flowResistance1.dp|flowResistance1.dr_corr|flowResistance1.h_in|flowResistance1.h_out|flowResistance1.initM_flow|der.flowResistance1.inlet.m_flow.|flowResistance1.inlet.m_flow|flowResistance1.inlet.r|flowResistance1.inlet.state.T|flowResistance1.inlet.state.X.[0-9,]+.|flowResistance1.inlet.state.p|flowResistance1.l|flowResistance1.m_acceleration_0|flowResistance1.m_flow|flowResistance1.m_flowStateSelect|flowResistance1.m_flow_0|flowResistance1.mu_in|flowResistance1.outlet.m_flow|flowResistance1.outlet.r|flowResistance1.outlet.state.T|flowResistance1.outlet.state.X.[0-9,]+.|flowResistance1.outlet.state.p|flowResistance1.p_in|flowResistance1.p_min|flowResistance1.p_out|flowResistance1.perimeter|flowResistance1.perimeterInput|flowResistance1.r|flowResistance1.rho_in|flowResistance1.rho_min|flowResistance1.shape|flowResistance2.D_h|flowResistance2.L|flowResistance2.L_value|flowResistance2.Xi_in.[0-9,]+.|flowResistance2.Xi_out.[0-9,]+.|flowResistance2.a|flowResistance2.areaCross|flowResistance2.areaCrossInput|flowResistance2.areaHydraulic|flowResistance2.b|flowResistance2.clip_p_out|flowResistance2.dp|flowResistance2.dr_corr|flowResistance2.h_in|flowResistance2.h_out|flowResistance2.initM_flow|der.flowResistance2.inlet.m_flow.|flowResistance2.inlet.m_flow|flowResistance2.inlet.r|flowResistance2.inlet.state.T|flowResistance2.inlet.state.X.[0-9,]+.|flowResistance2.inlet.state.p|flowResistanc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.|tank.staticHeadOutlets_Pa_relative.[0-9,]+.|tank.tankCenter.[0-9,]+.|tank.useHeatport|tank.usePreferredMediumStates|tank.use_hstart|tank.xLength|tank.yLength|tank.zLength|tank1.A|tank1.Area|tank1.AxLimit|tank1.AzLimit|tank1.D|tank1.D1|tank1.D2|tank1.D3|tank1.D4|tank1.K|tank1.L|tank1.M|tank1.MXi.[0-9,]+.|tank1.M_liq_start|tank1.M_outlets|tank1.N_inlets|tank1.Q_flow|tank1.T_heatPort|tank1.T_start|tank1.ThresholdEmpty|tank1.ThresholdFull|tank1.U|tank1.U_med|tank1.V|tank1.V_liquid|tank1.V_ref|tank1.W_v|tank1.Xi_0.[0-9,]+.|tank1.Xi_in.[0-9,]+.|tank1.Xi_out.[0-9,]+.|tank1.centerOfMass.[0-9,]+.|tank1.d|tank1.density_derp_h|der.tank1.M.|der.tank1.MXi.[0-9,]+..|der.tank1.U_med.|tank1.eps_geometry|tank1.fEmpty|tank1.fFull|tank1.gasDensity|tank1.h_in.[0-9,]+.|tank1.h_out.[0-9,]+.|tank1.h_start|tank1.heatPort.Q_flow|tank1.heatPort.T|tank1.initialize_LiquidMass|tank1.initialize_Xi|tank1.initialize_energy|tank1.initialize_pressure|tank1.inletPositions.[0-9,]+.|der.tank1.inlet.[0-9,]+..m_flow.|tank1.inlet.[0-9,]+..m_flow|tank1.inlet.[0-9,]+..r|tank1.inlet.[0-9,]+..state.T|tank1.inlet.[0-9,]+..state.X.[0-9,]+.|tank1.inlet.[0-9,]+..state.p|tank1.k_volume_damping|tank1.liquidDensity|tank1.m_flow_assert|tank1.m_flow_in.[0-9,]+.|tank1.m_flow_out.[0-9,]+.|tank1.medium.MM|tank1.medium.R_s|tank1.medium.T|tank1.medium.T_degC|tank1.medium.X.[0-9,]+.|tank1.medium.Xi.[0-9,]+.|tank1.medium.d|tank1.medium.h|tank1.medium.p|tank1.medium.p_bar|tank1.medium.preferredMediumStates|tank1.medium.standardOrderComponents|tank1.medium.state.T|tank1.medium.state.X.[0-9,]+.|tank1.medium.state.p|tank1.medium.u|tank1.normAcc.[0-9,]+.|tank1.nx|tank1.nz|tank1.outletPositions.[0-9,]+.|tank1.outletTransition|der.tank1.outlet.[0-9,]+..m_flow.|tank1.outlet.[0-9,]+..m_flow|tank1.outlet.[0-9,]+..r|tank1.outlet.[0-9,]+..state.T|tank1.outlet.[0-9,]+..state.X.[0-9,]+.|tank1.outlet.[0-9,]+..state.p|tank1.p_in.[0-9,]+.|tank1.p_ref|tank1.p_start|tank1.r.[0-9,]+.|tank1.r_damping|tank1.shiftOutlet.[0-9,]+.|tank1.state_out.[0-9,]+..T|tank1.state_out.[0-9,]+..X.[0-9,]+.|tank1.state_out.[0-9,]+..p|tank1.staticHeadInlets.[0-9,]+.|tank1.staticHeadInlets_Pa_relative.[0-9,]+.|tank1.staticHeadOutlets.[0-9,]+.|tank1.staticHeadOutlets_Pa_relative.[0-9,]+.|tank1.tankCenter.[0-9,]+.|tank1.useHeatport|tank1.usePreferredMediumStates|tank1.use_hstart|tank1.xLength|tank1.yLength|tank1.zLength",fileNamePrefix="ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating") [Timeout 660]
"Notification: Performance of FrontEnd - loaded program: time 1.874e-06/1.874e-06, allocations: 1.281 kB / 483.7 MB, free: 8.203 MB / 410.7 MB
Notification: Performance of FrontEnd - Absyn->SCode: time 1.762e-05/1.95e-05, allocations: 4.984 kB / 483.7 MB, free: 8.199 MB / 410.7 MB
Notification: Performance of NFInst.instantiate(ThermofluidStream.Boundaries.Tests.TankHeating): time 0.133/0.133, allocations: 153.2 MB / 0.622 GB, free: 6.887 MB / 0.5417 GB
Notification: Performance of NFInst.instExpressions: time 0.00488/0.1379, allocations: 3.88 MB / 0.6258 GB, free: 2.996 MB / 0.5417 GB
Notification: Performance of NFInst.updateImplicitVariability: time 0.0007351/0.1386, allocations: 59.44 kB / 0.6258 GB, free: 2.938 MB / 0.5417 GB
Notification: Performance of NFTyping.typeComponents: time 0.0007194/0.1393, allocations: 325.3 kB / 0.6261 GB, free: 2.617 MB / 0.5417 GB
Notification: Performance of NFTyping.typeBindings: time 0.003232/0.1426, allocations: 2.004 MB / 0.6281 GB, free: 0.6016 MB / 0.5417 GB
Notification: Performance of NFTyping.typeClassSections: time 0.002141/0.1447, allocations: 1.219 MB / 0.6293 GB, free: 15.38 MB / 0.5573 GB
Notification: Performance of NFFlatten.flatten: time 0.002816/0.1475, allocations: 3.5 MB / 0.6327 GB, free: 11.87 MB / 0.5573 GB
Notification: Performance of NFFlatten.resolveConnections: time 0.0003493/0.1479, allocations: 236.5 kB / 0.6329 GB, free: 11.61 MB / 0.5573 GB
Notification: Performance of NFEvalConstants.evaluate: time 0.002771/0.1506, allocations: 2.12 MB / 0.635 GB, free: 9.484 MB / 0.5573 GB
Notification: Performance of NFSimplifyModel.simplify: time 0.001427/0.1521, allocations: 1.418 MB / 0.6364 GB, free: 8.062 MB / 0.5573 GB
Notification: Performance of NFPackage.collectConstants: time 0.0003214/0.1524, allocations: 204 kB / 0.6366 GB, free: 7.863 MB / 0.5573 GB
Notification: Performance of NFFlatten.collectFunctions: time 0.002491/0.1549, allocations: 1.81 MB / 0.6383 GB, free: 6.051 MB / 0.5573 GB
Notification: Performance of NFScalarize.scalarize: time 0.0005966/0.1555, allocations: 0.8453 MB / 0.6392 GB, free: 5.203 MB / 0.5573 GB
Notification: Performance of NFVerifyModel.verify: time 0.0008092/0.1563, allocations: 0.8146 MB / 0.64 GB, free: 4.387 MB / 0.5573 GB
Notification: Performance of NFConvertDAE.convert: time 0.002929/0.1592, allocations: 2.862 MB / 0.6428 GB, free: 1.516 MB / 0.5573 GB
Notification: Performance of FrontEnd - DAE generated: time 6.092e-06/0.1592, allocations: 4 kB / 0.6428 GB, free: 1.512 MB / 0.5573 GB
Notification: Performance of FrontEnd: time 1.402e-06/0.1592, allocations: 0 / 0.6428 GB, free: 1.512 MB / 0.5573 GB
Notification: Performance of Transformations before backend: time 2.232e-05/0.1592, allocations: 3.938 kB / 0.6428 GB, free: 1.508 MB / 0.5573 GB
Notification: Model statistics after passing the front-end and creating the data structures used by the back-end:
 * Number of equations: 350
 * Number of variables: 350
Notification: Performance of Generate backend data structure: time 0.2307/0.3899, allocations: 3.017 MB / 0.6457 GB, free: 34.85 MB / 0.5573 GB
Notification: Performance of prepare preOptimizeDAE: time 4.951e-05/0.39, allocations: 12 kB / 0.6457 GB, free: 34.85 MB / 0.5573 GB
Notification: Performance of preOpt normalInlineFunction (simulation): time 0.002161/0.3922, allocations: 0.6423 MB / 0.6464 GB, free: 34.73 MB / 0.5573 GB
Notification: Performance of preOpt evaluateParameters (simulation): time 0.002375/0.3945, allocations: 1.161 MB / 0.6475 GB, free: 34.42 MB / 0.5573 GB
Notification: Performance of preOpt simplifyIfEquations (simulation): time 0.000521/0.395, allocations: 1.012 MB / 0.6485 GB, free: 33.42 MB / 0.5573 GB
Notification: Performance of preOpt expandDerOperator (simulation): time 0.0002584/0.3953, allocations: 150.2 kB / 0.6486 GB, free: 33.41 MB / 0.5573 GB
Notification: Performance of preOpt clockPartitioning (simulation): time 0.00268/0.398, allocations: 2.113 MB / 0.6507 GB, free: 32.57 MB / 0.5573 GB
Notification: Performance of preOpt findStateOrder (simulation): time 2.176e-05/0.398, allocations: 0.875 kB / 0.6507 GB, free: 32.57 MB / 0.5573 GB
Notification: Performance of preOpt replaceEdgeChange (simulation): time 0.0001306/0.3981, allocations: 59.61 kB / 0.6507 GB, free: 32.57 MB / 0.5573 GB
Notification: Performance of preOpt inlineArrayEqn (simulation): time 0.000304/0.3984, allocations: 191.1 kB / 0.6509 GB, free: 32.57 MB / 0.5573 GB
Notification: Performance of preOpt removeEqualRHS (simulation): time 0.001782/0.4002, allocations: 1.207 MB / 0.6521 GB, free: 32.54 MB / 0.5573 GB
Notification: Performance of preOpt removeSimpleEquations (simulation): time 0.006902/0.4071, allocations: 6.4 MB / 0.6584 GB, free: 30.39 MB / 0.5573 GB
Notification: Performance of preOpt comSubExp (simulation): time 0.001556/0.4087, allocations: 1.032 MB / 0.6594 GB, free: 30.34 MB / 0.5573 GB
Notification: Performance of preOpt resolveLoops (simulation): time 0.0007982/0.4095, allocations: 0.6069 MB / 0.66 GB, free: 30.32 MB / 0.5573 GB
Notification: Performance of preOpt evalFunc (simulation): time 0.0002431/0.4097, allocations: 117.8 kB / 0.6601 GB, free: 30.32 MB / 0.5573 GB
Notification: Performance of preOpt encapsulateWhenConditions (simulation): time 3.381e-05/0.4098, allocations: 62.52 kB / 0.6601 GB, free: 30.28 MB / 0.5573 GB
Notification: Performance of pre-optimization done (n=187): time 3.166e-06/0.4098, allocations: 0 / 0.6601 GB, free: 30.28 MB / 0.5573 GB
Notification: Performance of matching and sorting (n=187): time 0.004166/0.4139, allocations: 2.461 MB / 0.6625 GB, free: 30.01 MB / 0.5573 GB
Notification: Performance of inlineWhenForInitialization (initialization): time 3.118e-05/0.414, allocations: 69.34 kB / 0.6626 GB, free: 29.95 MB / 0.5573 GB
Notification: Performance of selectInitializationVariablesDAE (initialization): time 0.0008303/0.4148, allocations: 0.9233 MB / 0.6635 GB, free: 29.74 MB / 0.5573 GB
Notification: Performance of collectPreVariables (initialization): time 0.0001401/0.4149, allocations: 59.3 kB / 0.6636 GB, free: 29.71 MB / 0.5573 GB
Notification: Performance of collectInitialEqns (initialization): time 0.0003585/0.4153, allocations: 0.6744 MB / 0.6642 GB, free: 29.48 MB / 0.5573 GB
Notification: Performance of collectInitialBindings (initialization): time 0.0003985/0.4157, allocations: 0.6645 MB / 0.6649 GB, free: 29.12 MB / 0.5573 GB
Notification: Performance of simplifyInitialFunctions (initialization): time 0.0005319/0.4162, allocations: 351.8 kB / 0.6652 GB, free: 29.09 MB / 0.5573 GB
Notification: Performance of setup shared object (initialization): time 3.831e-05/0.4163, allocations: 476.8 kB / 0.6657 GB, free: 28.62 MB / 0.5573 GB
Notification: Performance of preBalanceInitialSystem (initialization): time 0.0009016/0.4172, allocations: 492 kB / 0.6661 GB, free: 28.62 MB / 0.5573 GB
Notification: Performance of partitionIndependentBlocks (initialization): time 0.001164/0.4183, allocations: 1.217 MB / 0.6673 GB, free: 27.81 MB / 0.5573 GB
Notification: Performance of analyzeInitialSystem (initialization): time 0.002695/0.421, allocations: 1.682 MB / 0.669 GB, free: 27.63 MB / 0.5573 GB
Notification: Performance of solveInitialSystemEqSystem (initialization): time 5.801e-06/0.421, allocations: 1.906 kB / 0.669 GB, free: 27.63 MB / 0.5573 GB
Notification: Performance of matching and sorting (n=210) (initialization): time 0.002818/0.4238, allocations: 1.758 MB / 0.6707 GB, free: 27.4 MB / 0.5573 GB
Notification: Performance of prepare postOptimizeDAE: time 2.181e-05/0.4239, allocations: 6.156 kB / 0.6707 GB, free: 27.4 MB / 0.5573 GB
Notification: Performance of postOpt simplifyComplexFunction (initialization): time 9.418e-06/0.4239, allocations: 2.594 kB / 0.6707 GB, free: 27.4 MB / 0.5573 GB
Notification: Performance of postOpt tearingSystem (initialization): time 0.0004911/0.4244, allocations: 194.2 kB / 0.6709 GB, free: 27.34 MB / 0.5573 GB
Notification: Performance of postOpt solveSimpleEquations (initialization): time 0.001024/0.4254, allocations: 380.4 kB / 0.6712 GB, free: 27.34 MB / 0.5573 GB
Notification: Performance of postOpt calculateStrongComponentJacobians (initialization): time 0.002583/0.428, allocations: 8.938 MB / 0.68 GB, free: 18.71 MB / 0.5573 GB
Notification: Performance of postOpt simplifyAllExpressions (initialization): time 0.001198/0.4292, allocations: 361.5 kB / 0.6803 GB, free: 18.64 MB / 0.5573 GB
Notification: Performance of postOpt collapseArrayExpressions (initialization): time 0.0001726/0.4293, allocations: 119.9 kB / 0.6804 GB, free: 18.64 MB / 0.5573 GB
Warning: Assuming fixed start value for the following 4 variables:
         staticHead.inlet.m_flow:VARIABLE(flow=true min = -1e5 max = 1e5 unit = \"kg/s\" fixed = true )  \"Mass flow rate\" type: Real
         flowResistance3.inlet.m_flow:VARIABLE(flow=true min = -1e5 max = 1e5 unit = \"kg/s\" fixed = true )  \"Mass flow rate\" type: Real
         flowResistance1.inlet.m_flow:VARIABLE(flow=true min = -1e5 max = 1e5 unit = \"kg/s\" fixed = true )  \"Mass flow rate\" type: Real
         flowResistance.inlet.m_flow:VARIABLE(flow=true min = -1e5 max = 1e5 unit = \"kg/s\" fixed = true )  \"Mass flow rate\" type: Real
Notification: Model statistics after passing the back-end for initialization:
 * Number of independent subsystems: 10
 * Number of states: 0 ()
 * Number of discrete variables: 4 (tank1.fEmpty,tank1.fFull,tank.fEmpty,tank.fFull)
 * Number of discrete states: 0 ()
 * Number of clocked states: 0 ()
 * Top-level inputs: 0
Notification: Strong component statistics for initialization (179):
 * Single equations (assignments): 163
 * Array equations: 7
 * Algorithm blocks: 0
 * Record equations: 4
 * When equations: 0
 * If-equations: 0
 * Equation systems (not torn): 0
 * Torn equation systems: 5
 * Mixed (continuous/discrete) equation systems: 0
Notification: Torn system details for strict tearing set:
 * Linear torn systems (#iteration vars, #inner vars, density): 5 systems
   {(1,3,100.0%), (1,2,100.0%), (1,2,100.0%), (1,2,100.0%), (1,1,100.0%)}
 * Non-linear torn systems (#iteration vars, #inner vars): 0 systems
Notification: Performance of prepare postOptimizeDAE: time 0.0004626/0.4298, allocations: 266.9 kB / 0.6807 GB, free: 18.48 MB / 0.5573 GB
Notification: Performance of postOpt lateInlineFunction (simulation): time 0.000293/0.4301, allocations: 219.2 kB / 0.6809 GB, free: 18.39 MB / 0.5573 GB
Notification: Performance of postOpt wrapFunctionCalls (simulation): time 0.003292/0.4334, allocations: 2.943 MB / 0.6838 GB, free: 18.04 MB / 0.5573 GB
Notification: Performance of postOpt inlineArrayEqn (simulation): time 0.002026/0.4354, allocations: 1.543 MB / 0.6853 GB, free: 17.87 MB / 0.5573 GB
Notification: Performance of postOpt constantLinearSystem (simulation): time 3.797e-06/0.4354, allocations: 0 / 0.6853 GB, free: 17.87 MB / 0.5573 GB
Notification: Performance of postOpt simplifysemiLinear (simulation): time 1.299e-05/0.4354, allocations: 12.45 kB / 0.6853 GB, free: 17.87 MB / 0.5573 GB
Notification: Performance of postOpt removeSimpleEquations (simulation): time 0.004565/0.44, allocations: 3.732 MB / 0.6889 GB, free: 17.3 MB / 0.5573 GB
Notification: Performance of postOpt simplifyComplexFunction (simulation): time 5.17e-06/0.44, allocations: 0 / 0.6889 GB, free: 17.3 MB / 0.5573 GB
Notification: Performance of postOpt solveSimpleEquations (simulation): time 0.0008795/0.4409, allocations: 367.5 kB / 0.6893 GB, free: 17.3 MB / 0.5573 GB
Notification: Performance of postOpt tearingSystem (simulation): time 0.0009065/0.4418, allocations: 414.4 kB / 0.6897 GB, free: 17.2 MB / 0.5573 GB
Notification: Performance of postOpt inputDerivativesUsed (simulation): time 0.0001418/0.4419, allocations: 79.09 kB / 0.6897 GB, free: 17.2 MB / 0.5573 GB
Notification: Performance of postOpt calculateStrongComponentJacobians (simulation): time 0.002665/0.4446, allocations: 10.6 MB / 0.7001 GB, free: 22.94 MB / 0.573 GB
Notification: Performance of postOpt calculateStateSetsJacobians (simulation): time 1.343e-06/0.4446, allocations: 2.625 kB / 0.7001 GB, free: 22.94 MB / 0.573 GB
Notification: Performance of postOpt symbolicJacobian (simulation): time 0.003377/0.448, allocations: 2.607 MB / 0.7026 GB, free: 22.5 MB / 0.573 GB
Notification: Performance of postOpt removeConstants (simulation): time 0.0005287/0.4485, allocations: 472 kB / 0.7031 GB, free: 22.38 MB / 0.573 GB
Notification: Performance of postOpt simplifyTimeIndepFuncCalls (simulation): time 0.0001793/0.4487, allocations: 42.81 kB / 0.7031 GB, free: 22.38 MB / 0.573 GB
Notification: Performance of postOpt simplifyAllExpressions (simulation): time 0.0007831/0.4495, allocations: 139.9 kB / 0.7033 GB, free: 22.38 MB / 0.573 GB
Notification: Performance of postOpt findZeroCrossings (simulation): time 0.0003474/0.4498, allocations: 242.5 kB / 0.7035 GB, free: 22.38 MB / 0.573 GB
Notification: Performance of postOpt collapseArrayExpressions (simulation): time 0.000157/0.45, allocations: 124.2 kB / 0.7036 GB, free: 22.38 MB / 0.573 GB
Notification: Performance of sorting global known variables: time 0.0004837/0.4505, allocations: 0.6127 MB / 0.7042 GB, free: 22.22 MB / 0.573 GB
Notification: Performance of sort global known variables: time 7e-08/0.4505, allocations: 1.094 kB / 0.7042 GB, free: 22.22 MB / 0.573 GB
Notification: Performance of remove unused functions: time 0.00146/0.4519, allocations: 0.7764 MB / 0.705 GB, free: 22.13 MB / 0.573 GB
Notification: Model statistics after passing the back-end for simulation:
 * Number of independent subsystems: 1
 * Number of states: 12 (tank.M,tank.MXi[1],tank.MXi[2],tank.U_med,flowResistance.inlet.m_flow,flowResistance1.inlet.m_flow,tank1.M,tank1.MXi[1],tank1.MXi[2],tank1.U_med,flowResistance3.inlet.m_flow,staticHead.inlet.m_flow)
 * Number of discrete variables: 4 (tank.fFull,tank.fEmpty,tank1.fFull,tank1.fEmpty)
 * Number of discrete states: 0 ()
 * Number of clocked states: 0 ()
 * Top-level inputs: 0
Notification: Strong component statistics for simulation (171):
 * Single equations (assignments): 153
 * Array equations: 7
 * Algorithm blocks: 0
 * Record equations: 4
 * When equations: 0
 * If-equations: 0
 * Equation systems (not torn): 0
 * Torn equation systems: 7
 * Mixed (continuous/discrete) equation systems: 0
Notification: Torn system details for strict tearing set:
 * Linear torn systems (#iteration vars, #inner vars, density): 5 systems
   {(1,2,100.0%), (1,2,100.0%), (1,3,100.0%), (1,2,100.0%), (1,1,100.0%)}
 * Non-linear torn systems (#iteration vars, #inner vars): 2 systems
   {(2,3), (2,3)}
Notification: Performance of Backend phase and start with SimCode phase: time 0.0007119/0.4526, allocations: 472.5 kB / 0.7054 GB, free: 22.01 MB / 0.573 GB
Notification: Performance of simCode: created initialization part: time 0.002521/0.4551, allocations: 2.42 MB / 0.7078 GB, free: 21.03 MB / 0.573 GB
Notification: Performance of simCode: created event and clocks part: time 3.306e-06/0.4551, allocations: 0.9375 kB / 0.7078 GB, free: 21.03 MB / 0.573 GB
Notification: Performance of simCode: created simulation system equations: time 0.001535/0.4567, allocations: 1.874 MB / 0.7096 GB, free: 20.08 MB / 0.573 GB
Notification: Performance of simCode: created of all other equations (e.g. parameter, nominal, assert, etc): time 0.001678/0.4584, allocations: 0.8017 MB / 0.7104 GB, free: 20 MB / 0.573 GB
Notification: Performance of simCode: created linear, non-linear and system jacobian parts: time 0.004425/0.4628, allocations: 3.659 MB / 0.714 GB, free: 18.62 MB / 0.573 GB
Notification: Performance of simCode: some other stuff during SimCode phase: time 0.0002731/0.4631, allocations: 417 kB / 0.7144 GB, free: 18.51 MB / 0.573 GB
Notification: Performance of simCode: alias equations: time 0.00116/0.4642, allocations: 0.5592 MB / 0.7149 GB, free: 18.35 MB / 0.573 GB
Notification: Performance of simCode: all other stuff during SimCode phase: time 0.0006528/0.4649, allocations: 227.9 kB / 0.7151 GB, free: 18.34 MB / 0.573 GB
Notification: Performance of SimCode: time 1.884e-06/0.4649, allocations: 0 / 0.7151 GB, free: 18.34 MB / 0.573 GB
Notification: Performance of Templates: time 0.05489/0.5198, allocations: 53.37 MB / 0.7672 GB, free: 12.22 MB / 0.6042 GB
"
[Timeout remaining time 659]
make -j1 -f ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating.makefile [Timeout 660]
(rm -f ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating.pipe ; mkfifo ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating.pipe ; head -c 1048576 < ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating.pipe >> ../files/ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating.sim & ./ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating -abortSlowSimulation -alarm=240  -emit_protected -lv LOG_STATS > ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating.pipe 2>&1) [Timeout 240]
diffSimulationResults("ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat","/mnt/ReferenceFiles/ThermofluidStream-main-regression/ReferenceData/ThermofluidStream.Boundaries.Tests.TankHeating_ref.mat","",relTol=0.003,relTolDiffMinMax=0.003,rangeDelta=0.001) [Timeout 660]
"Error: Could not read variable CPUtime in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat.
Warning: Get data of variable CPUtime from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat failed!
Error: Could not read variable EventCounter in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat.
Warning: Get data of variable EventCounter from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat failed!
Error: Could not read variable NonlinearSystems.simulation[1].Calls in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat.
Warning: Get data of variable NonlinearSystems.simulation[1].Calls from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat failed!
Error: Could not read variable NonlinearSystems.simulation[1].Iterations in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat.
Warning: Get data of variable NonlinearSystems.simulation[1].Iterations from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat failed!
Error: Could not read variable NonlinearSystems.simulation[1].Jacobians in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat.
Warning: Get data of variable NonlinearSystems.simulation[1].Jacobians from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat failed!
Error: Could not read variable NonlinearSystems.simulation[1].Residues in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat.
Warning: Get data of variable NonlinearSystems.simulation[1].Residues from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat failed!
Error: Could not read variable NonlinearSystems.simulation[2].Calls in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat.
Warning: Get data of variable NonlinearSystems.simulation[2].Calls from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat failed!
Error: Could not read variable NonlinearSystems.simulation[2].Iterations in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat.
Warning: Get data of variable NonlinearSystems.simulation[2].Iterations from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat failed!
Error: Could not read variable NonlinearSystems.simulation[2].Jacobians in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat.
Warning: Get data of variable NonlinearSystems.simulation[2].Jacobians from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat failed!
Error: Could not read variable NonlinearSystems.simulation[2].Residues in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat.
Warning: Get data of variable NonlinearSystems.simulation[2].Residues from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat failed!
Error: Could not read variable _GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.H0 in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat.
Warning: Get data of variable _GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.H0 from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat failed!
Error: Could not read variable _GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.Hf in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat.
Warning: Get data of variable _GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.Hf from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat failed!
Error: Could not read variable _GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.MM in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat.
Warning: Get data of variable _GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.MM from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat failed!
Error: Could not read variable _GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.R_s in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat.
Warning: Get data of variable _GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.R_s from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat failed!
Error: Could not read variable _GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.Tlimit in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat.
Warning: Get data of variable _GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.Tlimit from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat failed!
Error: Could not read variable _GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.ahigh[1] in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat.
Warning: Get data of variable _GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.ahigh[1] from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat failed!
Error: Could not read variable _GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.ahigh[2] in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat.
Warning: Get data of variable _GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.ahigh[2] from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat failed!
Error: Could not read variable _GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.ahigh[3] in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat.
Warning: Get data of variable _GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.ahigh[3] from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat failed!
Error: Could not read variable _GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.ahigh[4] in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat.
Warning: Get data of variable _GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.ahigh[4] from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat failed!
Error: Could not read variable _GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.ahigh[5] in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat.
Warning: Get data of variable _GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.ahigh[5] from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat failed!
Error: Could not read variable _GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.ahigh[6] in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat.
Warning: Get data of variable _GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.ahigh[6] from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat failed!
Error: Could not read variable _GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.ahigh[7] in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat.
Warning: Get data of variable _GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.ahigh[7] from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat failed!
Error: Could not read variable _GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.alow[1] in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat.
Warning: Get data of variable _GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.alow[1] from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat failed!
Error: Could not read variable _GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.alow[2] in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat.
Warning: Get data of variable _GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.alow[2] from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat failed!
Error: Could not read variable _GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.alow[3] in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat.
Warning: Get data of variable _GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.alow[3] from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat failed!
Error: Could not read variable _GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.alow[4] in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat.
Warning: Get data of variable _GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.alow[4] from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat failed!
Error: Could not read variable _GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.alow[5] in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat.
Warning: Get data of variable _GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.alow[5] from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat failed!
Error: Could not read variable _GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.alow[6] in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat.
Warning: Get data of variable _GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.alow[6] from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat failed!
Error: Could not read variable _GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.alow[7] in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat.
Warning: Get data of variable _GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.alow[7] from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat failed!
Error: Could not read variable _GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.bhigh[1] in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat.
Warning: Get data of variable _GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.bhigh[1] from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat failed!
Error: Could not read variable _GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.bhigh[2] in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat.
Warning: Get data of variable _GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.bhigh[2] from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat failed!
Error: Could not read variable _GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.blow[1] in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat.
Warning: Get data of variable _GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.blow[1] from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat failed!
Error: Could not read variable _GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.blow[2] in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat.
Warning: Get data of variable _GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.blow[2] from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat failed!
Error: Could not read variable _GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.H0 in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat.
Warning: Get data of variable _GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.H0 from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat failed!
Error: Could not read variable _GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.Hf in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat.
Warning: Get data of variable _GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.Hf from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat failed!
Error: Could not read variable _GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.MM in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat.
Warning: Get data of variable _GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.MM from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat failed!
Error: Could not read variable _GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.R_s in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat.
Warning: Get data of variable _GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.R_s from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat failed!
Error: Could not read variable _GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.Tlimit in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat.
Warning: Get data of variable _GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.Tlimit from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat failed!
Error: Could not read variable _GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.ahigh[1] in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat.
Warning: Get data of variable _GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.ahigh[1] from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat failed!
Error: Could not read variable _GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.ahigh[2] in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat.
Warning: Get data of variable _GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.ahigh[2] from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat failed!
Error: Could not read variable _GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.ahigh[3] in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat.
Warning: Get data of variable _GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.ahigh[3] from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat failed!
Error: Could not read variable _GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.ahigh[4] in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat.
Warning: Get data of variable _GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.ahigh[4] from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat failed!
Error: Could not read variable _GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.ahigh[5] in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat.
Warning: Get data of variable _GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.ahigh[5] from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat failed!
Error: Could not read variable _GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.ahigh[6] in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat.
Warning: Get data of variable _GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.ahigh[6] from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat failed!
Error: Could not read variable _GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.ahigh[7] in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat.
Warning: Get data of variable _GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.ahigh[7] from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat failed!
Error: Could not read variable _GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.alow[1] in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat.
Warning: Get data of variable _GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.alow[1] from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat failed!
Error: Could not read variable _GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.alow[2] in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat.
Warning: Get data of variable _GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.alow[2] from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat failed!
Error: Could not read variable _GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.alow[3] in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat.
Warning: Get data of variable _GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.alow[3] from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat failed!
Error: Could not read variable _GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.alow[4] in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat.
Warning: Get data of variable _GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.alow[4] from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat failed!
Error: Could not read variable _GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.alow[5] in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat.
Warning: Get data of variable _GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.alow[5] from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat failed!
Error: Could not read variable _GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.alow[6] in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat.
Warning: Get data of variable _GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.alow[6] from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat failed!
Error: Could not read variable _GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.alow[7] in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat.
Warning: Get data of variable _GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.alow[7] from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat failed!
Error: Could not read variable _GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.bhigh[1] in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat.
Warning: Get data of variable _GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.bhigh[1] from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat failed!
Error: Could not read variable _GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.bhigh[2] in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat.
Warning: Get data of variable _GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.bhigh[2] from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat failed!
Error: Could not read variable _GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.blow[1] in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat.
Warning: Get data of variable _GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.blow[1] from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat failed!
Error: Could not read variable _GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.blow[2] in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat.
Warning: Get data of variable _GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.blow[2] from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat failed!
Error: Could not read variable dropOfCommons.instanceNameColor[1] in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat.
Warning: Get data of variable dropOfCommons.instanceNameColor[1] from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat failed!
Error: Could not read variable dropOfCommons.instanceNameColor[2] in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat.
Warning: Get data of variable dropOfCommons.instanceNameColor[2] from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat failed!
Error: Could not read variable dropOfCommons.instanceNameColor[3] in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat.
Warning: Get data of variable dropOfCommons.instanceNameColor[3] from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat failed!
Error: Could not read variable tank.inlet[1].der(m_flow) in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat.
Warning: Get data of variable tank.inlet[1].der(m_flow) from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat failed!
Error: Could not read variable tank.inlet[2].der(m_flow) in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat.
Warning: Get data of variable tank.inlet[2].der(m_flow) from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat failed!
Error: Could not read variable tank.outlet[1].der(m_flow) in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat.
Warning: Get data of variable tank.outlet[1].der(m_flow) from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat failed!
Error: Could not read variable tank1.outlet[1].der(m_flow) in file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat.
Warning: Get data of variable tank1.outlet[1].der(m_flow) from file ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat failed!
"
[Timeout remaining time 660]
""

Variables in the reference:CPUtime,EventCounter,NonlinearSystems.simulation[1].Calls,NonlinearSystems.simulation[1].Iterations,NonlinearSystems.simulation[1].Jacobians,NonlinearSystems.simulation[1].Residues,NonlinearSystems.simulation[2].Calls,NonlinearSystems.simulation[2].Iterations,NonlinearSystems.simulation[2].Jacobians,NonlinearSystems.simulation[2].Residues,Time,_GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.H0,_GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.Hf,_GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.MM,_GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.R_s,_GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.Tlimit,_GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.ahigh[1],_GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.ahigh[2],_GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.ahigh[3],_GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.ahigh[4],_GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.ahigh[5],_GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.ahigh[6],_GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.ahigh[7],_GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.alow[1],_GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.alow[2],_GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.alow[3],_GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.alow[4],_GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.alow[5],_GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.alow[6],_GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.alow[7],_GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.bhigh[1],_GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.bhigh[2],_GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.blow[1],_GlobalScope.ThermofluidStream.Media.myMedia.Air.DryAirNasa.data.blow[2],_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.H0,_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.Hf,_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.MM,_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.R_s,_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.Tlimit,_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.ahigh[1],_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.ahigh[2],_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.ahigh[3],_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.ahigh[4],_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.ahigh[5],_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.ahigh[6],_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.ahigh[7],_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.alow[1],_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.alow[2],_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.alow[3],_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.alow[4],_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.alow[5],_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.alow[6],_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.alow[7],_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.bhigh[1],_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.bhigh[2],_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.blow[1],_GlobalScope.ThermofluidStream.Media.myMedia.IdealGases.Common.SingleGasesData.Air.blow[2],acceleration.a[1],acceleration.a[2],acceleration.a[3],acceleration.ax,acceleration.ay,acceleration.az,acceleration.setFromInputs,dropOfCommons.L,dropOfCommons.assertionLevel,dropOfCommons.g,dropOfCommons.instanceNameColor[1],dropOfCommons.instanceNameColor[2],dropOfCommons.instanceNameColor[3],dropOfCommons.k_volume_damping,dropOfCommons.m_flow_reg,dropOfCommons.omega_reg,dropOfCommons.p_min,dropOfCommons.rho_min,fixedHeatFlow.Q_flow,fixedHeatFlow.T_ref,fixedHeatFlow.alpha,fixedHeatFlow.port.Q_flow,fixedHeatFlow.port.T,flowResistance.D_h,flowResistance.L,flowResistance.L_value,flowResistance.Xi_in[1],flowResistance.Xi_in[2],flowResistance.Xi_out[1],flowResistance.Xi_out[2],flowResistance.a,flowResistance.areaCross,flowResistance.areaCrossInput,flowResistance.areaHydraulic,flowResistance.b,flowResistance.clip_p_out,flowResistance.dp,flowResistance.dr_corr,flowResistance.h_in,flowResistance.h_out,flowResistance.initM_flow,der(flowResistance.inlet.m_flow),flowResistance.inlet.m_flow,flowResistance.inlet.r,flowResistance.inlet.state.T,flowResistance.inlet.state.X[1],flowResistance.inlet.state.X[2],flowResistance.inlet.state.p,flowResistance.l,flowResistance.m_acceleration_0,flowResistance.m_flow,flowResistance.m_flowStateSelect,flowResistance.m_flow_0,flowResistance.mu_in,flowResistance.outlet.m_flow,flowResistance.outlet.r,flowResistance.outlet.state.T,flowResistance.outlet.state.X[1],flowResistance.outlet.state.X[2],flowResistance.outlet.state.p,flowResistance.p_in,flowResistance.p_min,flowResistance.p_out,flowResistance.perimeter,flowResistance.perimeterInput,flowResistance.r,flowResistance.rho_in,flowResistance.rho_min,flowResistance.shape,flowResistance1.D_h,flowResistance1.L,flowResistance1.L_value,flowResistance1.Xi_in[1],flowResistance1.Xi_in[2],flowResistance1.Xi_out[1],flowResistance1.Xi_out[2],flowResistance1.a,flowResistance1.areaCross,flowResistance1.areaCrossInput,flowResistance1.areaHydraulic,flowResistance1.b,flowResistance1.clip_p_out,flowResistance1.dp,flowResistance1.dr_corr,flowResistance1.h_in,flowResistance1.h_out,flowResistance1.initM_flow,der(flowResistance1.inlet.m_flow),flowResistance1.inlet.m_flow,flowResistance1.inlet.r,flowResistance1.inlet.state.T,flowResistance1.inlet.state.X[1],flowResistance1.inlet.state.X[2],flowResistance1.inlet.state.p,flowResistance1.l,flowResistance1.m_acceleration_0,flowResistance1.m_flow,flowResistance1.m_flowStateSelect,flowResistance1.m_flow_0,flowResistance1.mu_in,flowResistance1.outlet.m_flow,flowResistance1.outlet.r,flowResistance1.outlet.state.T,flowResistance1.outlet.state.X[1],flowResistance1.outlet.state.X[2],flowResistance1.outlet.state.p,flowResistance1.p_in,flowResistance1.p_min,flowResistance1.p_out,flowResistance1.perimeter,flowResistance1.perimeterInput,flowResistance1.r,flowResistance1.rho_in,flowResistance1.rho_min,flowResistance1.shape,flowResistance2.D_h,flowResistance2.L,flowResistance2.L_value,flowResistance2.Xi_in[1],flowResistance2.Xi_in[2],flowResistance2.Xi_out[1],flowResistance2.Xi_out[2],flowResistance2.a,flowResistance2.areaCross,flowResistance2.areaCrossInput,flowResistance2.areaHydraulic,flowResistance2.b,flowResistance2.clip_p_out,flowResistance2.dp,flowResistance2.dr_corr,flowResistance2.h_in,flowResistance2.h_out,flowResistance2.initM_flow,der(flowResistance2.inlet.m_flow),flowResistance2.inlet.m_flow,flowResistance2.inlet.r,flowResistance2.inlet.state.T,flowResistance2.inlet.state.X[1],flowResistance2.inlet.state.X[2],flowResistance2.inlet.state.p,flowResistance2.l,flowResistance2.m_acceleration_0,flowResistance2.m_flow,flowResistance2.m_flowStateSelect,flowResistance2.m_flow_0,flowResistance2.mu_in,flowResistance2.outlet.m_flow,flowResistance2.outlet.r,flowResistance2.outlet.state.T,flowResistance2.outlet.state.X[1],flowResistance2.outlet.state.X[2],flowResistance2.outlet.state.p,flowResistance2.p_in,flowResistance2.p_min,flowResistance2.p_out,flowResistance2.perimeter,flowResistance2.perimeterInput,flowResistance2.r,flowResistance2.rho_in,flowResistance2.rho_min,flowResistance2.shape,flowResistance3.D_h,flowResistance3.L,flowResistance3.L_value,flowResistance3.Xi_in[1],flowResistance3.Xi_in[2],flowResistance3.Xi_out[1],flowResistance3.Xi_out[2],flowResistance3.a,flowResistance3.areaCross,flowResistance3.areaCrossInput,flowResistance3.areaHydraulic,flowResistance3.b,flowResistance3.clip_p_out,flowResistance3.dp,flowResistance3.dr_corr,flowResistance3.h_in,flowResistance3.h_out,flowResistance3.initM_flow,der(flowResistance3.inlet.m_flow),flowResistance3.inlet.m_flow,flowResistance3.inlet.r,flowResistance3.inlet.state.T,flowResistance3.inlet.state.X[1],flowResistance3.inlet.state.X[2],flowResistance3.inlet.state.p,flowResistance3.l,flowResistance3.m_acceleration_0,flowResistance3.m_flow,flowResistance3.m_flowStateSelect,flowResistance3.m_flow_0,flowResistance3.mu_in,flowResistance3.outlet.m_flow,flowResistance3.outlet.r,flowResistance3.outlet.state.T,flowResistance3.outlet.state.X[1],flowResistance3.outlet.state.X[2],flowResistance3.outlet.state.p,flowResistance3.p_in,flowResistance3.p_min,flowResistance3.p_out,flowResistance3.perimeter,flowResistance3.perimeterInput,flowResistance3.r,flowResistance3.rho_in,flowResistance3.rho_min,flowResistance3.shape,sink1.L,der(sink1.inlet.m_flow),sink1.inlet.m_flow,sink1.inlet.r,sink1.inlet.state.T,sink1.inlet.state.X[1],sink1.inlet.state.X[2],sink1.inlet.state.p,sink1.p,sink1.p0,sink1.p0_par,sink1.r,source.L,source.T0,source.T0_par,source.Xi0[1],source.Xi0[2],source.Xi0_par[1],source.Xi0_par[2],source.h0,source.h0_par,der(source.outlet.m_flow),source.outlet.m_flow,source.outlet.r,source.outlet.state.T,source.outlet.state.X[1],source.outlet.state.X[2],source.outlet.state.p,source.p0,source.p0_par,source1.L,source1.T0,source1.T0_par,source1.Xi0[1],source1.Xi0[2],source1.Xi0_par[1],source1.Xi0_par[2],source1.h0,source1.h0_par,der(source1.outlet.m_flow),source1.outlet.m_flow,source1.outlet.r,source1.outlet.state.T,source1.outlet.state.X[1],source1.outlet.state.X[2],source1.outlet.state.p,source1.p0,source1.p0_par,staticHead.L,staticHead.L_value,staticHead.Xi_in[1],staticHead.Xi_in[2],staticHead.Xi_out[1],staticHead.Xi_out[2],staticHead.clip_p_out,staticHead.displayPositions,staticHead.dp,staticHead.dr_corr,staticHead.fromPosition[1],staticHead.fromPosition[2],staticHead.fromPosition[3],staticHead.h_in,staticHead.h_out,staticHead.initM_flow,der(staticHead.inlet.m_flow),staticHead.inlet.m_flow,staticHead.inlet.r,staticHead.inlet.state.T,staticHead.inlet.state.X[1],staticHead.inlet.state.X[2],staticHead.inlet.state.p,staticHead.m_acceleration_0,staticHead.m_flow,staticHead.m_flowStateSelect,staticHead.m_flow_0,staticHead.outlet.m_flow,staticHead.outlet.r,staticHead.outlet.state.T,staticHead.outlet.state.X[1],staticHead.outlet.state.X[2],staticHead.outlet.state.p,staticHead.p_in,staticHead.p_min,staticHead.p_out,staticHead.rho_in,staticHead.rho_min,staticHead.staticHead,staticHead.staticHead_Pa_relative,staticHead.toPosition[1],staticHead.toPosition[2],staticHead.toPosition[3],tank.A,tank.Area,tank.AxLimit,tank.AzLimit,tank.D,tank.D1,tank.D2,tank.D3,tank.D4,tank.K,tank.L,tank.M,tank.MXi[1],tank.MXi[2],tank.M_liq_start,tank.M_outlets,tank.N_inlets,tank.Q_flow,tank.T_heatPort,tank.T_start,tank.ThresholdEmpty,tank.ThresholdFull,tank.U,tank.U_med,tank.V,tank.V_liquid,tank.V_ref,tank.W_v,tank.Xi_0[1],tank.Xi_0[2],tank.Xi_in[1,1],tank.Xi_in[1,2],tank.Xi_in[2,1],tank.Xi_in[2,2],tank.Xi_out[1,1],tank.Xi_out[2,1],tank.centerOfMass[1],tank.centerOfMass[2],tank.centerOfMass[3],tank.d,tank.density_derp_h,der(tank.M),der(tank.MXi[1]),der(tank.MXi[2]),der(tank.U_med),tank.eps_geometry,tank.fEmpty,tank.fFull,tank.gasDensity,tank.h_in[1],tank.h_in[2],tank.h_out[1],tank.h_start,tank.initialize_LiquidMass,tank.initialize_Xi,tank.initialize_energy,tank.initialize_pressure,tank.inletPositions[1,1],tank.inletPositions[1,2],tank.inletPositions[1,3],tank.inletPositions[2,1],tank.inletPositions[2,2],tank.inletPositions[2,3],der(tank.inlet[1].m_flow),tank.inlet[1].m_flow,tank.inlet[1].r,tank.inlet[1].state.T,tank.inlet[1].state.X[1],tank.inlet[1].state.X[2],tank.inlet[1].state.p,der(tank.inlet[2].m_flow),tank.inlet[2].m_flow,tank.inlet[2].r,tank.inlet[2].state.T,tank.inlet[2].state.X[1],tank.inlet[2].state.X[2],tank.inlet[2].state.p,tank.k_volume_damping,tank.liquidDensity,tank.m_flow_assert,tank.m_flow_in[1],tank.m_flow_in[2],tank.m_flow_out[1],tank.medium.MM,tank.medium.R_s,tank.medium.T,tank.medium.T_degC,tank.medium.X[1],tank.medium.X[2],tank.medium.Xi[1],tank.medium.Xi[2],tank.medium.d,tank.medium.h,tank.medium.p,tank.medium.p_bar,tank.medium.preferredMediumStates,tank.medium.standardOrderComponents,tank.medium.state.T,tank.medium.state.X[1],tank.medium.state.X[2],tank.medium.state.p,tank.medium.u,tank.normAcc[1],tank.normAcc[2],tank.normAcc[3],tank.nx,tank.nz,tank.outletPositions[1,1],tank.outletPositions[1,2],tank.outletPositions[1,3],tank.outletTransition,der(tank.outlet[1].m_flow),tank.outlet[1].m_flow,tank.outlet[1].r,tank.outlet[1].state.T,tank.outlet[1].state.X[1],tank.outlet[1].state.X[2],tank.outlet[1].state.p,tank.p_in[1],tank.p_in[2],tank.p_ref,tank.p_start,tank.r[1],tank.r[2],tank.r_damping,tank.shiftOutlet[1],tank.state_out[1].T,tank.state_out[1].X[1],tank.state_out[1].X[2],tank.state_out[1].p,tank.staticHeadInlets[1],tank.staticHeadInlets[2],tank.staticHeadInlets_Pa_relative[1],tank.staticHeadInlets_Pa_relative[2],tank.staticHeadOutlets[1],tank.staticHeadOutlets_Pa_relative[1],tank.tankCenter[1],tank.tankCenter[2],tank.tankCenter[3],tank.useHeatport,tank.usePreferredMediumStates,tank.use_hstart,tank.xLength,tank.yLength,tank.zLength,tank1.A,tank1.Area,tank1.AxLimit,tank1.AzLimit,tank1.D,tank1.D1,tank1.D2,tank1.D3,tank1.D4,tank1.K,tank1.L,tank1.M,tank1.MXi[1],tank1.MXi[2],tank1.M_liq_start,tank1.M_outlets,tank1.N_inlets,tank1.Q_flow,tank1.T_heatPort,tank1.T_start,tank1.ThresholdEmpty,tank1.ThresholdFull,tank1.U,tank1.U_med,tank1.V,tank1.V_liquid,tank1.V_ref,tank1.W_v,tank1.Xi_0[1],tank1.Xi_0[2],tank1.Xi_in[1,1],tank1.Xi_in[2,1],tank1.Xi_out[1,1],tank1.Xi_out[2,1],tank1.centerOfMass[1],tank1.centerOfMass[2],tank1.centerOfMass[3],tank1.d,tank1.density_derp_h,der(tank1.M),der(tank1.MXi[1]),der(tank1.MXi[2]),der(tank1.U_med),tank1.eps_geometry,tank1.fEmpty,tank1.fFull,tank1.gasDensity,tank1.h_in[1],tank1.h_out[1],tank1.h_start,tank1.heatPort.Q_flow,tank1.heatPort.T,tank1.initialize_LiquidMass,tank1.initialize_Xi,tank1.initialize_energy,tank1.initialize_pressure,tank1.inletPositions[1,1],tank1.inletPositions[1,2],tank1.inletPositions[1,3],der(tank1.inlet[1].m_flow),tank1.inlet[1].m_flow,tank1.inlet[1].r,tank1.inlet[1].state.T,tank1.inlet[1].state.X[1],tank1.inlet[1].state.X[2],tank1.inlet[1].state.p,tank1.k_volume_damping,tank1.liquidDensity,tank1.m_flow_assert,tank1.m_flow_in[1],tank1.m_flow_out[1],tank1.medium.MM,tank1.medium.R_s,tank1.medium.T,tank1.medium.T_degC,tank1.medium.X[1],tank1.medium.X[2],tank1.medium.Xi[1],tank1.medium.Xi[2],tank1.medium.d,tank1.medium.h,tank1.medium.p,tank1.medium.p_bar,tank1.medium.preferredMediumStates,tank1.medium.standardOrderComponents,tank1.medium.state.T,tank1.medium.state.X[1],tank1.medium.state.X[2],tank1.medium.state.p,tank1.medium.u,tank1.normAcc[1],tank1.normAcc[2],tank1.normAcc[3],tank1.nx,tank1.nz,tank1.outletPositions[1,1],tank1.outletPositions[1,2],tank1.outletPositions[1,3],tank1.outletTransition,der(tank1.outlet[1].m_flow),tank1.outlet[1].m_flow,tank1.outlet[1].r,tank1.outlet[1].state.T,tank1.outlet[1].state.X[1],tank1.outlet[1].state.X[2],tank1.outlet[1].state.p,tank1.p_in[1],tank1.p_ref,tank1.p_start,tank1.r[1],tank1.r_damping,tank1.shiftOutlet[1],tank1.state_out[1].T,tank1.state_out[1].X[1],tank1.state_out[1].X[2],tank1.state_out[1].p,tank1.staticHeadInlets[1],tank1.staticHeadInlets_Pa_relative[1],tank1.staticHeadOutlets[1],tank1.staticHeadOutlets_Pa_relative[1],tank1.tankCenter[1],tank1.tankCenter[2],tank1.tankCenter[3],tank1.useHeatport,tank1.usePreferredMediumStates,tank1.use_hstart,tank1.xLength,tank1.yLength,tank1.zLength

Variables in the result:$cse3.T,$cse3.p,$cse9.T,$cse9.p,acceleration.a[1],acceleration.a[2],acceleration.a[3],acceleration.ax,acceleration.ay,acceleration.az,acceleration.setFromInputs,der(flowResistance.inlet.m_flow),der(flowResistance1.inlet.m_flow),der(flowResistance3.inlet.m_flow),der(staticHead.inlet.m_flow),der(tank.M),der(tank.MXi[1]),der(tank.MXi[2]),der(tank.U_med),der(tank1.M),der(tank1.MXi[1]),der(tank1.MXi[2]),der(tank1.U_med),dropOfCommons.L,dropOfCommons.assertionLevel,dropOfCommons.g,dropOfCommons.k_volume_damping,dropOfCommons.m_flow_reg,dropOfCommons.omega_reg,dropOfCommons.p_min,dropOfCommons.rho_min,fixedHeatFlow.Q_flow,fixedHeatFlow.T_ref,fixedHeatFlow.alpha,fixedHeatFlow.port.Q_flow,fixedHeatFlow.port.T,flowResistance.D_h,flowResistance.L,flowResistance.L_value,flowResistance.Xi_in[1],flowResistance.Xi_in[2],flowResistance.Xi_out[1],flowResistance.Xi_out[2],flowResistance.a,flowResistance.areaCross,flowResistance.areaCrossInput,flowResistance.areaHydraulic,flowResistance.b,flowResistance.clip_p_out,flowResistance.dp,flowResistance.dp_ref_color,flowResistance.dr_corr,flowResistance.h_in,flowResistance.h_out,flowResistance.initM_flow,flowResistance.inlet.m_flow,flowResistance.inlet.r,flowResistance.inlet.state.T,flowResistance.inlet.state.X[1],flowResistance.inlet.state.X[2],flowResistance.inlet.state.p,flowResistance.l,flowResistance.m_acceleration_0,flowResistance.m_flow,flowResistance.m_flowStateSelect,flowResistance.m_flow_0,flowResistance.mu_in,flowResistance.outlet.m_flow,flowResistance.outlet.r,flowResistance.outlet.state.T,flowResistance.outlet.state.X[1],flowResistance.outlet.state.X[2],flowResistance.outlet.state.p,flowResistance.p_in,flowResistance.p_min,flowResistance.p_out,flowResistance.perimeter,flowResistance.perimeterInput,flowResistance.pressureDropSignificantDigits,flowResistance.r,flowResistance.rho_in,flowResistance.rho_min,flowResistance.shape,flowResistance1.D_h,flowResistance1.L,flowResistance1.L_value,flowResistance1.Xi_in[1],flowResistance1.Xi_in[2],flowResistance1.Xi_out[1],flowResistance1.Xi_out[2],flowResistance1.a,flowResistance1.areaCross,flowResistance1.areaCrossInput,flowResistance1.areaHydraulic,flowResistance1.b,flowResistance1.clip_p_out,flowResistance1.dp,flowResistance1.dp_ref_color,flowResistance1.dr_corr,flowResistance1.h_in,flowResistance1.h_out,flowResistance1.initM_flow,flowResistance1.inlet.m_flow,flowResistance1.inlet.r,flowResistance1.inlet.state.T,flowResistance1.inlet.state.X[1],flowResistance1.inlet.state.X[2],flowResistance1.inlet.state.p,flowResistance1.l,flowResistance1.m_acceleration_0,flowResistance1.m_flow,flowResistance1.m_flowStateSelect,flowResistance1.m_flow_0,flowResistance1.mu_in,flowResistance1.outlet.m_flow,flowResistance1.outlet.r,flowResistance1.outlet.state.T,flowResistance1.outlet.state.X[1],flowResistance1.outlet.state.X[2],flowResistance1.outlet.state.p,flowResistance1.p_in,flowResistance1.p_min,flowResistance1.p_out,flowResistance1.perimeter,flowResistance1.perimeterInput,flowResistance1.pressureDropSignificantDigits,flowResistance1.r,flowResistance1.rho_in,flowResistance1.rho_min,flowResistance1.shape,flowResistance2.D_h,flowResistance2.L,flowResistance2.L_value,flowResistance2.Xi_in[1],flowResistance2.Xi_in[2],flowResistance2.Xi_out[1],flowResistance2.Xi_out[2],flowResistance2.a,flowResistance2.areaCross,flowResistance2.areaCrossInput,flowResistance2.areaHydraulic,flowResistance2.b,flowResistance2.clip_p_out,flowResistance2.dp,flowResistance2.dp_ref_color,flowResistance2.dr_corr,flowResistance2.h_in,flowResistance2.h_out,flowResistance2.initM_flow,flowResistance2.inlet.m_flow,flowResistance2.inlet.r,flowResistance2.inlet.state.T,flowResistance2.inlet.state.X[1],flowResistance2.inlet.state.X[2],flowResistance2.inlet.state.p,flowResistance2.l,flowResistance2.m_acceleration_0,flowResistance2.m_flow,flowResistance2.m_flowStateSelect,flowResistance2.m_flow_0,flowResistance2.mu_in,flowResistance2.outlet.m_flow,flowResistance2.outlet.r,flowResistance2.outlet.state.T,flowResistance2.outlet.state.X[1],flowResistance2.outlet.state.X[2],flowResistance2.outlet.state.p,flowResistance2.p_in,flowResistance2.p_min,flowResistance2.p_out,flowResistance2.perimeter,flowResistance2.perimeterInput,flowResistance2.pressureDropSignificantDigits,flowResistance2.r,flowResistance2.rho_in,flowResistance2.rho_min,flowResistance2.shape,flowResistance3.D_h,flowResistance3.L,flowResistance3.L_value,flowResistance3.Xi_in[1],flowResistance3.Xi_in[2],flowResistance3.Xi_out[1],flowResistance3.Xi_out[2],flowResistance3.a,flowResistance3.areaCross,flowResistance3.areaCrossInput,flowResistance3.areaHydraulic,flowResistance3.b,flowResistance3.clip_p_out,flowResistance3.dp,flowResistance3.dp_ref_color,flowResistance3.dr_corr,flowResistance3.h_in,flowResistance3.h_out,flowResistance3.initM_flow,flowResistance3.inlet.m_flow,flowResistance3.inlet.r,flowResistance3.inlet.state.T,flowResistance3.inlet.state.X[1],flowResistance3.inlet.state.X[2],flowResistance3.inlet.state.p,flowResistance3.l,flowResistance3.m_acceleration_0,flowResistance3.m_flow,flowResistance3.m_flowStateSelect,flowResistance3.m_flow_0,flowResistance3.mu_in,flowResistance3.outlet.m_flow,flowResistance3.outlet.r,flowResistance3.outlet.state.T,flowResistance3.outlet.state.X[1],flowResistance3.outlet.state.X[2],flowResistance3.outlet.state.p,flowResistance3.p_in,flowResistance3.p_min,flowResistance3.p_out,flowResistance3.perimeter,flowResistance3.perimeterInput,flowResistance3.pressureDropSignificantDigits,flowResistance3.r,flowResistance3.rho_in,flowResistance3.rho_min,flowResistance3.shape,sink1.L,sink1.inlet.m_flow,sink1.inlet.r,sink1.inlet.state.T,sink1.inlet.state.X[1],sink1.inlet.state.X[2],sink1.inlet.state.p,sink1.p,sink1.p0,sink1.p0_par,sink1.r,source.L,source.T0,source.T0_par,source.Xi0[1],source.Xi0[2],source.Xi0_par[1],source.Xi0_par[2],source.h0,source.h0_par,source.outlet.m_flow,source.outlet.r,source.outlet.state.T,source.outlet.state.X[1],source.outlet.state.X[2],source.outlet.state.p,source.p0,source.p0_par,source1.L,source1.T0,source1.T0_par,source1.Xi0[1],source1.Xi0[2],source1.Xi0_par[1],source1.Xi0_par[2],source1.h0,source1.h0_par,source1.outlet.m_flow,source1.outlet.r,source1.outlet.state.T,source1.outlet.state.X[1],source1.outlet.state.X[2],source1.outlet.state.p,source1.p0,source1.p0_par,staticHead.L,staticHead.L_value,staticHead.Xi_in[1],staticHead.Xi_in[2],staticHead.Xi_out[1],staticHead.Xi_out[2],staticHead.clip_p_out,staticHead.displayPositions,staticHead.dp,staticHead.dr_corr,staticHead.fromPosition[1],staticHead.fromPosition[2],staticHead.fromPosition[3],staticHead.h_in,staticHead.h_out,staticHead.initM_flow,staticHead.inlet.m_flow,staticHead.inlet.r,staticHead.inlet.state.T,staticHead.inlet.state.X[1],staticHead.inlet.state.X[2],staticHead.inlet.state.p,staticHead.m_acceleration_0,staticHead.m_flow,staticHead.m_flowStateSelect,staticHead.m_flow_0,staticHead.outlet.m_flow,staticHead.outlet.r,staticHead.outlet.state.T,staticHead.outlet.state.X[1],staticHead.outlet.state.X[2],staticHead.outlet.state.p,staticHead.p_in,staticHead.p_min,staticHead.p_out,staticHead.rho_in,staticHead.rho_min,staticHead.staticHead,staticHead.staticHead_Pa_relative,staticHead.toPosition[1],staticHead.toPosition[2],staticHead.toPosition[3],tank.A,tank.Area,tank.AxLimit,tank.AzLimit,tank.D,tank.D1,tank.D2,tank.D3,tank.D4,tank.K,tank.L,tank.M,tank.MXi[1],tank.MXi[2],tank.M_liq_start,tank.M_outlets,tank.N_inlets,tank.Q_flow,tank.T_heatPort,tank.T_start,tank.ThresholdEmpty,tank.ThresholdFull,tank.U,tank.U_med,tank.V,tank.V_liquid,tank.V_ref,tank.W_v,tank.Xi_0[1],tank.Xi_0[2],tank.Xi_in[1,1],tank.Xi_in[1,2],tank.Xi_in[2,1],tank.Xi_in[2,2],tank.Xi_out[1,1],tank.Xi_out[2,1],tank.centerOfMass[1],tank.centerOfMass[2],tank.centerOfMass[3],tank.d,tank.density_derp_h,tank.eps_geometry,tank.fEmpty,tank.fFull,tank.gasDensity,tank.h_in[1],tank.h_in[2],tank.h_out[1],tank.h_start,tank.initialize_LiquidMass,tank.initialize_Xi,tank.initialize_energy,tank.initialize_pressure,tank.inletPositions[1,1],tank.inletPositions[1,2],tank.inletPositions[1,3],tank.inletPositions[2,1],tank.inletPositions[2,2],tank.inletPositions[2,3],tank.inlet[1].m_flow,tank.inlet[1].r,tank.inlet[1].state.T,tank.inlet[1].state.X[1],tank.inlet[1].state.X[2],tank.inlet[1].state.p,tank.inlet[2].m_flow,tank.inlet[2].r,tank.inlet[2].state.T,tank.inlet[2].state.X[1],tank.inlet[2].state.X[2],tank.inlet[2].state.p,tank.k_volume_damping,tank.liquidDensity,tank.m_flow_assert,tank.m_flow_in[1],tank.m_flow_in[2],tank.m_flow_out[1],tank.medium.MM,tank.medium.R_s,tank.medium.T,tank.medium.T_degC,tank.medium.X[1],tank.medium.X[2],tank.medium.Xi[1],tank.medium.Xi[2],tank.medium.d,tank.medium.h,tank.medium.p,tank.medium.p_bar,tank.medium.preferredMediumStates,tank.medium.standardOrderComponents,tank.medium.state.T,tank.medium.state.X[1],tank.medium.state.X[2],tank.medium.state.p,tank.medium.u,tank.normAcc[1],tank.normAcc[2],tank.normAcc[3],tank.nx,tank.nz,tank.outletPositions[1,1],tank.outletPositions[1,2],tank.outletPositions[1,3],tank.outletTransition,tank.outlet[1].m_flow,tank.outlet[1].r,tank.outlet[1].state.T,tank.outlet[1].state.X[1],tank.outlet[1].state.X[2],tank.outlet[1].state.p,tank.p_in[1],tank.p_in[2],tank.p_ref,tank.p_start,tank.r[1],tank.r[2],tank.r_damping,tank.shiftOutlet[1],tank.state_out[1].T,tank.state_out[1].X[1],tank.state_out[1].X[2],tank.state_out[1].p,tank.staticHeadInlets[1],tank.staticHeadInlets[2],tank.staticHeadInlets_Pa_relative[1],tank.staticHeadInlets_Pa_relative[2],tank.staticHeadOutlets[1],tank.staticHeadOutlets_Pa_relative[1],tank.tankCenter[1],tank.tankCenter[2],tank.tankCenter[3],tank.useHeatport,tank.usePreferredMediumStates,tank.use_hstart,tank.xLength,tank.yLength,tank.zLength,tank1.A,tank1.Area,tank1.AxLimit,tank1.AzLimit,tank1.D,tank1.D1,tank1.D2,tank1.D3,tank1.D4,tank1.K,tank1.L,tank1.M,tank1.MXi[1],tank1.MXi[2],tank1.M_liq_start,tank1.M_outlets,tank1.N_inlets,tank1.Q_flow,tank1.T_heatPort,tank1.T_start,tank1.ThresholdEmpty,tank1.ThresholdFull,tank1.U,tank1.U_med,tank1.V,tank1.V_liquid,tank1.V_ref,tank1.W_v,tank1.Xi_0[1],tank1.Xi_0[2],tank1.Xi_in[1,1],tank1.Xi_in[2,1],tank1.Xi_out[1,1],tank1.Xi_out[2,1],tank1.centerOfMass[1],tank1.centerOfMass[2],tank1.centerOfMass[3],tank1.d,tank1.density_derp_h,tank1.eps_geometry,tank1.fEmpty,tank1.fFull,tank1.gasDensity,tank1.h_in[1],tank1.h_out[1],tank1.h_start,tank1.heatPort.Q_flow,tank1.heatPort.T,tank1.initialize_LiquidMass,tank1.initialize_Xi,tank1.initialize_energy,tank1.initialize_pressure,tank1.inletPositions[1,1],tank1.inletPositions[1,2],tank1.inletPositions[1,3],tank1.inlet[1].m_flow,tank1.inlet[1].r,tank1.inlet[1].state.T,tank1.inlet[1].state.X[1],tank1.inlet[1].state.X[2],tank1.inlet[1].state.p,tank1.k_volume_damping,tank1.liquidDensity,tank1.m_flow_assert,tank1.m_flow_in[1],tank1.m_flow_out[1],tank1.medium.MM,tank1.medium.R_s,tank1.medium.T,tank1.medium.T_degC,tank1.medium.X[1],tank1.medium.X[2],tank1.medium.Xi[1],tank1.medium.Xi[2],tank1.medium.d,tank1.medium.h,tank1.medium.p,tank1.medium.p_bar,tank1.medium.preferredMediumStates,tank1.medium.standardOrderComponents,tank1.medium.state.T,tank1.medium.state.X[1],tank1.medium.state.X[2],tank1.medium.state.p,tank1.medium.u,tank1.normAcc[1],tank1.normAcc[2],tank1.normAcc[3],tank1.nx,tank1.nz,tank1.outletPositions[1,1],tank1.outletPositions[1,2],tank1.outletPositions[1,3],tank1.outletTransition,tank1.outlet[1].m_flow,tank1.outlet[1].r,tank1.outlet[1].state.T,tank1.outlet[1].state.X[1],tank1.outlet[1].state.X[2],tank1.outlet[1].state.p,tank1.p_in[1],tank1.p_ref,tank1.p_start,tank1.r[1],tank1.r_damping,tank1.shiftOutlet[1],tank1.state_out[1].T,tank1.state_out[1].X[1],tank1.state_out[1].X[2],tank1.state_out[1].p,tank1.staticHeadInlets[1],tank1.staticHeadInlets_Pa_relative[1],tank1.staticHeadOutlets[1],tank1.staticHeadOutlets_Pa_relative[1],tank1.tankCenter[1],tank1.tankCenter[2],tank1.tankCenter[3],tank1.useHeatport,tank1.usePreferredMediumStates,tank1.use_hstart,tank1.xLength,tank1.yLength,tank1.zLength,time
filterSimulationResults("ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat", "/var/lib/jenkins/ws/OpenModelicaLibraryTestingWork/OpenModelicaLibraryTesting/files/ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating.diff.mat", vars={"tank1.inlet[1].state.X[1]", "tank1.der(MXi[1])", "tank1.Xi_in[1, 1]", "tank.state_out[1].X[1]", "tank.m_flow_in[1]", "tank.der(MXi[1])", "tank.Xi_out[1, 1]", "staticHead.inlet.state.X[1]", "staticHead.Xi_out[1]", "flowResistance2.inlet.state.X[1]", "flowResistance2.Xi_out[1]"}, removeDescription=false) [Timeout 660]
""
[Timeout remaining time 660]
filterSimulationResults("/mnt/ReferenceFiles/ThermofluidStream-main-regression/ReferenceData/ThermofluidStream.Boundaries.Tests.TankHeating_ref.mat", "/var/lib/jenkins/ws/OpenModelicaLibraryTestingWork/OpenModelicaLibraryTesting/files/ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating.diff.ref.mat", vars={"tank1.inlet[1].state.X[1]", "tank1.der(MXi[1])", "tank1.Xi_in[1, 1]", "tank.state_out[1].X[1]", "tank.m_flow_in[1]", "tank.der(MXi[1])", "tank.Xi_out[1, 1]", "staticHead.inlet.state.X[1]", "staticHead.Xi_out[1]", "flowResistance2.inlet.state.X[1]", "flowResistance2.Xi_out[1]"}, removeDescription=false) [Timeout 660]
""
[Timeout remaining time 660]
[Calling sys.exit(0), Time elapsed: 5.54818348120898]