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 0.001371/0.001371, allocations: 88.72 kB / 19.44 MB, free: 356 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 0.001538/0.001538, allocations: 157.7 kB / 22.75 MB, free: 1.684 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 1.471/1.471, allocations: 177.1 MB / 203.1 MB, free: 5.605 MB / 186.7 MB
"
[Timeout remaining time 178]
loadFile("/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermofluidStream main/package.mo", uses=false) [Timeout 180]
"Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermofluidStream main/package.mo): time 1.021/1.021, allocations: 118.6 MB / 378.2 MB, free: 1.453 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.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|source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[Timeout 660]
"Notification: Performance of FrontEnd - loaded program: time 1.232e-06/1.232e-06, allocations: 0 / 482.9 MB, free: 8.262 MB / 410.7 MB
Notification: Performance of FrontEnd - Absyn->SCode: time 1.704e-05/1.827e-05, allocations: 6.312 kB / 482.9 MB, free: 8.254 MB / 410.7 MB
Notification: Performance of NFInst.instantiate(ThermofluidStream.Boundaries.Tests.TankHeating): time 0.5499/0.5499, allocations: 258.9 MB / 0.7244 GB, free: 9.332 MB / 0.5573 GB
Notification: Performance of NFInst.instExpressions: time 0.009336/0.5592, allocations: 7.33 MB / 0.7316 GB, free: 9.078 MB / 0.5573 GB
Notification: Performance of NFInst.updateImplicitVariability: time 0.0009582/0.5602, allocations: 64.94 kB / 0.7317 GB, free: 9.074 MB / 0.5573 GB
Notification: Performance of NFTyping.typeComponents: time 0.001943/0.5621, allocations: 0.8354 MB / 0.7325 GB, free: 8.984 MB / 0.5573 GB
Notification: Performance of NFTyping.typeBindings: time 0.008785/0.5709, allocations: 4.286 MB / 0.7367 GB, free: 8.203 MB / 0.5573 GB
Notification: Performance of NFTyping.typeClassSections: time 0.005634/0.5765, allocations: 2.63 MB / 0.7392 GB, free: 7.309 MB / 0.5573 GB
Notification: Performance of NFFlatten.flatten: time 0.003132/0.5797, allocations: 3.51 MB / 0.7427 GB, free: 5.637 MB / 0.5573 GB
Notification: Performance of NFFlatten.resolveConnections: time 0.0003615/0.58, allocations: 242.7 kB / 0.7429 GB, free: 5.484 MB / 0.5573 GB
Notification: Performance of NFEvalConstants.evaluate: time 0.005616/0.5857, allocations: 3.6 MB / 0.7464 GB, free: 3.684 MB / 0.5573 GB
Notification: Performance of NFSimplifyModel.simplify: time 0.001582/0.5872, allocations: 1.413 MB / 0.7478 GB, free: 3.008 MB / 0.5573 GB
Notification: Performance of NFPackage.collectConstants: time 0.0002973/0.5875, allocations: 208.6 kB / 0.748 GB, free: 3.008 MB / 0.5573 GB
Notification: Performance of NFFlatten.collectFunctions: time 0.01204/0.5996, allocations: 7.373 MB / 0.7552 GB, free: 216 kB / 0.5573 GB
Notification: Performance of NFScalarize.scalarize: time 0.001017/0.6006, allocations: 0.8425 MB / 0.756 GB, free: 15.63 MB / 0.573 GB
Notification: Performance of NFVerifyModel.verify: time 0.001248/0.6018, allocations: 0.8234 MB / 0.7568 GB, free: 15.21 MB / 0.573 GB
Notification: Performance of NFConvertDAE.convert: time 0.01007/0.6119, allocations: 5.165 MB / 0.7619 GB, free: 12.52 MB / 0.573 GB
Notification: Performance of FrontEnd - DAE generated: time 5.711e-06/0.6119, allocations: 2.562 kB / 0.7619 GB, free: 12.52 MB / 0.573 GB
Notification: Performance of FrontEnd: time 1.392e-06/0.6119, allocations: 0 / 0.7619 GB, free: 12.52 MB / 0.573 GB
Notification: Performance of Transformations before backend: time 2.848e-05/0.6119, allocations: 0 / 0.7619 GB, free: 12.52 MB / 0.573 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 0.009452/0.6214, allocations: 3.327 MB / 0.7651 GB, free: 10.41 MB / 0.573 GB
Notification: Performance of prepare preOptimizeDAE: time 4.585e-05/0.6214, allocations: 8.812 kB / 0.7651 GB, free: 10.41 MB / 0.573 GB
Notification: Performance of preOpt normalInlineFunction (simulation): time 0.003241/0.6247, allocations: 0.6947 MB / 0.7658 GB, free: 10.09 MB / 0.573 GB
Notification: Performance of preOpt evaluateParameters (simulation): time 0.002688/0.6274, allocations: 1.243 MB / 0.767 GB, free: 9.289 MB / 0.573 GB
Notification: Performance of preOpt simplifyIfEquations (simulation): time 0.00111/0.6285, allocations: 1.025 MB / 0.768 GB, free: 8.188 MB / 0.573 GB
Notification: Performance of preOpt expandDerOperator (simulation): time 0.0003096/0.6288, allocations: 145.6 kB / 0.7682 GB, free: 8.145 MB / 0.573 GB
Notification: Performance of preOpt clockPartitioning (simulation): time 0.00621/0.635, allocations: 3.194 MB / 0.7713 GB, free: 4.957 MB / 0.573 GB
Notification: Performance of preOpt findStateOrder (simulation): time 3.227e-05/0.635, allocations: 11.92 kB / 0.7713 GB, free: 4.945 MB / 0.573 GB
Notification: Performance of preOpt replaceEdgeChange (simulation): time 0.0002076/0.6352, allocations: 53.23 kB / 0.7713 GB, free: 4.898 MB / 0.573 GB
Notification: Performance of preOpt inlineArrayEqn (simulation): time 0.0006297/0.6359, allocations: 190.3 kB / 0.7715 GB, free: 4.711 MB / 0.573 GB
Notification: Performance of preOpt removeEqualRHS (simulation): time 0.007487/0.6434, allocations: 3.054 MB / 0.7745 GB, free: 1.664 MB / 0.573 GB
Notification: Performance of preOpt removeSimpleEquations (simulation): time 0.01654/0.6599, allocations: 7.153 MB / 0.7815 GB, free: 10.56 MB / 0.5886 GB
Notification: Performance of preOpt comSubExp (simulation): time 0.005211/0.6651, allocations: 1.889 MB / 0.7833 GB, free: 8.672 MB / 0.5886 GB
Notification: Performance of preOpt resolveLoops (simulation): time 0.003605/0.6687, allocations: 1.386 MB / 0.7847 GB, free: 7.289 MB / 0.5886 GB
Notification: Performance of preOpt evalFunc (simulation): time 0.0009758/0.6697, allocations: 305.1 kB / 0.785 GB, free: 6.992 MB / 0.5886 GB
Notification: Performance of preOpt encapsulateWhenConditions (simulation): time 6.277e-05/0.6698, allocations: 55.88 kB / 0.785 GB, free: 6.926 MB / 0.5886 GB
Notification: Performance of pre-optimization done (n=187): time 4.668e-06/0.6698, allocations: 4 kB / 0.785 GB, free: 6.922 MB / 0.5886 GB
Notification: Performance of matching and sorting (n=187): time 0.01397/0.6837, allocations: 4.748 MB / 0.7897 GB, free: 2.16 MB / 0.5886 GB
Notification: Performance of inlineWhenForInitialization (initialization): time 6.73e-05/0.6838, allocations: 68.72 kB / 0.7897 GB, free: 2.082 MB / 0.5886 GB
Notification: Performance of selectInitializationVariablesDAE (initialization): time 0.001571/0.6854, allocations: 0.9592 MB / 0.7907 GB, free: 1.109 MB / 0.5886 GB
Notification: Performance of collectPreVariables (initialization): time 0.0002796/0.6856, allocations: 62.36 kB / 0.7907 GB, free: 1.047 MB / 0.5886 GB
Notification: Performance of collectInitialEqns (initialization): time 0.0007576/0.6864, allocations: 0.6244 MB / 0.7913 GB, free: 424 kB / 0.5886 GB
Notification: Performance of collectInitialBindings (initialization): time 0.0008704/0.6873, allocations: 0.648 MB / 0.792 GB, free: 15.77 MB / 0.6042 GB
Notification: Performance of simplifyInitialFunctions (initialization): time 0.0008267/0.6881, allocations: 349.3 kB / 0.7923 GB, free: 15.43 MB / 0.6042 GB
Notification: Performance of setup shared object (initialization): time 0.0002019/0.6883, allocations: 309.1 kB / 0.7926 GB, free: 15.12 MB / 0.6042 GB
Notification: Performance of preBalanceInitialSystem (initialization): time 0.00351/0.6918, allocations: 1.28 MB / 0.7938 GB, free: 13.84 MB / 0.6042 GB
Notification: Performance of partitionIndependentBlocks (initialization): time 0.004325/0.6961, allocations: 2.031 MB / 0.7958 GB, free: 11.64 MB / 0.6042 GB
Notification: Performance of analyzeInitialSystem (initialization): time 0.05886/0.755, allocations: 10.64 MB / 0.8062 GB, free: 1.012 MB / 0.6042 GB
Notification: Performance of solveInitialSystemEqSystem (initialization): time 7.043e-06/0.755, allocations: 0 / 0.8062 GB, free: 1.012 MB / 0.6042 GB
Notification: Performance of matching and sorting (n=210) (initialization): time 0.009214/0.7642, allocations: 3.329 MB / 0.8095 GB, free: 13.69 MB / 0.6198 GB
Notification: Performance of prepare postOptimizeDAE: time 2.707e-05/0.7642, allocations: 11.98 kB / 0.8095 GB, free: 13.68 MB / 0.6198 GB
Notification: Performance of postOpt simplifyComplexFunction (initialization): time 1.14e-05/0.7643, allocations: 0 / 0.8095 GB, free: 13.68 MB / 0.6198 GB
Notification: Performance of postOpt tearingSystem (initialization): time 0.001013/0.7653, allocations: 216.2 kB / 0.8097 GB, free: 13.45 MB / 0.6198 GB
Notification: Performance of postOpt solveSimpleEquations (initialization): time 0.002111/0.7674, allocations: 389.5 kB / 0.8101 GB, free: 13.09 MB / 0.6198 GB
Notification: Performance of postOpt calculateStrongComponentJacobians (initialization): time 0.007228/0.7746, allocations: 6.802 MB / 0.8167 GB, free: 5.812 MB / 0.6198 GB
Notification: Performance of postOpt simplifyAllExpressions (initialization): time 0.002881/0.7775, allocations: 375 kB / 0.8171 GB, free: 5.445 MB / 0.6198 GB
Notification: Performance of postOpt collapseArrayExpressions (initialization): time 0.0003201/0.7778, allocations: 120.7 kB / 0.8172 GB, free: 5.328 MB / 0.6198 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 0.001071/0.7789, allocations: 422.2 kB / 0.8176 GB, free: 4.93 MB / 0.6198 GB
Notification: Performance of postOpt lateInlineFunction (simulation): time 0.0006651/0.7796, allocations: 215 kB / 0.8178 GB, free: 4.719 MB / 0.6198 GB
Notification: Performance of postOpt wrapFunctionCalls (simulation): time 0.01101/0.7906, allocations: 4.447 MB / 0.8221 GB, free: 248 kB / 0.6198 GB
Notification: Performance of postOpt inlineArrayEqn (simulation): time 0.008517/0.7991, allocations: 3.098 MB / 0.8252 GB, free: 13.14 MB / 0.6355 GB
Notification: Performance of postOpt constantLinearSystem (simulation): time 1.341e-05/0.7991, allocations: 4 kB / 0.8252 GB, free: 13.13 MB / 0.6355 GB
Notification: Performance of postOpt simplifysemiLinear (simulation): time 2.266e-05/0.7991, allocations: 11.91 kB / 0.8252 GB, free: 13.12 MB / 0.6355 GB
Notification: Performance of postOpt removeSimpleEquations (simulation): time 0.01426/0.8134, allocations: 5.594 MB / 0.8306 GB, free: 7.527 MB / 0.6355 GB
Notification: Performance of postOpt simplifyComplexFunction (simulation): time 7.504e-06/0.8134, allocations: 0 / 0.8306 GB, free: 7.527 MB / 0.6355 GB
Notification: Performance of postOpt solveSimpleEquations (simulation): time 0.002075/0.8155, allocations: 371.1 kB / 0.831 GB, free: 7.18 MB / 0.6355 GB
Notification: Performance of postOpt tearingSystem (simulation): time 0.00212/0.8176, allocations: 451.9 kB / 0.8314 GB, free: 6.719 MB / 0.6355 GB
Notification: Performance of postOpt inputDerivativesUsed (simulation): time 0.0002346/0.8178, allocations: 79.91 kB / 0.8315 GB, free: 6.641 MB / 0.6355 GB
Notification: Performance of postOpt calculateStrongComponentJacobians (simulation): time 0.008289/0.8261, allocations: 8.002 MB / 0.8393 GB, free: 14.11 MB / 0.6511 GB
Notification: Performance of postOpt calculateStateSetsJacobians (simulation): time 1.462e-06/0.8261, allocations: 4 kB / 0.8393 GB, free: 14.11 MB / 0.6511 GB
Notification: Performance of postOpt symbolicJacobian (simulation): time 0.01367/0.8398, allocations: 5.331 MB / 0.8445 GB, free: 8.758 MB / 0.6511 GB
Notification: Performance of postOpt removeConstants (simulation): time 0.001416/0.8412, allocations: 494.1 kB / 0.845 GB, free: 8.273 MB / 0.6511 GB
Notification: Performance of postOpt simplifyTimeIndepFuncCalls (simulation): time 0.0003095/0.8415, allocations: 47.12 kB / 0.845 GB, free: 8.23 MB / 0.6511 GB
Notification: Performance of postOpt simplifyAllExpressions (simulation): time 0.002081/0.8436, allocations: 191.7 kB / 0.8452 GB, free: 8.043 MB / 0.6511 GB
Notification: Performance of postOpt findZeroCrossings (simulation): time 0.0006081/0.8442, allocations: 225.6 kB / 0.8454 GB, free: 7.82 MB / 0.6511 GB
Notification: Performance of postOpt collapseArrayExpressions (simulation): time 0.0003062/0.8445, allocations: 123.9 kB / 0.8455 GB, free: 7.699 MB / 0.6511 GB
Notification: Performance of sorting global known variables: time 0.00111/0.8456, allocations: 0.7013 MB / 0.8462 GB, free: 6.992 MB / 0.6511 GB
Notification: Performance of sort global known variables: time 7e-08/0.8456, allocations: 0 / 0.8462 GB, free: 6.992 MB / 0.6511 GB
Notification: Performance of remove unused functions: time 0.00358/0.8492, allocations: 1.245 MB / 0.8474 GB, free: 5.746 MB / 0.6511 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 0.003166/0.8523, allocations: 1.519 MB / 0.8489 GB, free: 4.344 MB / 0.6511 GB
Notification: Performance of simCode: created initialization part: time 0.009069/0.8614, allocations: 3.681 MB / 0.8525 GB, free: 0.6133 MB / 0.6511 GB
Notification: Performance of simCode: created event and clocks part: time 3.537e-06/0.8614, allocations: 8.062 kB / 0.8525 GB, free: 0.6055 MB / 0.6511 GB
Notification: Performance of simCode: created simulation system equations: time 0.005283/0.8667, allocations: 2.32 MB / 0.8548 GB, free: 14.24 MB / 0.6667 GB
Notification: Performance of simCode: created of all other equations (e.g. parameter, nominal, assert, etc): time 0.003622/0.8703, allocations: 0.8032 MB / 0.8556 GB, free: 13.45 MB / 0.6667 GB
Notification: Performance of simCode: created linear, non-linear and system jacobian parts: time 0.009993/0.8803, allocations: 4.51 MB / 0.86 GB, free: 8.918 MB / 0.6667 GB
Notification: Performance of simCode: some other stuff during SimCode phase: time 0.001138/0.8815, allocations: 0.8642 MB / 0.8608 GB, free: 8.016 MB / 0.6667 GB
Notification: Performance of simCode: alias equations: time 0.002343/0.8838, allocations: 0.6657 MB / 0.8615 GB, free: 7.348 MB / 0.6667 GB
Notification: Performance of simCode: all other stuff during SimCode phase: time 0.0008834/0.8847, allocations: 224.3 kB / 0.8617 GB, free: 7.129 MB / 0.6667 GB
Notification: Performance of SimCode: time 8.21e-07/0.8847, allocations: 0 / 0.8617 GB, free: 7.129 MB / 0.6667 GB
Notification: Performance of Templates: time 0.2716/1.156, allocations: 62.44 MB / 0.9227 GB, free: 313.2 MB / 0.7136 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=1200  -emit_protected -lv LOG_STATS > ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating.pipe 2>&1) [Timeout 1200]
diffSimulationResults("ThermofluidStream_dev_ThermofluidStream.Boundaries.Tests.TankHeating_res.mat","/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",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
[Calling sys.exit(0), Time elapsed: 9.545753745012917]