Running: ./testmodel.py --libraries=/home/hudson/saved_omc/libraries/.openmodelica/libraries --ompython_omhome=/usr ThermofluidStream_dev_ThermofluidStream.Media.additionalMedia.SingleGasAndIncompressible.Tests.TestSimpleLoopJP8DryAir.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 0.002076/0.002076, allocations: 87.56 kB / 20.22 MB, free: 1.195 MB / 14.72 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 0.00202/0.00202, allocations: 156.7 kB / 23.52 MB, free: 4.109 MB / 14.72 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 1.425/1.425, allocations: 177.1 MB / 203.9 MB, free: 9.07 MB / 190.1 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 0.9499/0.9499, allocations: 116.2 MB / 376.5 MB, free: 7.27 MB / 350.1 MB " [Timeout remaining time 179] Using package ThermofluidStream with version 1.3.0 (/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.Media.additionalMedia.SingleGasAndIncompressible.Tests.TestSimpleLoopJP8DryAir,tolerance=1e-06,outputFormat="mat",numberOfIntervals=2500,variableFilter="CPUtime|EventCounter|NonlinearSystems.initialization.1..Calls|NonlinearSystems.initialization.1..Iterations|NonlinearSystems.initialization.1..Jacobians|NonlinearSystems.initialization.1..Residues|NonlinearSystems.simulation.1..Calls|NonlinearSystems.simulation.1..Iterations|NonlinearSystems.simulation.1..Jacobians|NonlinearSystems.simulation.1..Residues|PI2.T|der.PI2.x.|PI2.initType|PI2.k|PI2.u|PI2.x|PI2.x_start|PI2.y|PI2.y_start|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.|conductionElement.A|conductionElement.L|conductionElement.M|conductionElement.Q_flow|conductionElement.T|conductionElement.T_0|conductionElement.T_e|conductionElement.T_heatPort|conductionElement.U|conductionElement.U_internal|conductionElement.V|conductionElement.Xi_in.1.|conductionElement.Xi_in.2.|conductionElement.Xi_out.1.|conductionElement.Xi_out.2.|conductionElement.clip_p_out|conductionElement.deltaE_system|der.conductionElement.h.|conductionElement.dp|conductionElement.dr_corr|conductionElement.h|conductionElement.h_0|conductionElement.h_in|conductionElement.h_in_norm|conductionElement.h_out|conductionElement.heatPort.Q_flow|conductionElement.heatPort.T|conductionElement.init|conductionElement.initM_flow|der.conductionElement.inlet.m_flow.|conductionElement.inlet.m_flow|conductionElement.inlet.r|conductionElement.inlet.state.T|conductionElement.inlet.state.X.1.|conductionElement.inlet.state.X.2.|der.conductionElement.inlet.state.T.|der.conductionElement.inlet.state.p.|conductionElement.inlet.state.p|conductionElement.k|conductionElement.k_internal|conductionElement.k_par|conductionElement.m_acceleration_0|conductionElement.m_flow|conductionElement.m_flowStateSelect|conductionElement.m_flow_0|conductionElement.m_flow_assert|conductionElement.outlet.m_flow|conductionElement.outlet.r|conductionElement.outlet.state.T|conductionElement.outlet.state.X.1.|conductionElement.outlet.state.X.2.|conductionElement.outlet.state.p|conductionElement.p_in|conductionElement.p_min|conductionElement.p_out|conductionElement.rho|conductionElement.rho_min|conductionElement.state.T|conductionElement.state.X.1.|conductionElement.state.X.2.|conductionElement.state.p|differenceSensor_Tp.T|differenceSensor_Tp.TA|differenceSensor_Tp.TB|differenceSensor_Tp.TC|differenceSensor_Tp.T_0|differenceSensor_Tp.T_out|differenceSensor_Tp.digits|differenceSensor_Tp.direct_T|differenceSensor_Tp.direct_p|differenceSensor_Tp.init|differenceSensor_Tp.inletA.m_flow|differenceSensor_Tp.inletA.r|differenceSensor_Tp.inletA.state.T|differenceSensor_Tp.inletA.state.X.1.|differenceSensor_Tp.inletA.state.X.2.|differenceSensor_Tp.inletA.state.p|differenceSensor_Tp.inletB.m_flow|differenceSensor_Tp.inletB.r|differenceSensor_Tp.inletB.state.T|differenceSensor_Tp.inletB.state.X.1.|differenceSensor_Tp.inletB.state.X.2.|differenceSensor_Tp.inletB.state.p|differenceSensor_Tp.p|differenceSensor_Tp.pA|differenceSensor_Tp.pB|differenceSensor_Tp.p_0|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|feedback2.u1|feedback2.u2|feedback2.y|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|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.phi|flowResistance1.pressureDropSignificantDigits|flowResistance1.r|flowResistance1.rho_in|flowResistance1.rho_min|flowResistance1.shape|heat.y|heating_element.Q_flow|heating_element.T_ref|heating_element.alpha|heating_element.port.Q_flow|heating_element.port.T|limiter2.homotopyType|limiter2.simplifiedExpr|limiter2.strict|limiter2.u|limiter2.uMax|limiter2.uMin|limiter2.y|multiSensor_Tpm2.T|multiSensor_Tpm2.TC|multiSensor_Tpm2.T_0|multiSensor_Tpm2.digits|multiSensor_Tpm2.direct_T|multiSensor_Tpm2.direct_m_flow|multiSensor_Tpm2.direct_p|multiSensor_Tpm2.init|multiSensor_Tpm2.inlet.m_flow|multiSensor_Tpm2.inlet.r|multiSensor_Tpm2.inlet.state.T|multiSensor_Tpm2.inlet.state.X.1.|multiSensor_Tpm2.inlet.state.X.2.|multiSensor_Tpm2.inlet.state.p|multiSensor_Tpm2.m_flow|multiSensor_Tpm2.m_flow_0|multiSensor_Tpm2.outlet.m_flow|multiSensor_Tpm2.outlet.r|multiSensor_Tpm2.outlet.state.T|multiSensor_Tpm2.outlet.state.X.1.|multiSensor_Tpm2.outlet.state.X.2.|multiSensor_Tpm2.outlet.state.p|multiSensor_Tpm2.p|multiSensor_Tpm2.p_0|pump.J_p|pump.L|pump.Q_t|pump.W_t|pump.Xi_in.1.|pump.Xi_in.2.|pump.Xi_out.1.|pump.Xi_out.2.|pump.clip_p_out|der.pump.m_flow.|pump.dh|pump.dp|pump.dr_corr|pump.eta|pump.h_in|pump.h_out|pump.initM_flow|pump.initOmega|der.pump.inlet.m_flow.|pump.inlet.m_flow|pump.inlet.r|pump.inlet.state.T|pump.inlet.state.X.1.|pump.inlet.state.X.2.|pump.inlet.state.p|pump.m_acceleration_0|pump.m_flow|pump.m_flowStateSelect|pump.m_flow_0|pump.m_flow_reg|pump.max_rel_volume|pump.omega|pump.omegaStateSelect|pump.omega_0|pump.omega_dot_0|pump.omega_input|pump.omega_reg|pump.outlet.m_flow|pump.outlet.r|pump.outlet.state.T|pump.outlet.state.X.1.|pump.outlet.state.X.2.|pump.outlet.state.p|pump.outputQuantity|pump.p_in|pump.p_min|pump.p_out|pump.phi|pump.phi_0|pump.rho_min|pump.tau|pump.tau_normalized|pump.tau_st|pump.v_in|pump.v_out|refFlow_setPoint2.y|reservoir.A|reservoir.A_surf|reservoir.L|reservoir.M|reservoir.MXi.1.|reservoir.MXi.2.|reservoir.Q_flow|reservoir.T_heatPort|reservoir.T_start|reservoir.U|reservoir.U_med|reservoir.V|reservoir.W_v|reservoir.Xi_0.1.|reservoir.Xi_0.2.|reservoir.Xi_in.1.|reservoir.Xi_in.2.|reservoir.Xi_out.1.|reservoir.Xi_out.2.|reservoir.d|reservoir.density_derp_h|der.reservoir.M.|der.reservoir.MXi.1..|der.reservoir.MXi.2..|der.reservoir.U_med.|der.reservoir.V.|der.reservoir.m_flow_in.|der.reservoir.m_flow_out.|reservoir.g|reservoir.h_in|reservoir.h_out|reservoir.h_start|reservoir.height|reservoir.height_0|reservoir.height_min|reservoir.inlet.m_flow|reservoir.inlet.r|reservoir.inlet.state.T|reservoir.inlet.state.X.1.|reservoir.inlet.state.X.2.|reservoir.inlet.state.p|reservoir.k_volume_damping|reservoir.m_flow_assert|reservoir.m_flow_in|reservoir.m_flow_out|reservoir.medium.MM|reservoir.medium.R_s|reservoir.medium.T|reservoir.medium.T_degC|reservoir.medium.X.1.|reservoir.medium.X.2.|reservoir.medium.Xi.1.|reservoir.medium.Xi.2.|reservoir.medium.d|der.reservoir.medium.X.1..|der.reservoir.medium.X.2..|der.reservoir.medium.d.|der.reservoir.medium.h.|der.reservoir.medium.u.|reservoir.medium.h|reservoir.medium.p|reservoir.medium.p_bar|reservoir.medium.preferredMediumStates|reservoir.medium.standardOrderComponents|reservoir.medium.state.T|reservoir.medium.state.X.1.|reservoir.medium.state.X.2.|reservoir.medium.state.p|reservoir.medium.u|reservoir.outlet.m_flow|reservoir.outlet.r|reservoir.outlet.state.T|reservoir.outlet.state.X.1.|reservoir.outlet.state.X.2.|reservoir.outlet.state.p|reservoir.p_env|reservoir.p_env_par|reservoir.p_in|reservoir.p_start|reservoir.r|reservoir.r_damping|reservoir.r_in|reservoir.r_out|reservoir.state_in.T|reservoir.state_in.X.1.|reservoir.state_in.X.2.|reservoir.state_in.p|reservoir.state_out.T|reservoir.state_out.X.1.|reservoir.state_out.X.2.|reservoir.state_out.p",fileNamePrefix="ThermofluidStream_dev_ThermofluidStream.Media.additionalMedia.SingleGasAndIncompressible.Tests.TestSimpleLoopJP8DryAir") translateModel(ThermofluidStream.Media.additionalMedia.SingleGasAndIncompressible.Tests.TestSimpleLoopJP8DryAir,tolerance=1e-06,outputFormat="mat",numberOfIntervals=2500,variableFilter="CPUtime|EventCounter|NonlinearSystems.initialization.1..Calls|NonlinearSystems.initialization.1..Iterations|NonlinearSystems.initialization.1..Jacobians|NonlinearSystems.initialization.1..Residues|NonlinearSystems.simulation.1..Calls|NonlinearSystems.simulation.1..Iterations|NonlinearSystems.simulation.1..Jacobians|NonlinearSystems.simulation.1..Residues|PI2.T|der.PI2.x.|PI2.initType|PI2.k|PI2.u|PI2.x|PI2.x_start|PI2.y|PI2.y_start|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.|conductionElement.A|conductionElement.L|conductionElement.M|conductionElement.Q_flow|conductionElement.T|conductionElement.T_0|conductionElement.T_e|conductionElement.T_heatPort|conductionElement.U|conductionElement.U_internal|conductionElement.V|conductionElement.Xi_in.1.|conductionElement.Xi_in.2.|conductionElement.Xi_out.1.|conductionElement.Xi_out.2.|conductionElement.clip_p_out|conductionElement.deltaE_system|der.conductionElement.h.|conductionElement.dp|conductionElement.dr_corr|conductionElement.h|conductionElement.h_0|conductionElement.h_in|conductionElement.h_in_norm|conductionElement.h_out|conductionElement.heatPort.Q_flow|conductionElement.heatPort.T|conductionElement.init|conductionElement.initM_flow|der.conductionElement.inlet.m_flow.|conductionElement.inlet.m_flow|conductionElement.inlet.r|conductionElement.inlet.state.T|conductionElement.inlet.state.X.1.|conductionElement.inlet.state.X.2.|der.conductionElement.inlet.state.T.|der.conductionElement.inlet.state.p.|conductionElement.inlet.state.p|conductionElement.k|conductionElement.k_internal|conductionElement.k_par|conductionElement.m_acceleration_0|conductionElement.m_flow|conductionElement.m_flowStateSelect|conductionElement.m_flow_0|conductionElement.m_flow_assert|conductionElement.outlet.m_flow|conductionElement.outlet.r|conductionElement.outlet.state.T|conductionElement.outlet.state.X.1.|conductionElement.outlet.state.X.2.|conductionElement.outlet.state.p|conductionElement.p_in|conductionElement.p_min|conductionElement.p_out|conductionElement.rho|conductionElement.rho_min|conductionElement.state.T|conductionElement.state.X.1.|conductionElement.state.X.2.|conductionElement.state.p|differenceSensor_Tp.T|differenceSensor_Tp.TA|differenceSensor_Tp.TB|differenceSensor_Tp.TC|differenceSensor_Tp.T_0|differenceSensor_Tp.T_out|differenceSensor_Tp.digits|differenceSensor_Tp.direct_T|differenceSensor_Tp.direct_p|differenceSensor_Tp.init|differenceSensor_Tp.inletA.m_flow|differenceSensor_Tp.inletA.r|differenceSensor_Tp.inletA.state.T|differenceSensor_Tp.inletA.state.X.1.|differenceSensor_Tp.inletA.state.X.2.|differenceSensor_Tp.inletA.state.p|differenceSensor_Tp.inletB.m_flow|differenceSensor_Tp.inletB.r|differenceSensor_Tp.inletB.state.T|differenceSensor_Tp.inletB.state.X.1.|differenceSensor_Tp.inletB.state.X.2.|differenceSensor_Tp.inletB.state.p|differenceSensor_Tp.p|differenceSensor_Tp.pA|differenceSensor_Tp.pB|differenceSensor_Tp.p_0|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|feedback2.u1|feedback2.u2|feedback2.y|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|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.phi|flowResistance1.pressureDropSignificantDigits|flowResistance1.r|flowResistance1.rho_in|flowResistance1.rho_min|flowResistance1.shape|heat.y|heating_element.Q_flow|heating_element.T_ref|heating_element.alpha|heating_element.port.Q_flow|heating_element.port.T|limiter2.homotopyType|limiter2.simplifiedExpr|limiter2.strict|limiter2.u|limiter2.uMax|limiter2.uMin|limiter2.y|multiSensor_Tpm2.T|multiSensor_Tpm2.TC|multiSensor_Tpm2.T_0|multiSensor_Tpm2.digits|multiSensor_Tpm2.direct_T|multiSensor_Tpm2.direct_m_flow|multiSensor_Tpm2.direct_p|multiSensor_Tpm2.init|multiSensor_Tpm2.inlet.m_flow|multiSensor_Tpm2.inlet.r|multiSensor_Tpm2.inlet.state.T|multiSensor_Tpm2.inlet.state.X.1.|multiSensor_Tpm2.inlet.state.X.2.|multiSensor_Tpm2.inlet.state.p|multiSensor_Tpm2.m_flow|multiSensor_Tpm2.m_flow_0|multiSensor_Tpm2.outlet.m_flow|multiSensor_Tpm2.outlet.r|multiSensor_Tpm2.outlet.state.T|multiSensor_Tpm2.outlet.state.X.1.|multiSensor_Tpm2.outlet.state.X.2.|multiSensor_Tpm2.outlet.state.p|multiSensor_Tpm2.p|multiSensor_Tpm2.p_0|pump.J_p|pump.L|pump.Q_t|pump.W_t|pump.Xi_in.1.|pump.Xi_in.2.|pump.Xi_out.1.|pump.Xi_out.2.|pump.clip_p_out|der.pump.m_flow.|pump.dh|pump.dp|pump.dr_corr|pump.eta|pump.h_in|pump.h_out|pump.initM_flow|pump.initOmega|der.pump.inlet.m_flow.|pump.inlet.m_flow|pump.inlet.r|pump.inlet.state.T|pump.inlet.state.X.1.|pump.inlet.state.X.2.|pump.inlet.state.p|pump.m_acceleration_0|pump.m_flow|pump.m_flowStateSelect|pump.m_flow_0|pump.m_flow_reg|pump.max_rel_volume|pump.omega|pump.omegaStateSelect|pump.omega_0|pump.omega_dot_0|pump.omega_input|pump.omega_reg|pump.outlet.m_flow|pump.outlet.r|pump.outlet.state.T|pump.outlet.state.X.1.|pump.outlet.state.X.2.|pump.outlet.state.p|pump.outputQuantity|pump.p_in|pump.p_min|pump.p_out|pump.phi|pump.phi_0|pump.rho_min|pump.tau|pump.tau_normalized|pump.tau_st|pump.v_in|pump.v_out|refFlow_setPoint2.y|reservoir.A|reservoir.A_surf|reservoir.L|reservoir.M|reservoir.MXi.1.|reservoir.MXi.2.|reservoir.Q_flow|reservoir.T_heatPort|reservoir.T_start|reservoir.U|reservoir.U_med|reservoir.V|reservoir.W_v|reservoir.Xi_0.1.|reservoir.Xi_0.2.|reservoir.Xi_in.1.|reservoir.Xi_in.2.|reservoir.Xi_out.1.|reservoir.Xi_out.2.|reservoir.d|reservoir.density_derp_h|der.reservoir.M.|der.reservoir.MXi.1..|der.reservoir.MXi.2..|der.reservoir.U_med.|der.reservoir.V.|der.reservoir.m_flow_in.|der.reservoir.m_flow_out.|reservoir.g|reservoir.h_in|reservoir.h_out|reservoir.h_start|reservoir.height|reservoir.height_0|reservoir.height_min|reservoir.inlet.m_flow|reservoir.inlet.r|reservoir.inlet.state.T|reservoir.inlet.state.X.1.|reservoir.inlet.state.X.2.|reservoir.inlet.state.p|reservoir.k_volume_damping|reservoir.m_flow_assert|reservoir.m_flow_in|reservoir.m_flow_out|reservoir.medium.MM|reservoir.medium.R_s|reservoir.medium.T|reservoir.medium.T_degC|reservoir.medium.X.1.|reservoir.medium.X.2.|reservoir.medium.Xi.1.|reservoir.medium.Xi.2.|reservoir.medium.d|der.reservoir.medium.X.1..|der.reservoir.medium.X.2..|der.reservoir.medium.d.|der.reservoir.medium.h.|der.reservoir.medium.u.|reservoir.medium.h|reservoir.medium.p|reservoir.medium.p_bar|reservoir.medium.preferredMediumStates|reservoir.medium.standardOrderComponents|reservoir.medium.state.T|reservoir.medium.state.X.1.|reservoir.medium.state.X.2.|reservoir.medium.state.p|reservoir.medium.u|reservoir.outlet.m_flow|reservoir.outlet.r|reservoir.outlet.state.T|reservoir.outlet.state.X.1.|reservoir.outlet.state.X.2.|reservoir.outlet.state.p|reservoir.p_env|reservoir.p_env_par|reservoir.p_in|reservoir.p_start|reservoir.r|reservoir.r_damping|reservoir.r_in|reservoir.r_out|reservoir.state_in.T|reservoir.state_in.X.1.|reservoir.state_in.X.2.|reservoir.state_in.p|reservoir.state_out.T|reservoir.state_out.X.1.|reservoir.state_out.X.2.|reservoir.state_out.p",fileNamePrefix="ThermofluidStream_dev_ThermofluidStream.Media.additionalMedia.SingleGasAndIncompressible.Tests.TestSimpleLoopJP8DryAir") [Timeout 660] "Notification: Performance of FrontEnd - Absyn->SCode: time 1.909e-05/1.909e-05, allocations: 2.312 kB / 480.6 MB, free: 42.48 MB / 446.1 MB Notification: Performance of NFInst.instantiate(ThermofluidStream.Media.additionalMedia.SingleGasAndIncompressible.Tests.TestSimpleLoopJP8DryAir): time 0.2404/0.2404, allocations: 206.2 MB / 0.6707 GB, free: 9.695 MB / 0.5762 GB Notification: Performance of NFInst.instExpressions: time 0.3346/0.575, allocations: 29.39 MB / 0.6994 GB, free: 2.309 MB / 0.5919 GB Notification: Performance of NFInst.updateImplicitVariability: time 0.001156/0.5762, allocations: 47.64 kB / 0.6995 GB, free: 2.309 MB / 0.5919 GB Notification: Performance of NFTyping.typeComponents: time 0.001617/0.5778, allocations: 0.5543 MB / 0.7 GB, free: 2.309 MB / 0.5919 GB Notification: Performance of NFTyping.typeBindings: time 0.006807/0.5846, allocations: 2.752 MB / 0.7027 GB, free: 2.309 MB / 0.5919 GB Notification: Performance of NFTyping.typeClassSections: time 0.003733/0.5883, allocations: 1.663 MB / 0.7043 GB, free: 2.309 MB / 0.5919 GB Notification: Performance of NFFlatten.flatten: time 0.002278/0.5906, allocations: 1.919 MB / 0.7062 GB, free: 2.309 MB / 0.5919 GB Notification: Performance of NFFlatten.resolveConnections: time 0.0003396/0.5909, allocations: 159 kB / 0.7064 GB, free: 2.281 MB / 0.5919 GB Notification: Performance of NFEvalConstants.evaluate: time 0.002645/0.5936, allocations: 1.611 MB / 0.7079 GB, free: 2.281 MB / 0.5919 GB Notification: Performance of NFSimplifyModel.simplify: time 0.0005707/0.5942, allocations: 486.6 kB / 0.7084 GB, free: 2.25 MB / 0.5919 GB Notification: Performance of NFPackage.collectConstants: time 0.0001279/0.5943, allocations: 79.34 kB / 0.7085 GB, free: 2.25 MB / 0.5919 GB Notification: Performance of NFFlatten.collectFunctions: time 0.008175/0.6025, allocations: 4.383 MB / 0.7128 GB, free: 2.062 MB / 0.5919 GB Notification: Performance of combineBinaries: time 0.001505/0.604, allocations: 2.016 MB / 0.7147 GB, free: 1.277 MB / 0.5919 GB Notification: Performance of replaceArrayConstructors: time 0.0006773/0.6046, allocations: 1.297 MB / 0.716 GB, free: 0.6289 MB / 0.5919 GB Notification: Performance of NFVerifyModel.verify: time 0.0002521/0.6049, allocations: 101.4 kB / 0.7161 GB, free: 0.6289 MB / 0.5919 GB Notification: Performance of FrontEnd: time 0.0003351/0.6052, allocations: 88.59 kB / 0.7162 GB, free: 0.6172 MB / 0.5919 GB Notification: Model statistics after passing the front-end and creating the data structures used by the back-end: * Number of equations: 212 (173) * Number of variables: 216 (189) Notification: Performance of [SIM] Bindings: time 0.005526/0.6108, allocations: 5.662 MB / 0.7217 GB, free: 14.64 MB / 0.6075 GB Notification: Performance of [SIM] FunctionAlias: time 0.0009917/0.6118, allocations: 0.8696 MB / 0.7226 GB, free: 14.53 MB / 0.6075 GB Notification: Performance of [SIM] Early Inline: time 0.00698/0.6187, allocations: 5.944 MB / 0.7284 GB, free: 13.71 MB / 0.6075 GB Notification: Performance of [SIM] Simplify 1: time 0.0007761/0.6195, allocations: 433.6 kB / 0.7288 GB, free: 13.61 MB / 0.6075 GB Notification: Performance of [SIM] Alias: time 0.007029/0.6265, allocations: 4.258 MB / 0.7329 GB, free: 12.32 MB / 0.6075 GB Notification: Performance of [SIM] Simplify 2: time 0.0009052/0.6274, allocations: 374.8 kB / 0.7333 GB, free: 12.2 MB / 0.6075 GB Notification: Performance of [SIM] Remove Stream: time 0.0005916/0.628, allocations: 289.8 kB / 0.7336 GB, free: 12.11 MB / 0.6075 GB Notification: Performance of [SIM] Detect States: time 0.001569/0.6296, allocations: 0.9004 MB / 0.7344 GB, free: 11.89 MB / 0.6075 GB Notification: Performance of [SIM] Events: time 0.0002462/0.6299, allocations: 118.7 kB / 0.7346 GB, free: 11.88 MB / 0.6075 GB Notification: Performance of [SIM] Partitioning: time 0.002339/0.6322, allocations: 1.202 MB / 0.7357 GB, free: 11.67 MB / 0.6075 GB Error: Internal error NBSorting.tarjan failed to sort system: System Variables (152/182) **************************** (1|1) [ALGB] (1) input Real pump.inlet.state.T (start = 288.15, min = 0.0, nominal = 300.0) (2|2) [ALGB] (1) output Real multiSensor_Tpm2.outlet.state.T (start = 288.15, min = 0.0, nominal = 300.0) (3|3) [ALGB] (1) input Real pump.inlet.state.p (min = 0.0, nominal = 1e5) (4|4) [ALGB] (1) protected Real reservoir.r (5|5) [ALGB] (2) Real[2] pump.Xi_out (min = max(fill(0.0, 2), {0.0 for $f3 in 1:2}, {0.0 for $f3 in 1:2}), max = max(fill(1.0, 2), {1.0 for $f2 in 1:2}, {1.0 for $f2 in 1:2}), nominal = {0.1 for $f1 in 1:2}) (6|7) [ALGB] (1) input Real conductionElement.inlet.state.p (min = 0.0, nominal = 1e5) (7|8) [ALGB] (1) Real pump.eta = if noEvent(abs(pump.W_t) > 1e-4) then (pump.v_in * pump.dp * flowResistance1.m_flow) / pump.W_t else 0.0 (8|9) [ALGB] (2) Real[2] reservoir.medium.state.X (min = {0.0 for $f3 in 1:2}, max = {1.0 for $f2 in 1:2}, nominal = {0.1 for $f1 in 1:2}) (9|11) [DER-] (1) Real $DER.reservoir.U_med (10|12) [ALGB] (1) Real conductionElement.M (min = 0.0) (11|13) [ALGB] (1) Real flowResistance1.p_in = ThermofluidStream.Media.additionalMedia.SingleGasAndIncompressible.Tests.TestSimpleLoopJP8DryAir.flowResistance1.Medium.pressure(flowResistance1.inlet.state) (start = 1e5, min = 0.0, max = 1e8, nominal = 1e5) (12|14) [ALGB] (2) output Real[2] reservoir.outlet.state.X = reservoir.state_out.X (min = {0.0 for $f3 in 1:2}, max = {1.0 for $f2 in 1:2}, nominal = {0.1 for $f1 in 1:2}) (13|16) [ALGB] (1) Real $FUN_6.p (14|17) [DDER] (1) Real $DER.conductionElement.m_flow (StateSelect = avoid) (15|18) [ALGB] (1) output Real conductionElement.outlet.state.p (min = 0.0, nominal = 1e5) (16|19) [ALGB] (1) Real $FUN_5.p (17|20) [DER-] (2) Real[2] $DER.reservoir.MXi (18|22) [ALGB] (1) Real $FUN_2.p (19|23) [ALGB] (1) output Real multiSensor_Tpm2.outlet.state.p (min = 0.0, nominal = 1e5) (20|24) [ALGB] (1) protected Real reservoir.h_in = if noEvent(flowResistance1.m_flow >= 0.0) then ThermofluidStream.Media.additionalMedia.SingleGasAndIncompressible.Tests.TestSimpleLoopJP8DryAir.reservoir.Medium.specificEnthalpy(reservoir.state_in) else reservoir.medium.h (min = -1e10, max = 1e10, nominal = 1e6) (21|25) [ALGB] (2) output Real[2] flowResistance1.outlet.state.X (min = {0.0 for $f3 in 1:2}, max = {1.0 for $f2 in 1:2}, nominal = {0.1 for $f1 in 1:2}) (22|27) [ALGB] (1) input Real differenceSensor_Tp.inletB.state.T (start = 288.15, min = 0.0, nominal = 300.0) (23|28) [ALGB] (1) Real $FUN_42.p (24|29) [ALGB] (2) protected Real[2] reservoir.state_in.X (min = {0.0 for $f3 in 1:2}, max = {1.0 for $f2 in 1:2}, nominal = {0.1 for $f1 in 1:2}) (25|31) [ALGB] (1) output Real conductionElement.outlet.state.T (start = 288.15, min = 0.0, nominal = 300.0) (26|32) [ALGB] (1) Real $FUN_38 (start = 1.0, min = 0.0, max = 1e5, nominal = 1.0) (27|33) [ALGB] (1) output Real pump.outlet.state.p (min = 0.0, nominal = 1e5) (28|34) [ALGB] (1) Real $FUN_33 (29|35) [ALGB] (1) output Real flowResistance1.outlet.state.T (start = 288.15, min = 0.0, nominal = 300.0) (30|36) [ALGB] (1) Real $FUN_32 (start = 1.0, min = 0.0, max = 1e5, nominal = 1.0) (31|37) [ALGB] (1) input Real differenceSensor_Tp.inletA.state.p (min = 0.0, nominal = 1e5) (32|38) [ALGB] (1) Real pump.h_in = ThermofluidStream.Media.additionalMedia.SingleGasAndIncompressible.Tests.TestSimpleLoopJP8DryAir.pump.Medium.specificEnthalpy(pump.inlet.state) (min = -1e10, max = 1e10, nominal = 1e6) (33|39) [ALGB] (2) Real[2] reservoir.medium.X (start = {1e-4, 0.9999}, min = {0.0 for $f3 in 1:2}, max = {1.0 for $f2 in 1:2}, nominal = {0.1 for $f1 in 1:2}) (34|41) [ALGB] (1) output Real flowResistance1.outlet.state.p (min = 0.0, nominal = 1e5) (35|42) [ALGB] (1) Real conductionElement.T = ThermofluidStream.Media.additionalMedia.SingleGasAndIncompressible.Tests.TestSimpleLoopJP8DryAir.conductionElement.Medium.temperature(conductionElement.state) (start = 288.15, min = 1.0, max = 1e4, nominal = 300.0) (36|43) [ALGB] (2) input Real[2] reservoir.inlet.state.X = reservoir.state_in.X (min = {0.0 for $f3 in 1:2}, max = {1.0 for $f2 in 1:2}, nominal = {0.1 for $f1 in 1:2}) (37|45) [ALGB] (2) Real[2] conductionElement.Xi_out (min = max(fill(0.0, 2), {0.0 for $f3 in 1:2}, {0.0 for $f3 in 1:2}), max = max(fill(1.0, 2), {1.0 for $f2 in 1:2}, {1.0 for $f2 in 1:2}), nominal = {0.1 for $f1 in 1:2}) (38|47) [ALGB] (2) Real[2] flowResistance1.Xi_out (min = max(fill(0.0, 2), {0.0 for $f3 in 1:2}, {0.0 for $f3 in 1:2}), max = max(fill(1.0, 2), {1.0 for $f2 in 1:2}, {1.0 for $f2 in 1:2}), nominal = {0.1 for $f1 in 1:2}) (39|49) [ALGB] (2) Real[2] $FUN_42.X (40|51) [DDER] (1) Real $DER.reservoir.m_flow_out (StateSelect = avoid) (41|52) [ALGB] (1) Real conductionElement.state.T (start = 288.15, min = 0.0, nominal = 300.0) (42|53) [ALGB] (1) Real $FUN_27 (start = 1.0, min = 0.0, max = 1e5, nominal = 1.0) (43|54) [ALGB] (1) protected Real flowResistance1.rho_in = max(flowResistance1.rho_min, ThermofluidStream.Media.additionalMedia.SingleGasAndIncompressible.Tests.TestSimpleLoopJP8DryAir.flowResistance1.Medium.density(flowResistance1.inlet.state)) (start = 1.0, min = 0.0, max = 1e5, nominal = 1.0) (44|55) [ALGB] (1) protected Real reservoir.r_out (45|56) [ALGB] (1) Real conductionElement.state.p (min = 0.0, nominal = 1e5) (46|57) [ALGB] (1) protected Real reservoir.state_out.T (start = 288.15, min = 0.0, nominal = 300.0) (47|58) [ALGB] (1) protected Real reservoir.state_in.T (start = 288.15, min = 0.0, nominal = 300.0) (48|59) [ALGB] (1) Real $FUN_24 (49|60) [ALGB] (1) protected Real pump.v_in = 1.0 / max(pump.rho_min, ThermofluidStream.Media.additionalMedia.SingleGasAndIncompressible.Tests.TestSimpleLoopJP8DryAir.pump.Medium.density(pump.inlet.state)) (min = 0.0) (50|61) [ALGB] (1) Real $FUN_23 (51|62) [ALGB] (1) Real differenceSensor_Tp.p (52|63) [ALGB] (1) Real pump.dr_corr (53|64) [ALGB] (1) Real $FUN_21 (min = -1e10, max = 1e10, nominal = 1e6) (54|65) [ALGB] (2) Real[2] $FUN_20 (min = fill(0.0, 2), max = fill(1.0, 2), nominal = fill(0.1, 2)) (55|67) [ALGB] (1) protected Real pump.v_out = 1.0 / max(pump.rho_min, ThermofluidStream.Media.additionalMedia.SingleGasAndIncompressible.Tests.TestSimpleLoopJP8DryAir.pump.Medium.density(pump.inlet.state)) (min = 0.0) (56|68) [ALGB] (1) input Real reservoir.inlet.state.p = reservoir.state_in.p (min = 0.0, nominal = 1e5) (57|69) [ALGB] (1) Real reservoir.Q_flow (58|70) [ALGB] (1) Real conductionElement.k (59|71) [ALGB] (1) Real pump.W_t (60|72) [ALGB] (2) input Real[2] differenceSensor_Tp.inletA.state.X (min = {0.0 for $f3 in 1:2}, max = {1.0 for $f2 in 1:2}, nominal = {0.1 for $f1 in 1:2}) (61|74) [ALGB] (1) Real reservoir.medium.p (start = 1e5, min = 0.0, max = 1e8, nominal = 1e5, StateSelect = default) (62|75) [ALGB] (1) output Real reservoir.outlet.state.p = reservoir.state_out.p (min = 0.0, nominal = 1e5) (63|76) [ALGB] (2) output Real[2] multiSensor_Tpm2.outlet.state.X (min = {0.0 for $f3 in 1:2}, max = {1.0 for $f2 in 1:2}, nominal = {0.1 for $f1 in 1:2}) (64|78) [ALGB] (1) protected Real reservoir.state_in.p (min = 0.0, nominal = 1e5) (65|79) [ALGB] (1) input Real flowResistance1.inlet.state.T (start = 288.15, min = 0.0, nominal = 300.0) (66|80) [ALGB] (2) Real[2] reservoir.medium.Xi (start = {1e-4, 0.9999}, min = {0.0 for $f3 in 1:2}, max = {1.0 for $f2 in 1:2}, StateSelect = default) (67|82) [ALGB] (1) input Real differenceSensor_Tp.inletB.state.p (min = 0.0, nominal = 1e5) (68|83) [ALGB] (1) protected Real conductionElement.h_in_norm = if noEvent(conductionElement.m_flow >= 0.0) then conductionElement.h_in else conductionElement.h_out (min = -1e10, max = 1e10, nominal = 1e6) (69|84) [ALGB] (1) Real $FUN_19 (min = -1e10, max = 1e10, nominal = 1e6) (70|85) [ALGB] (2) Real[2] $FUN_18 (min = fill(0.0, 2), max = fill(1.0, 2), nominal = fill(0.1, 2)) (71|87) [DER-] (1) Real $DER.reservoir.V (72|88) [DER-] (1) Real $DER.flowResistance1.m_flow (73|89) [ALGB] (1) output Real reservoir.outlet.state.T = reservoir.state_out.T (start = 288.15, min = 0.0, nominal = 300.0) (74|90) [ALGB] (1) Real flowResistance1.h_out (min = -1e10, max = 1e10, nominal = 1e6) (75|91) [ALGB] (1) protected Real pump.dh (min = -1e8, max = 1e8, nominal = 1e6) (76|92) [DER-] (1) Real $DER.reservoir.M (77|93) [ALGB] (1) Real conductionElement.p_in = ThermofluidStream.Media.additionalMedia.SingleGasAndIncompressible.Tests.TestSimpleLoopJP8DryAir.conductionElement.Medium.pressure(conductionElement.inlet.state) (start = 1e5, min = 0.0, max = 1e8, nominal = 1e5) (78|94) [ALGB] (1) Real reservoir.medium.MM (min = 0.001, max = 0.25, nominal = 0.032) (79|95) [ALGB] (1) input Real differenceSensor_Tp.inletA.state.T (start = 288.15, min = 0.0, nominal = 300.0) (80|96) [ALGB] (1) Real reservoir.height (min = 0.0) (81|97) [ALGB] (1) Real pump.h_out (min = -1e10, max = 1e10, nominal = 1e6) (82|98) [ALGB] (1) protected Real reservoir.state_out.p (min = 0.0, nominal = 1e5) (83|99) [ALGB] (1) Real feedback2.y (84|100) [DISC] (1) Boolean $SEV_1 (85|101) [ALGB] (2) output Real[2] pump.outlet.state.X (min = {0.0 for $f3 in 1:2}, max = {1.0 for $f2 in 1:2}, nominal = {0.1 for $f1 in 1:2}) (86|103) [ALGB] (2) output Real[2] conductionElement.outlet.state.X (min = {0.0 for $f3 in 1:2}, max = {1.0 for $f2 in 1:2}, nominal = {0.1 for $f1 in 1:2}) (87|105) [DISC] (1) Boolean $SEV_0 (88|106) [ALGB] (1) Real reservoir.W_v (89|107) [ALGB] (1) Real conductionElement.p_out (start = 1e5, min = 0.0, max = 1e8, nominal = 1e5) (90|108) [ALGB] (1) Real pump.Q_t (91|109) [ALGB] (1) Real pump.inlet.r (92|110) [ALGB] (2) Real[2] conductionElement.state.X (min = {0.0 for $f3 in 1:2}, max = {1.0 for $f2 in 1:2}, nominal = {0.1 for $f1 in 1:2}) (93|112) [ALGB] (1) Real pump.p_out (start = 1e5, min = 0.0, max = 1e8, nominal = 1e5) (94|113) [ALGB] (1) protected Real conductionElement.rho = max(conductionElement.rho_min, ThermofluidStream.Media.additionalMedia.SingleGasAndIncompressible.Tests.TestSimpleLoopJP8DryAir.conductionElement.Medium.density(conductionElement.state)) (start = 1.0, min = 0.0, max = 1e5, nominal = 1.0) (95|114) [ALGB] (1) Real $FUN_6.T (96|115) [ALGB] (1) Real $FUN_5.T (97|116) [ALGB] (2) protected Real[2] reservoir.state_out.X (min = {0.0 for $f3 in 1:2}, max = {1.0 for $f2 in 1:2}, nominal = {0.1 for $f1 in 1:2}) (98|118) [ALGB] (1) Real $FUN_2.T (99|119) [ALGB] (1) protected Real reservoir.p_in = ThermofluidStream.Media.additionalMedia.SingleGasAndIncompressible.Tests.TestSimpleLoopJP8DryAir.reservoir.Medium.pressure(reservoir.state_in) (start = 1e5, min = 0.0, max = 1e8, nominal = 1e5) (100|120) [ALGB] (1) Real reservoir.medium.h (min = -1e10, max = 1e10, nominal = 1e6) (101|121) [ALGB] (1) protected Real conductionElement.T_heatPort (start = 288.15, min = 1.0, max = 1e4, nominal = 300.0) (102|122) [ALGB] (1) Real multiSensor_Tpm2.T (min = -272.15, max = 9726.85) (103|123) [ALGB] (1) input Real multiSensor_Tpm2.inlet.state.p (min = 0.0, nominal = 1e5) (104|124) [ALGB] (1) protected Real reservoir.h_out = if noEvent((-reservoir.m_flow_out) >= 0.0) then ThermofluidStream.Media.additionalMedia.SingleGasAndIncompressible.Tests.TestSimpleLoopJP8DryAir.reservoir.Medium.specificEnthalpy(reservoir.state_out) else reservoir.medium.h (min = -1e10, max = 1e10, nominal = 1e6) (105|125) [ALGB] (1) protected Real flowResistance1.mu_in = ThermofluidStream.Media.additionalMedia.SingleGasAndIncompressible.Tests.TestSimpleLoopJP8DryAir.flowResistance1.Medium.dynamicViscosity(flowResistance1.inlet.state) (start = 0.001, min = 0.0, max = 1e8, nominal = 0.001) (106|126) [ALGB] (1) input Real flowResistance1.inlet.state.p (min = 0.0, nominal = 1e5) (107|127) [ALGB] (1) Real pump.dp (108|128) [ALGB] (1) input Real conductionElement.inlet.state.T (start = 288.15, min = 0.0, nominal = 300.0) (109|129) [ALGB] (1) protected Real differenceSensor_Tp.pA (start = 1e5, min = 0.0, max = 1e8, nominal = 1e5) (110|130) [ALGB] (1) Real reservoir.medium.state.p (min = 0.0, nominal = 1e5) (111|131) [ALGB] (1) Real reservoir.medium.R_s (start = 1000.0, min = 0.0, max = 1e7, nominal = 1000.0) (112|132) [ALGB] (1) protected Real conductionElement.Q_flow (113|133) [ALGB] (1) Real conductionElement.h_in = ThermofluidStream.Media.additionalMedia.SingleGasAndIncompressible.Tests.TestSimpleLoopJP8DryAir.conductionElement.Medium.specificEnthalpy(conductionElement.inlet.state) (min = -1e10, max = 1e10, nominal = 1e6) (114|134) [ALGB] (1) Real flowResistance1.p_out (start = 1e5, min = 0.0, max = 1e8, nominal = 1e5) (115|135) [DER-] (1) Real $DER.PI2.x (116|136) [ALGB] (1) Real pump.tau_st (117|137) [ALGB] (1) protected Real pump.omega (StateSelect = default) (118|138) [ALGB] (1) Real reservoir.medium.u (min = -1e8, max = 1e8, nominal = 1e6) (119|139) [ALGB] (1) protected Real differenceSensor_Tp.TA (start = 288.15, min = 1.0, max = 1e4, nominal = 300.0) (120|140) [ALGB] (1) protected Real pump.tau_normalized (121|141) [ALGB] (2) protected Real[2] reservoir.Xi_out = if noEvent((-reservoir.m_flow_out) >= 0.0) then ThermofluidStream.Media.additionalMedia.SingleGasAndIncompressible.Tests.TestSimpleLoopJP8DryAir.reservoir.Medium.massFraction(reservoir.state_out) else reservoir.medium.Xi (min = {0.0 for $f3 in 1:2}, max = {1.0 for $f2 in 1:2}, nominal = {0.1 for $f1 in 1:2}) (122|143) [ALGB] (1) Real reservoir.medium.state.T (start = 288.15, min = 0.0, nominal = 300.0) (123|144) [ALGB] (1) Real pump.outlet.r (124|145) [ALGB] (1) output Real pump.outlet.state.T (start = 288.15, min = 0.0, nominal = 300.0) (125|146) [ALGB] (1) Real multiSensor_Tpm2.p (min = 0.0, max = 1000.0000000000001) (126|147) [ALGB] (2) input Real[2] multiSensor_Tpm2.inlet.state.X (min = {0.0 for $f3 in 1:2}, max = {1.0 for $f2 in 1:2}, nominal = {0.1 for $f1 in 1:2}) (127|149) [ALGB] (2) input Real[2] differenceSensor_Tp.inletB.state.X (min = {0.0 for $f3 in 1:2}, max = {1.0 for $f2 in 1:2}, nominal = {0.1 for $f1 in 1:2}) (128|151) [ALGB] (2) Real[2] $FUN_6.X (129|153) [ALGB] (1) protected Real limiter2.simplifiedExpr (130|154) [ALGB] (2) Real[2] $FUN_5.X (131|156) [ALGB] (2) Real[2] $FUN_2.X (132|158) [ALGB] (2) input Real[2] conductionElement.inlet.state.X (min = {0.0 for $f3 in 1:2}, max = {1.0 for $f2 in 1:2}, nominal = {0.1 for $f1 in 1:2}) (133|160) [ALGB] (1) input Real multiSensor_Tpm2.inlet.state.T (start = 288.15, min = 0.0, nominal = 300.0) (134|161) [ALGB] (1) Real differenceSensor_Tp.T (135|162) [ALGB] (1) protected Real reservoir.r_damping = reservoir.d * der(reservoir.M) (136|163) [ALGB] (1) Real pump.p_in = ThermofluidStream.Media.additionalMedia.SingleGasAndIncompressible.Tests.TestSimpleLoopJP8DryAir.pump.Medium.pressure(pump.inlet.state) (start = 1e5, min = 0.0, max = 1e8, nominal = 1e5) (137|164) [DER-] (1) Real $DER.conductionElement.h_out (138|165) [ALGB] (1) input Real reservoir.inlet.state.T = reservoir.state_in.T (start = 288.15, min = 0.0, nominal = 300.0) (139|166) [ALGB] (1) protected Real differenceSensor_Tp.pB (start = 1e5, min = 0.0, max = 1e8, nominal = 1e5) (140|167) [ALGB] (1) protected Real reservoir.T_heatPort (start = 288.15, min = 1.0, max = 1e4, nominal = 300.0) (141|168) [ALGB] (1) protected Real reservoir.r_in (142|169) [ALGB] (1) Real reservoir.medium.d (start = 1.0, min = 0.0, max = 1e5, nominal = 1.0) (143|170) [ALGB] (2) protected Real[2] reservoir.Xi_in = if noEvent(flowResistance1.m_flow >= 0.0) then ThermofluidStream.Media.additionalMedia.SingleGasAndIncompressible.Tests.TestSimpleLoopJP8DryAir.reservoir.Medium.massFraction(reservoir.state_in) else reservoir.medium.Xi (min = {0.0 for $f3 in 1:2}, max = {1.0 for $f2 in 1:2}, nominal = {0.1 for $f1 in 1:2}) (144|172) [ALGB] (2) input Real[2] flowResistance1.inlet.state.X (min = {0.0 for $f3 in 1:2}, max = {1.0 for $f2 in 1:2}, nominal = {0.1 for $f1 in 1:2}) (145|174) [ALGB] (1) protected Real reservoir.d = reservoir.k_volume_damping * sqrt(abs((2.0 * reservoir.L) / (reservoir.V * max(reservoir.density_derp_h, 1e-10)))) (146|175) [ALGB] (1) Real $FUN_42.T (147|176) [ALGB] (2) input Real[2] pump.inlet.state.X (min = {0.0 for $f3 in 1:2}, max = {1.0 for $f2 in 1:2}, nominal = {0.1 for $f1 in 1:2}) (148|178) [ALGB] (1) protected Real differenceSensor_Tp.TB (start = 288.15, min = 1.0, max = 1e4, nominal = 300.0) (149|179) [ALGB] (1) Real flowResistance1.dr_corr (150|180) [ALGB] (1) protected Real reservoir.density_derp_h (151|181) [DSTA] (1) Real conductionElement.m_flow = conductionElement.m_flow (StateSelect = default) (152|182) [DSTA] (1) protected Real reservoir.m_flow_out System Equations (136/178) **************************** (1|1) [SCAL] (1) pump.outlet.r = (pump.dr_corr + pump.inlet.r) - $DER.flowResistance1.m_flow * pump.L; ($RES_SIM_80) (2|2) [SCAL] (1) conductionElement.rho = max(conductionElement.rho_min, $FUN_27); ($RES_BND_171) (3|3) [ARRY] (2) flowResistance1.outlet.state.X = multiSensor_Tpm2.inlet.state.X; ($RES_SIM_120) (4|5) [SCAL] (1) conductionElement.h_in_norm = if noEvent(conductionElement.m_flow >= 0.0) then conductionElement.h_in else conductionElement.h_out; ($RES_BND_172) (5|6) [SCAL] (1) flowResistance1.outlet.state.T = multiSensor_Tpm2.inlet.state.T; ($RES_SIM_121) (6|7) [SCAL] (1) flowResistance1.outlet.state.p = multiSensor_Tpm2.inlet.state.p; ($RES_SIM_122) (7|8) [SCAL] (1) pump.tau_normalized = if noEvent(pump.W_t >= 0.0) then pump.tau_st else (flowResistance1.m_flow * pump.dh) / noEvent(if abs(pump.omega) > pump.omega_reg then pump.omega else if pump.omega < 0.0 then -pump.omega_reg else pump.omega_reg); ($RES_SIM_84) (8|9) [SCAL] (1) differenceSensor_Tp.inletB.state.X[2] = conductionElement.inlet.state.X[2]; ($RES_SIM_124) (9|10) [SCAL] (1) differenceSensor_Tp.inletB.state.X[2] = reservoir.outlet.state.X[2]; ($RES_SIM_125) (10|11) [SCAL] (1) differenceSensor_Tp.inletB.state.X[1] = conductionElement.inlet.state.X[1]; ($RES_SIM_126) (11|12) [SCAL] (1) pump.Q_t = if noEvent(pump.W_t >= 0.0) then pump.W_t - flowResistance1.m_flow * pump.dh else 0.0; ($RES_SIM_87) (12|13) [SCAL] (1) differenceSensor_Tp.inletB.state.X[1] = reservoir.outlet.state.X[1]; ($RES_SIM_127) (13|14) [SCAL] (1) differenceSensor_Tp.inletB.state.T = conductionElement.inlet.state.T; ($RES_SIM_128) (14|15) [SCAL] (1) differenceSensor_Tp.inletB.state.T = reservoir.outlet.state.T; ($RES_SIM_129) (15|16) [SCAL] (1) feedback2.y = 15.0 - differenceSensor_Tp.T; ($RES_SIM_16) (16|17) [SCAL] (1) reservoir.d = reservoir.k_volume_damping * $FUN_24; ($RES_BND_180) (17|18) [SCAL] (1) differenceSensor_Tp.inletB.state.p = conductionElement.inlet.state.p; ($RES_SIM_130) (18|19) [SCAL] (1) pump.dh = (pump.W_t * flowResistance1.m_flow) / (flowResistance1.m_flow ^ 2.0 + pump.m_flow_reg ^ 2.0); ($RES_SIM_90) (19|20) [SCAL] (1) limiter2.simplifiedExpr = PI2.k * (PI2.x + feedback2.y); ($RES_SIM_17) (20|21) [SCAL] (1) reservoir.r_damping = reservoir.d * $DER.reservoir.M; ($RES_BND_181) (21|22) [SCAL] (1) differenceSensor_Tp.inletB.state.p = reservoir.outlet.state.p; ($RES_SIM_131) (22|23) [SCAL] (1) pump.W_t = pump.tau_st * pump.omega; ($RES_SIM_91) (23|24) [SCAL] (1) $DER.PI2.x = feedback2.y / PI2.T; ($RES_SIM_18) (24|25) [SCAL] (1) pump.omega = homotopy(smooth(0, if $SEV_0 then limiter2.uMax else if $SEV_1 then limiter2.uMin else limiter2.simplifiedExpr), limiter2.simplifiedExpr); ($RES_SIM_19) (25|26) [SCAL] (1) reservoir.h_in = if noEvent(flowResistance1.m_flow >= 0.0) then $FUN_21 else reservoir.medium.h; ($RES_BND_183) (26|27) [SCAL] (1) pump.h_out = pump.h_in + pump.dh; ($RES_SIM_93) (27|28) [ARRY] (2) reservoir.Xi_in = if noEvent(flowResistance1.m_flow >= 0.0) then $FUN_20 else reservoir.medium.Xi; ($RES_BND_184) (28|30) [SCAL] (1) reservoir.h_out = if noEvent((-reservoir.m_flow_out) >= 0.0) then $FUN_19 else reservoir.medium.h; ($RES_BND_185) (29|31) [ARRY] (2) reservoir.Xi_out = if noEvent((-reservoir.m_flow_out) >= 0.0) then $FUN_18 else reservoir.medium.Xi; ($RES_BND_186) (30|33) [RECD] (4) flowResistance1.outlet.state = $FUN_2; ($RES_SIM_96) (31|37) [SCAL] (1) differenceSensor_Tp.inletA.state.X[2] = pump.inlet.state.X[2]; ($RES_SIM_136) (32|38) [SCAL] (1) flowResistance1.dr_corr = flowResistance1.p_in - (flowResistance1.p_out + 1e4 * flowResistance1.m_flow); ($RES_SIM_97) (33|39) [SCAL] (1) differenceSensor_Tp.inletA.state.X[2] = conductionElement.outlet.state.X[2]; ($RES_SIM_137) (34|40) [SCAL] (1) flowResistance1.p_out = max(flowResistance1.p_min, flowResistance1.p_in - 1e4 * flowResistance1.m_flow); ($RES_SIM_98) (35|41) [RECD] (4) conductionElement.state = $FUN_42; ($RES_BND_189) (36|45) [SCAL] (1) differenceSensor_Tp.inletA.state.X[1] = pump.inlet.state.X[1]; ($RES_SIM_138) (37|46) [SCAL] (1) reservoir.r_in = (flowResistance1.dr_corr + pump.outlet.r) - $DER.flowResistance1.m_flow * flowResistance1.L; ($RES_SIM_99) (38|47) [SCAL] (1) differenceSensor_Tp.inletA.state.X[1] = conductionElement.outlet.state.X[1]; ($RES_SIM_139) (39|48) [SCAL] (1) flowResistance1.p_in = flowResistance1.inlet.state.p; ($RES_AUX_193) (40|49) [SCAL] (1) flowResistance1.h_out = {ThermofluidStream.Media.myMedia.IdealGases.Common.Functions.h_T(ThermofluidStream.Media.myMedia.IdealGases.Common.DataRecord(\"Air\", 0.0289651159, -4333.833858403446, 298609.6803431054, 1000.0, {10099.5016, -196.827561, 5.00915511, -0.00576101373, 1.06685993e-5, -7.94029797e-9, 2.18523191e-12}, {-176.796731, -3.921504225}, {241521.443, -1257.8746, 5.14455867, -2.13854179e-4, 7.06522784e-8, -1.07148349e-11, 6.57780015e-16}, {6462.26319, -8.147411905}, 287.0512249529787), flowResistance1.inlet.state.T, true, ThermofluidStream.Media.myMedia.Interfaces.Choices.ReferenceEnthalpy.ZeroAt0K, 0.0), Modelica.Math.Polynomials.integralValue({4.333333333333335, 1869.9999999999995}, (-273.15) + flowResistance1.inlet.state.T, 0.0)} * flowResistance1.inlet.state.X; ($RES_AUX_194) (41|50) [ARRY] (2) flowResistance1.Xi_out = flowResistance1.inlet.state.X; ($RES_AUX_195) (42|52) [SCAL] (1) $FUN_38 = (Modelica.Math.Polynomials.evaluate({-0.7230769230769221, 823.076923076923}, (-273.15) + flowResistance1.inlet.state.T) * ((0.0034836987724536205 * flowResistance1.inlet.state.p) / flowResistance1.inlet.state.T)) / (flowResistance1.inlet.state.X * {Modelica.Math.Polynomials.evaluate({-0.7230769230769221, 823.076923076923}, (-273.15) + flowResistance1.inlet.state.T), (0.0034836987724536205 * flowResistance1.inlet.state.p) / flowResistance1.inlet.state.T}); ($RES_AUX_196) (43|53) [SCAL] (1) flowResistance1.mu_in = {1e-6 * Modelica.Math.Polynomials.evaluateWithRange({9.739110288630587e-15, -3.1353724870333906e-11, 4.3004876595642225e-8, -3.822801629175824e-5, 0.05042787436718076, 17.23926013924253}, -149.99999999999997, 1000.0000000000001, (-273.15) + flowResistance1.inlet.state.T), ThermofluidStream.Media.additionalMedia.SingleGasAndIncompressible.Tests.TestSimpleLoopJP8DryAir.flowResistance1.Medium.Incompressible.dynamicViscosity(ThermofluidStream.Media.additionalMedia.SingleGasAndIncompressible.Tests.TestSimpleLoopJP8DryAir.flowResistance1.Medium.Incompressible.ThermodynamicState(flowResistance1.inlet.state.T, flowResistance1.inlet.state.p))} * flowResistance1.inlet.state.X; ($RES_AUX_197) (44|54) [SCAL] (1) pump.p_in = pump.inlet.state.p; ($RES_AUX_198) (45|55) [SCAL] (1) pump.h_in = {ThermofluidStream.Media.myMedia.IdealGases.Common.Functions.h_T(ThermofluidStream.Media.myMedia.IdealGases.Common.DataRecord(\"Air\", 0.0289651159, -4333.833858403446, 298609.6803431054, 1000.0, {10099.5016, -196.827561, 5.00915511, -0.00576101373, 1.06685993e-5, -7.94029797e-9, 2.18523191e-12}, {-176.796731, -3.921504225}, {241521.443, -1257.8746, 5.14455867, -2.13854179e-4, 7.06522784e-8, -1.07148349e-11, 6.57780015e-16}, {6462.26319, -8.147411905}, 287.0512249529787), pump.inlet.state.T, true, ThermofluidStream.Media.myMedia.Interfaces.Choices.ReferenceEnthalpy.ZeroAt0K, 0.0), Modelica.Math.Polynomials.integralValue({4.333333333333335, 1869.9999999999995}, (-273.15) + pump.inlet.state.T, 0.0)} * pump.inlet.state.X; ($RES_AUX_199) (46|56) [RECD] (4) reservoir.inlet.state = reservoir.state_in; ($RES_BND_190) (47|60) [RECD] (4) reservoir.outlet.state = reservoir.state_out; ($RES_BND_191) (48|64) [SCAL] (1) differenceSensor_Tp.inletA.state.T = pump.inlet.state.T; ($RES_SIM_140) (49|65) [RECD] (4) multiSensor_Tpm2.outlet.state = multiSensor_Tpm2.inlet.state; ($RES_SIM_28) (50|69) [SCAL] (1) differenceSensor_Tp.inletA.state.T = conductionElement.outlet.state.T; ($RES_SIM_141) (51|70) [SCAL] (1) differenceSensor_Tp.inletA.state.p = pump.inlet.state.p; ($RES_SIM_142) (52|71) [ARRY] (2) pump.Xi_out = pump.inlet.state.X; ($RES_AUX_200) (53|73) [SCAL] (1) differenceSensor_Tp.inletA.state.p = conductionElement.outlet.state.p; ($RES_SIM_143) (54|74) [SCAL] (1) $FUN_33 = abs(pump.W_t); ($RES_AUX_201) (55|75) [SCAL] (1) $FUN_32 = (Modelica.Math.Polynomials.evaluate({-0.7230769230769221, 823.076923076923}, (-273.15) + pump.inlet.state.T) * ((0.0034836987724536205 * pump.inlet.state.p) / pump.inlet.state.T)) / (pump.inlet.state.X * {Modelica.Math.Polynomials.evaluate({-0.7230769230769221, 823.076923076923}, (-273.15) + pump.inlet.state.T), (0.0034836987724536205 * pump.inlet.state.p) / pump.inlet.state.T}); ($RES_AUX_202) (56|76) [SCAL] (1) conductionElement.p_in = conductionElement.inlet.state.p; ($RES_AUX_203) (57|77) [ARRY] (2) pump.outlet.state.X = flowResistance1.inlet.state.X; ($RES_SIM_146) (58|79) [SCAL] (1) conductionElement.h_in = {ThermofluidStream.Media.myMedia.IdealGases.Common.Functions.h_T(ThermofluidStream.Media.myMedia.IdealGases.Common.DataRecord(\"Air\", 0.0289651159, -4333.833858403446, 298609.6803431054, 1000.0, {10099.5016, -196.827561, 5.00915511, -0.00576101373, 1.06685993e-5, -7.94029797e-9, 2.18523191e-12}, {-176.796731, -3.921504225}, {241521.443, -1257.8746, 5.14455867, -2.13854179e-4, 7.06522784e-8, -1.07148349e-11, 6.57780015e-16}, {6462.26319, -8.147411905}, 287.0512249529787), conductionElement.inlet.state.T, true, ThermofluidStream.Media.myMedia.Interfaces.Choices.ReferenceEnthalpy.ZeroAt0K, 0.0), Modelica.Math.Polynomials.integralValue({4.333333333333335, 1869.9999999999995}, (-273.15) + conductionElement.inlet.state.T, 0.0)} * conductionElement.inlet.state.X; ($RES_AUX_204) (59|80) [SCAL] (1) pump.outlet.state.T = flowResistance1.inlet.state.T; ($RES_SIM_147) (60|81) [ARRY] (2) conductionElement.Xi_out = conductionElement.inlet.state.X; ($RES_AUX_205) (61|83) [SCAL] (1) pump.outlet.state.p = flowResistance1.inlet.state.p; ($RES_SIM_148) (62|84) [SCAL] (1) conductionElement.T = conductionElement.state.T; ($RES_AUX_206) (63|85) [SCAL] (1) $FUN_27 = (Modelica.Math.Polynomials.evaluate({-0.7230769230769221, 823.076923076923}, (-273.15) + conductionElement.state.T) * ((0.0034836987724536205 * conductionElement.state.p) / conductionElement.state.T)) / (conductionElement.state.X * {Modelica.Math.Polynomials.evaluate({-0.7230769230769221, 823.076923076923}, (-273.15) + conductionElement.state.T), (0.0034836987724536205 * conductionElement.state.p) / conductionElement.state.T}); ($RES_AUX_207) (64|86) [SCAL] (1) reservoir.Q_flow = 0.0; ($RES_SIM_32) (65|87) [ARRY] (2) $DER.reservoir.MXi = reservoir.Xi_in .* flowResistance1.m_flow + reservoir.Xi_out .* reservoir.m_flow_out; ($RES_SIM_33) (66|89) [SCAL] (1) $DER.reservoir.U_med = reservoir.h_in * flowResistance1.m_flow + reservoir.Q_flow + reservoir.W_v + reservoir.h_out * reservoir.m_flow_out; ($RES_SIM_34) (67|90) [SCAL] (1) $DER.reservoir.M = flowResistance1.m_flow + reservoir.m_flow_out; ($RES_SIM_35) (68|91) [SCAL] (1) reservoir.r + reservoir.p_in = reservoir.medium.p; ($RES_SIM_36) (69|92) [SCAL] (1) $FUN_2.p = flowResistance1.p_out; ($RES_SIM_235) (70|93) [SCAL] (1) $DER.reservoir.m_flow_out * reservoir.L = reservoir.r_out - reservoir.r_damping; ($RES_SIM_37) (71|94) [SCAL] (1) $FUN_2.T = Modelica.Math.Nonlinear.solveOneNonlinearEquation(function ThermofluidStream.Media.additionalMedia.SingleGasAndIncompressible.Tests.TestSimpleLoopJP8DryAir.flowResistance1.Medium.T_hX.f_nonlinear(h = BOX(flowResistance1.h_out), X = BOX(flowResistance1.Xi_out)), 200.0, 6000.0, 2.220446049250313e-14); ($RES_SIM_236) (72|95) [SCAL] (1) $DER.flowResistance1.m_flow * reservoir.L = reservoir.r_in - (reservoir.r_damping + reservoir.r); ($RES_SIM_38) (73|96) [ARRY] (2) $FUN_2.X = flowResistance1.Xi_out; ($RES_SIM_237) (74|98) [SCAL] (1) $FUN_24 = sqrt($FUN_23); ($RES_AUX_210) (75|99) [SCAL] (1) $FUN_5.p = pump.p_out; ($RES_SIM_238) (76|100) [SCAL] (1) $FUN_23 = abs((2.0 * reservoir.L) / (reservoir.V * max(reservoir.density_derp_h, 1e-10))); ($RES_AUX_211) (77|101) [SCAL] (1) $FUN_5.T = Modelica.Math.Nonlinear.solveOneNonlinearEquation(function ThermofluidStream.Media.additionalMedia.SingleGasAndIncompressible.Tests.TestSimpleLoopJP8DryAir.pump.Medium.T_hX.f_nonlinear(h = BOX(pump.h_out), X = BOX(pump.Xi_out)), 200.0, 6000.0, 2.220446049250313e-14); ($RES_SIM_239) (78|102) [SCAL] (1) reservoir.p_in = reservoir.state_in.p; ($RES_AUX_212) (79|103) [SCAL] (1) $FUN_21 = {ThermofluidStream.Media.myMedia.IdealGases.Common.Functions.h_T(ThermofluidStream.Media.myMedia.IdealGases.Common.DataRecord(\"Air\", 0.0289651159, -4333.833858403446, 298609.6803431054, 1000.0, {10099.5016, -196.827561, 5.00915511, -0.00576101373, 1.06685993e-5, -7.94029797e-9, 2.18523191e-12}, {-176.796731, -3.921504225}, {241521.443, -1257.8746, 5.14455867, -2.13854179e-4, 7.06522784e-8, -1.07148349e-11, 6.57780015e-16}, {6462.26319, -8.147411905}, 287.0512249529787), reservoir.state_in.T, true, ThermofluidStream.Media.myMedia.Interfaces.Choices.ReferenceEnthalpy.ZeroAt0K, 0.0), Modelica.Math.Polynomials.integralValue({4.333333333333335, 1869.9999999999995}, (-273.15) + reservoir.state_in.T, 0.0)} * reservoir.state_in.X; ($RES_AUX_213) (80|104) [ARRY] (2) $FUN_20 = reservoir.state_in.X; ($RES_AUX_214) (81|106) [SCAL] (1) $FUN_19 = {ThermofluidStream.Media.myMedia.IdealGases.Common.Functions.h_T(ThermofluidStream.Media.myMedia.IdealGases.Common.DataRecord(\"Air\", 0.0289651159, -4333.833858403446, 298609.6803431054, 1000.0, {10099.5016, -196.827561, 5.00915511, -0.00576101373, 1.06685993e-5, -7.94029797e-9, 2.18523191e-12}, {-176.796731, -3.921504225}, {241521.443, -1257.8746, 5.14455867, -2.13854179e-4, 7.06522784e-8, -1.07148349e-11, 6.57780015e-16}, {6462.26319, -8.147411905}, 287.0512249529787), reservoir.state_out.T, true, ThermofluidStream.Media.myMedia.Interfaces.Choices.ReferenceEnthalpy.ZeroAt0K, 0.0), Modelica.Math.Polynomials.integralValue({4.333333333333335, 1869.9999999999995}, (-273.15) + reservoir.state_out.T, 0.0)} * reservoir.state_out.X; ($RES_AUX_215) (82|107) [ARRY] (2) $FUN_18 = reservoir.state_out.X; ($RES_AUX_216) (83|109) [SCAL] (1) differenceSensor_Tp.pB = differenceSensor_Tp.inletB.state.p; ($RES_AUX_217) (84|110) [SCAL] (1) differenceSensor_Tp.pA = differenceSensor_Tp.inletA.state.p; ($RES_AUX_218) (85|111) [SCAL] (1) differenceSensor_Tp.TB = differenceSensor_Tp.inletB.state.T; ($RES_AUX_219) (86|112) [ARRY] (2) $FUN_5.X = pump.Xi_out; ($RES_SIM_240) (87|114) [RECD] (4) reservoir.state_out = reservoir.medium.state; ($RES_SIM_42) (88|118) [SCAL] (1) $FUN_6.p = conductionElement.p_out; ($RES_SIM_241) (89|119) [SCAL] (1) $FUN_6.T = Modelica.Math.Nonlinear.solveOneNonlinearEquation(function ThermofluidStream.Media.additionalMedia.SingleGasAndIncompressible.Tests.TestSimpleLoopJP8DryAir.conductionElement.Medium.T_hX.f_nonlinear(h = BOX(conductionElement.h_out), X = BOX(conductionElement.Xi_out)), 200.0, 6000.0, 2.220446049250313e-14); ($RES_SIM_242) (90|120) [SCAL] (1) reservoir.W_v = -$DER.reservoir.V * reservoir.p_env_par; ($RES_SIM_44) (91|121) [SCAL] (1) reservoir.medium.p = reservoir.p_env_par + (reservoir.M / reservoir.A_surf) * reservoir.g; ($RES_SIM_45) (92|122) [ARRY] (2) $FUN_6.X = conductionElement.Xi_out; ($RES_SIM_243) (93|124) [SCAL] (1) reservoir.V = reservoir.A_surf * reservoir.height; ($RES_SIM_46) (94|125) [SCAL] (1) $FUN_42.p = conductionElement.p_in; ($RES_SIM_244) (95|126) [SCAL] (1) reservoir.density_derp_h = 1/(reservoir.g * reservoir.height); ($RES_SIM_47) (96|127) [SCAL] (1) $FUN_42.T = Modelica.Math.Nonlinear.solveOneNonlinearEquation(function ThermofluidStream.Media.additionalMedia.SingleGasAndIncompressible.Tests.TestSimpleLoopJP8DryAir.conductionElement.Medium.T_hX.f_nonlinear(h = BOX(conductionElement.h_out), X = BOX(conductionElement.Xi_out)), 200.0, 6000.0, 2.220446049250313e-14); ($RES_SIM_245) (97|128) [ARRY] (2) $FUN_42.X = conductionElement.Xi_out; ($RES_SIM_246) (98|130) [SCAL] (1) differenceSensor_Tp.TA = differenceSensor_Tp.inletA.state.T; ($RES_AUX_220) (99|131) [SCAL] (1) 99999.99999999999 * multiSensor_Tpm2.p = multiSensor_Tpm2.inlet.state.p; ($RES_AUX_222) (100|132) [SCAL] (1) 273.15 + multiSensor_Tpm2.T = multiSensor_Tpm2.inlet.state.T; ($RES_AUX_224) (101|133) [SCAL] (1) reservoir.medium.d = (Modelica.Math.Polynomials.evaluate({-0.7230769230769221, 823.076923076923}, (-273.15) + (ThermofluidStream.Media.additionalMedia.SingleGasAndIncompressible.Tests.TestSimpleLoopJP8DryAir.reservoir.Medium.setState_pTX(reservoir.medium.p, reservoir.T_heatPort, reservoir.medium.X)).T) * ((0.0034836987724536205 * (ThermofluidStream.Media.additionalMedia.SingleGasAndIncompressible.Tests.TestSimpleLoopJP8DryAir.reservoir.Medium.setState_pTX(reservoir.medium.p, reservoir.T_heatPort, reservoir.medium.X)).p) / (ThermofluidStream.Media.additionalMedia.SingleGasAndIncompressible.Tests.TestSimpleLoopJP8DryAir.reservoir.Medium.setState_pTX(reservoir.medium.p, reservoir.T_heatPort, reservoir.medium.X)).T)) / ((ThermofluidStream.Media.additionalMedia.SingleGasAndIncompressible.Tests.TestSimpleLoopJP8DryAir.reservoir.Medium.setState_pTX(reservoir.medium.p, reservoir.T_heatPort, reservoir.medium.X)).X * {Modelica.Math.Polynomials.evaluate({-0.7230769230769221, 823.076923076923}, (-273.15) + (ThermofluidStream.Media.additionalMedia.SingleGasAndIncompressible.Tests.TestSimpleLoopJP8DryAir.reservoir.Medium.setState_pTX(reservoir.medium.p, reservoir.T_heatPort, reservoir.medium.X)).T), (0.0034836987724536205 * (ThermofluidStream.Media.additionalMedia.SingleGasAndIncompressible.Tests.TestSimpleLoopJP8DryAir.reservoir.Medium.setState_pTX(reservoir.medium.p, reservoir.T_heatPort, reservoir.medium.X)).p) / (ThermofluidStream.Media.additionalMedia.SingleGasAndIncompressible.Tests.TestSimpleLoopJP8DryAir.reservoir.Medium.setState_pTX(reservoir.medium.p, reservoir.T_heatPort, reservoir.medium.X)).T}); ($RES_AUX_225) (102|134) [SCAL] (1) reservoir.medium.h = reservoir.medium.X * {ThermofluidStream.Media.myMedia.IdealGases.Common.Functions.h_T(ThermofluidStream.Media.myMedia.IdealGases.Common.DataRecord(\"Air\", 0.0289651159, -4333.833858403446, 298609.6803431054, 1000.0, {10099.5016, -196.827561, 5.00915511, -0.00576101373, 1.06685993e-5, -7.94029797e-9, 2.18523191e-12}, {-176.796731, -3.921504225}, {241521.443, -1257.8746, 5.14455867, -2.13854179e-4, 7.06522784e-8, -1.07148349e-11, 6.57780015e-16}, {6462.26319, -8.147411905}, 287.0512249529787), reservoir.T_heatPort, true, ThermofluidStream.Media.myMedia.Interfaces.Choices.ReferenceEnthalpy.ZeroAt0K, 0.0), Modelica.Math.Polynomials.integralValue({4.333333333333335, 1869.9999999999995}, (-273.15) + reservoir.T_heatPort, 0.0)}; ($RES_AUX_226) (103|135) [SCAL] (1) reservoir.medium.MM = 0.0028965115900000003 / (reservoir.medium.state.X * {0.1, 0.0289651159}); ($RES_AUX_227) (104|136) [SCAL] (1) $SEV_0 = limiter2.simplifiedExpr > limiter2.uMax; ($RES_EVT_255) (105|137) [SCAL] (1) $SEV_1 = limiter2.simplifiedExpr < limiter2.uMin; ($RES_EVT_256) (106|138) [ARRY] (2) reservoir.medium.Xi = reservoir.medium.X[{1, 2}]; ($RES_SIM_51) (107|140) [ARRY] (2) reservoir.medium.state.X = reservoir.medium.X; ($RES_SIM_52) (108|142) [SCAL] (1) reservoir.medium.state.p = reservoir.medium.p; ($RES_SIM_53) (109|143) [SCAL] (1) differenceSensor_Tp.T = differenceSensor_Tp.TA - differenceSensor_Tp.TB; ($RES_SIM_9) (110|144) [SCAL] (1) reservoir.medium.state.T = reservoir.T_heatPort; ($RES_SIM_54) (111|145) [SCAL] (1) differenceSensor_Tp.p = differenceSensor_Tp.pA - differenceSensor_Tp.pB; ($RES_SIM_8) (112|146) [SCAL] (1) reservoir.medium.u = reservoir.medium.h - 1e5 / reservoir.medium.d; ($RES_SIM_56) (113|147) [SCAL] (1) reservoir.medium.R_s = {287.0512249529787, 83.14462618153239} * reservoir.medium.X; ($RES_SIM_57) (114|148) [TUPL] (2) (pump.dp, pump.tau_st) = ThermofluidStream.Media.additionalMedia.SingleGasAndIncompressible.Tests.TestSimpleLoopJP8DryAir.pump.dp_tau(flowResistance1.m_flow, pump.omega, pump.inlet.state, pump.m_flow_reg, pump.omega_reg, pump.rho_min, false, true, 3.661, 0.00306, 314.2, 9.73e-6, 1, 0.016, 1000.0, 4.864e-5, -2.677, 396700.0, 0.5427, 27770.0, 1.218e-6, 1.832e-4, 100.0, \"TestSimpleLoopJP8DryAir.pump\"); ($RES_AUX_230) (115|150) [SCAL] (1) -conductionElement.Q_flow = -4e4 * (1.0 + heating_element.alpha * (conductionElement.T_heatPort - heating_element.T_ref)); ($RES_SIM_60) (116|151) [RECD] (4) conductionElement.outlet.state = $FUN_6; ($RES_SIM_61) (117|155) [SCAL] (1) conductionElement.p_out = conductionElement.p_in; ($RES_SIM_63) (118|156) [SCAL] (1) flowResistance1.rho_in = max(flowResistance1.rho_min, $FUN_38); ($RES_BND_154) (119|157) [SCAL] (1) pump.inlet.r = reservoir.r_out - $DER.conductionElement.m_flow * conductionElement.L; ($RES_SIM_64) (120|158) [SCAL] (1) reservoir.m_flow_out + conductionElement.m_flow = 0.0; ($RES_SIM_107) (121|159) [SCAL] (1) conductionElement.Q_flow = conductionElement.k * (conductionElement.T_heatPort - conductionElement.T); ($RES_SIM_69) (122|160) [SCAL] (1) flowResistance1.m_flow - conductionElement.m_flow = 0.0; ($RES_SIM_109) (123|161) [SCAL] (1) pump.v_in = 1.0 / max(pump.rho_min, $FUN_32); ($RES_BND_161) (124|162) [SCAL] (1) conductionElement.M * $DER.conductionElement.h_out = conductionElement.Q_flow + conductionElement.m_flow * (conductionElement.h_in_norm - conductionElement.h_out); ($RES_SIM_71) (125|163) [SCAL] (1) pump.eta = if noEvent($FUN_33 > 1e-4) then pump.v_in * pump.dp * flowResistance1.m_flow / pump.W_t else 0.0; ($RES_BND_162) (126|164) [SCAL] (1) conductionElement.M = conductionElement.V * conductionElement.rho; ($RES_SIM_72) (127|165) [SCAL] (1) pump.v_out = 1.0 / max(pump.rho_min, $FUN_32); ($RES_BND_163) (128|166) [ARRY] (2) multiSensor_Tpm2.outlet.state.X = reservoir.inlet.state.X; ($RES_SIM_112) (129|168) [SCAL] (1) multiSensor_Tpm2.outlet.state.T = reservoir.inlet.state.T; ($RES_SIM_113) (130|169) [SCAL] (1) multiSensor_Tpm2.outlet.state.p = reservoir.inlet.state.p; ($RES_SIM_114) (131|170) [SCAL] (1) conductionElement.k = conductionElement.A * conductionElement.U; ($RES_SIM_75) (132|171) [RECD] (4) pump.outlet.state = $FUN_5; ($RES_SIM_77) (133|175) [SCAL] (1) pump.dr_corr = (pump.p_in + pump.dp) - pump.p_out; ($RES_SIM_78) (134|176) [SCAL] (1) pump.p_out = max(pump.p_min, pump.p_in + pump.dp); ($RES_SIM_79) (135|177) [SCAL] (1) $DER.reservoir.m_flow_out + $DER.conductionElement.m_flow = 0.0; ($RES_SIM_257) (136|178) [SCAL] (1) $DER.flowResistance1.m_flow - $DER.conductionElement.m_flow = 0.0; ($RES_SIM_258) =================== Scalar Matching =================== variable to equation ********************** var 1 --> eqn 64 var 2 --> eqn 66 var 3 --> eqn 70 var 4 --> eqn 91 var 5 --> eqn 71 var 6 --> eqn 72 var 7 --> eqn 18 var 8 --> eqn 163 var 9 --> eqn 116 var 10 --> eqn 141 var 11 --> eqn -1 var 12 --> eqn 164 var 13 --> eqn 48 var 14 --> eqn 13 var 15 --> eqn 63 var 16 --> eqn 118 var 17 --> eqn 178 var 18 --> eqn 151 var 19 --> eqn 99 var 20 --> eqn 87 var 21 --> eqn 88 var 22 --> eqn 92 var 23 --> eqn 65 var 24 --> eqn 89 var 25 --> eqn 35 var 26 --> eqn 36 var 27 --> eqn 14 var 28 --> eqn 125 var 29 --> eqn 58 var 30 --> eqn 59 var 31 --> eqn 152 var 32 --> eqn 52 var 33 --> eqn 171 var 34 --> eqn 74 var 35 --> eqn 34 var 36 --> eqn 165 var 37 --> eqn 73 var 38 --> eqn 55 var 39 --> eqn 140 var 40 --> eqn 134 var 41 --> eqn 33 var 42 --> eqn 84 var 43 --> eqn 166 var 44 --> eqn 167 var 45 --> eqn 122 var 46 --> eqn 82 var 47 --> eqn 50 var 48 --> eqn 51 var 49 --> eqn 128 var 50 --> eqn 129 var 51 --> eqn 177 var 52 --> eqn 42 var 53 --> eqn 85 var 54 --> eqn 156 var 55 --> eqn 93 var 56 --> eqn 41 var 57 --> eqn 61 var 58 --> eqn 57 var 59 --> eqn 98 var 60 --> eqn 161 var 61 --> eqn 100 var 62 --> eqn 145 var 63 --> eqn 175 var 64 --> eqn 103 var 65 --> eqn 104 var 66 --> eqn 105 var 67 --> eqn -1 var 68 --> eqn 169 var 69 --> eqn 86 var 70 --> eqn 170 var 71 --> eqn 23 var 72 --> eqn 45 var 73 --> eqn 39 var 74 --> eqn 121 var 75 --> eqn 60 var 76 --> eqn 67 var 77 --> eqn 68 var 78 --> eqn 56 var 79 --> eqn 80 var 80 --> eqn 138 var 81 --> eqn 139 var 82 --> eqn 22 var 83 --> eqn 162 var 84 --> eqn 106 var 85 --> eqn 107 var 86 --> eqn 108 var 87 --> eqn 120 var 88 --> eqn 1 var 89 --> eqn 15 var 90 --> eqn 49 var 91 --> eqn 19 var 92 --> eqn 90 var 93 --> eqn 76 var 94 --> eqn 135 var 95 --> eqn 69 var 96 --> eqn 124 var 97 --> eqn 27 var 98 --> eqn 114 var 99 --> eqn 16 var 100 --> eqn 137 var 101 --> eqn 173 var 102 --> eqn 174 var 103 --> eqn 47 var 104 --> eqn 154 var 105 --> eqn 136 var 106 --> eqn -1 var 107 --> eqn 155 var 108 --> eqn 12 var 109 --> eqn 157 var 110 --> eqn 43 var 111 --> eqn 44 var 112 --> eqn 176 var 113 --> eqn 2 var 114 --> eqn 119 var 115 --> eqn 101 var 116 --> eqn 62 var 117 --> eqn 117 var 118 --> eqn 94 var 119 --> eqn 102 var 120 --> eqn 26 var 121 --> eqn 150 var 122 --> eqn 132 var 123 --> eqn 7 var 124 --> eqn 30 var 125 --> eqn 53 var 126 --> eqn 83 var 127 --> eqn 148 var 128 --> eqn 79 var 129 --> eqn 110 var 130 --> eqn 142 var 131 --> eqn 147 var 132 --> eqn 159 var 133 --> eqn 5 var 134 --> eqn 40 var 135 --> eqn 24 var 136 --> eqn 149 var 137 --> eqn 25 var 138 --> eqn 146 var 139 --> eqn 130 var 140 --> eqn 8 var 141 --> eqn 31 var 142 --> eqn 32 var 143 --> eqn 115 var 144 --> eqn 46 var 145 --> eqn 172 var 146 --> eqn 131 var 147 --> eqn 3 var 148 --> eqn 4 var 149 --> eqn 11 var 150 --> eqn 10 var 151 --> eqn 153 var 152 --> eqn 123 var 153 --> eqn 20 var 154 --> eqn 112 var 155 --> eqn 113 var 156 --> eqn 96 var 157 --> eqn 97 var 158 --> eqn 81 var 159 --> eqn 9 var 160 --> eqn 6 var 161 --> eqn 143 var 162 --> eqn 21 var 163 --> eqn 54 var 164 --> eqn -1 var 165 --> eqn 168 var 166 --> eqn 109 var 167 --> eqn 144 var 168 --> eqn 95 var 169 --> eqn 133 var 170 --> eqn 28 var 171 --> eqn 29 var 172 --> eqn 77 var 173 --> eqn 78 var 174 --> eqn 17 var 175 --> eqn 127 var 176 --> eqn 75 var 177 --> eqn 37 var 178 --> eqn 111 var 179 --> eqn 38 var 180 --> eqn 126 var 181 --> eqn 160 var 182 --> eqn 158 equation to variable ********************** eqn 1 --> var 88 eqn 2 --> var 113 eqn 3 --> var 147 eqn 4 --> var 148 eqn 5 --> var 133 eqn 6 --> var 160 eqn 7 --> var 123 eqn 8 --> var 140 eqn 9 --> var 159 eqn 10 --> var 150 eqn 11 --> var 149 eqn 12 --> var 108 eqn 13 --> var 14 eqn 14 --> var 27 eqn 15 --> var 89 eqn 16 --> var 99 eqn 17 --> var 174 eqn 18 --> var 7 eqn 19 --> var 91 eqn 20 --> var 153 eqn 21 --> var 162 eqn 22 --> var 82 eqn 23 --> var 71 eqn 24 --> var 135 eqn 25 --> var 137 eqn 26 --> var 120 eqn 27 --> var 97 eqn 28 --> var 170 eqn 29 --> var 171 eqn 30 --> var 124 eqn 31 --> var 141 eqn 32 --> var 142 eqn 33 --> var 41 eqn 34 --> var 35 eqn 35 --> var 25 eqn 36 --> var 26 eqn 37 --> var 177 eqn 38 --> var 179 eqn 39 --> var 73 eqn 40 --> var 134 eqn 41 --> var 56 eqn 42 --> var 52 eqn 43 --> var 110 eqn 44 --> var 111 eqn 45 --> var 72 eqn 46 --> var 144 eqn 47 --> var 103 eqn 48 --> var 13 eqn 49 --> var 90 eqn 50 --> var 47 eqn 51 --> var 48 eqn 52 --> var 32 eqn 53 --> var 125 eqn 54 --> var 163 eqn 55 --> var 38 eqn 56 --> var 78 eqn 57 --> var 58 eqn 58 --> var 29 eqn 59 --> var 30 eqn 60 --> var 75 eqn 61 --> var 57 eqn 62 --> var 116 eqn 63 --> var 15 eqn 64 --> var 1 eqn 65 --> var 23 eqn 66 --> var 2 eqn 67 --> var 76 eqn 68 --> var 77 eqn 69 --> var 95 eqn 70 --> var 3 eqn 71 --> var 5 eqn 72 --> var 6 eqn 73 --> var 37 eqn 74 --> var 34 eqn 75 --> var 176 eqn 76 --> var 93 eqn 77 --> var 172 eqn 78 --> var 173 eqn 79 --> var 128 eqn 80 --> var 79 eqn 81 --> var 158 eqn 82 --> var 46 eqn 83 --> var 126 eqn 84 --> var 42 eqn 85 --> var 53 eqn 86 --> var 69 eqn 87 --> var 20 eqn 88 --> var 21 eqn 89 --> var 24 eqn 90 --> var 92 eqn 91 --> var 4 eqn 92 --> var 22 eqn 93 --> var 55 eqn 94 --> var 118 eqn 95 --> var 168 eqn 96 --> var 156 eqn 97 --> var 157 eqn 98 --> var 59 eqn 99 --> var 19 eqn 100 --> var 61 eqn 101 --> var 115 eqn 102 --> var 119 eqn 103 --> var 64 eqn 104 --> var 65 eqn 105 --> var 66 eqn 106 --> var 84 eqn 107 --> var 85 eqn 108 --> var 86 eqn 109 --> var 166 eqn 110 --> var 129 eqn 111 --> var 178 eqn 112 --> var 154 eqn 113 --> var 155 eqn 114 --> var 98 eqn 115 --> var 143 eqn 116 --> var 9 eqn 117 --> var 117 eqn 118 --> var 16 eqn 119 --> var 114 eqn 120 --> var 87 eqn 121 --> var 74 eqn 122 --> var 45 eqn 123 --> var 152 eqn 124 --> var 96 eqn 125 --> var 28 eqn 126 --> var 180 eqn 127 --> var 175 eqn 128 --> var 49 eqn 129 --> var 50 eqn 130 --> var 139 eqn 131 --> var 146 eqn 132 --> var 122 eqn 133 --> var 169 eqn 134 --> var 40 eqn 135 --> var 94 eqn 136 --> var 105 eqn 137 --> var 100 eqn 138 --> var 80 eqn 139 --> var 81 eqn 140 --> var 39 eqn 141 --> var 10 eqn 142 --> var 130 eqn 143 --> var 161 eqn 144 --> var 167 eqn 145 --> var 62 eqn 146 --> var 138 eqn 147 --> var 131 eqn 148 --> var 127 eqn 149 --> var 136 eqn 150 --> var 121 eqn 151 --> var 18 eqn 152 --> var 31 eqn 153 --> var 151 eqn 154 --> var 104 eqn 155 --> var 107 eqn 156 --> var 54 eqn 157 --> var 109 eqn 158 --> var 182 eqn 159 --> var 132 eqn 160 --> var 181 eqn 161 --> var 60 eqn 162 --> var 83 eqn 163 --> var 8 eqn 164 --> var 12 eqn 165 --> var 36 eqn 166 --> var 43 eqn 167 --> var 44 eqn 168 --> var 165 eqn 169 --> var 68 eqn 170 --> var 70 eqn 171 --> var 33 eqn 172 --> var 145 eqn 173 --> var 101 eqn 174 --> var 102 eqn 175 --> var 63 eqn 176 --> var 112 eqn 177 --> var 51 eqn 178 --> var 17 " [Timeout remaining time 659] [Calling sys.exit(0), Time elapsed: 3.8995801471173763] Failed to read output from testmodel.py, exit status != 0: 0.8417211882770061 0.668668784 0.06092796899999994 Calling exit ...