Running: ./testmodel.py --libraries=/home/hudson/saved_omc/libraries/.openmodelica/libraries --ompython_omhome=/usr ThermofluidStream_dev_ThermofluidStream.Idealized.Tests.Processes.Isochoric.Fixed2.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 0.0007531/0.0007531, allocations: 80.25 kB / 20.06 MB, free: 4.469 MB / 18.57 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 0.0007366/0.0007366, allocations: 173.9 kB / 23.36 MB, free: 1.164 MB / 18.57 MB " [Timeout remaining time 180] loadFile("/home/hudson/saved_omc/libraries/.openmodelica/libraries/Modelica 4.1.0+maint.om/package.mo", uses=false) [Timeout 180] "Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/Modelica 4.1.0+maint.om/package.mo): time 0.8704/0.8704, allocations: 177.2 MB / 203.7 MB, free: 5.691 MB / 186.7 MB " [Timeout remaining time 179] loadFile("/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermofluidStream main/package.mo", uses=false) [Timeout 180] "Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermofluidStream main/package.mo): time 0.5958/0.5958, allocations: 116.1 MB / 376.2 MB, free: 4.145 MB / 346.7 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.Idealized.Tests.Processes.Isochoric.Fixed2,tolerance=1e-06,outputFormat="mat",numberOfIntervals=100,variableFilter="CPUtime|EventCounter|Q_flow|T_in|T_out|T_out2.L|T_out2.P|T_out2.P_out|T_out2.Q_flow|T_out2.Q_flow_in|T_out2.T_out_fixed|T_out2.assertionLevel|T_out2.clip_p_out|T_out2.dT|T_out2.dT_fixed|T_out2.dp|T_out2.dp_start|T_out2.dr_corr|T_out2.du|T_out2.h_in|T_out2.h_out|T_out2.initM_flow|der.T_out2.inlet.m_flow.|T_out2.inlet.m_flow|T_out2.inlet.r|T_out2.inlet.state.T|T_out2.inlet.state.p|T_out2.m_acceleration_0|T_out2.m_flow|T_out2.m_flowStateSelect|T_out2.m_flow_0|T_out2.outlet.m_flow|T_out2.outlet.r|T_out2.outlet.state.T|T_out2.outlet.state.p|T_out2.outletSpec|T_out2.outletSpec_actual|T_out2.outletValueSpec|T_out2.p_in|T_out2.p_min|T_out2.p_out|T_out2.rho|T_out2.singularityRegime|T_out2.systemSpec|T_out2.u_in|T_out2.u_out|T_out2.w_p|T_out2c.L|T_out2c.P|T_out2c.Q_flow|T_out2c.Q_flow_in|T_out2c.T_out_fixed|T_out2c.assertionLevel|T_out2c.clip_p_out|T_out2c.dT|T_out2c.dT_fixed|T_out2c.dp|T_out2c.dp_start|T_out2c.dr_corr|T_out2c.du|T_out2c.h_in|T_out2c.h_out|T_out2c.initM_flow|der.T_out2c.inlet.m_flow.|T_out2c.inlet.m_flow|T_out2c.inlet.r|T_out2c.inlet.state.T|T_out2c.inlet.state.p|T_out2c.m_acceleration_0|T_out2c.m_flow|T_out2c.m_flowStateSelect|T_out2c.m_flow_0|T_out2c.outlet.m_flow|T_out2c.outlet.r|T_out2c.outlet.state.T|T_out2c.outlet.state.p|T_out2c.outletSpec|T_out2c.outletSpec_actual|T_out2c.outletValueSpec|T_out2c.p_in|T_out2c.p_min|T_out2c.p_out|T_out2c.rho|T_out2c.singularityRegime|T_out2c.systemSpec|T_out2c.u_in|T_out2c.u_out|T_out2c.w_p|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.|_derdummy|_dummy|cv|dT|dT2.L|dT2.P|dT2.P_out|dT2.Q_flow|dT2.Q_flow_in|dT2.T_out_fixed|dT2.assertionLevel|dT2.clip_p_out|dT2.dT|dT2.dT_fixed|dT2.dp|dT2.dp_start|dT2.dr_corr|dT2.du|dT2.h_in|dT2.h_out|dT2.initM_flow|der.dT2.inlet.m_flow.|dT2.inlet.m_flow|dT2.inlet.r|dT2.inlet.state.T|dT2.inlet.state.p|dT2.m_acceleration_0|dT2.m_flow|dT2.m_flowStateSelect|dT2.m_flow_0|dT2.outlet.m_flow|dT2.outlet.r|dT2.outlet.state.T|dT2.outlet.state.p|dT2.outletSpec|dT2.outletSpec_actual|dT2.outletValueSpec|dT2.p_in|dT2.p_min|dT2.p_out|dT2.rho|dT2.singularityRegime|dT2.systemSpec|dT2.u_in|dT2.u_out|dT2.w_p|dT2c.L|dT2c.P|dT2c.Q_flow|dT2c.Q_flow_in|dT2c.T_out_fixed|dT2c.assertionLevel|dT2c.clip_p_out|dT2c.dT|dT2c.dT_fixed|dT2c.dp|dT2c.dp_start|dT2c.dr_corr|dT2c.du|dT2c.h_in|dT2c.h_out|dT2c.initM_flow|der.dT2c.inlet.m_flow.|dT2c.inlet.m_flow|dT2c.inlet.r|dT2c.inlet.state.T|dT2c.inlet.state.p|dT2c.m_acceleration_0|dT2c.m_flow|dT2c.m_flowStateSelect|dT2c.m_flow_0|dT2c.outlet.m_flow|dT2c.outlet.r|dT2c.outlet.state.T|dT2c.outlet.state.p|dT2c.outletSpec|dT2c.outletSpec_actual|dT2c.outletValueSpec|dT2c.p_in|dT2c.p_min|dT2c.p_out|dT2c.rho|dT2c.singularityRegime|dT2c.systemSpec|dT2c.u_in|dT2c.u_out|dT2c.w_p|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|energyFlowSource.E_flow|energyFlowSource.E_flow_out|m_flow|p_in|sink.L|der.sink.inlet.m_flow.|sink.inlet.m_flow|sink.inlet.r|sink.inlet.state.T|sink.inlet.state.p|sink1.L|der.sink1.inlet.m_flow.|sink1.inlet.m_flow|sink1.inlet.r|sink1.inlet.state.T|sink1.inlet.state.p|sink2.L|der.sink2.inlet.m_flow.|sink2.inlet.m_flow|sink2.inlet.r|sink2.inlet.state.T|sink2.inlet.state.p|sink3.L|der.sink3.inlet.m_flow.|sink3.inlet.m_flow|sink3.inlet.r|sink3.inlet.state.T|sink3.inlet.state.p|source.L|source.T0|source.T0_par|source.h0|source.h0_par|der.source.outlet.m_flow.|source.outlet.m_flow|source.outlet.r|source.outlet.state.T|source.outlet.state.p|source.p0|source.p0_par|source1.L|source1.T0|source1.T0_par|source1.h0|source1.h0_par|der.source1.outlet.m_flow.|source1.outlet.m_flow|source1.outlet.r|source1.outlet.state.T|source1.outlet.state.p|source1.p0|source1.p0_par|source2.L|source2.T0|source2.T0_par|source2.h0|source2.h0_par|der.source2.outlet.m_flow.|source2.outlet.m_flow|source2.outlet.r|source2.outlet.state.T|source2.outlet.state.p|source2.p0|source2.p0_par|source3.L|source3.T0|source3.T0_par|source3.h0|source3.h0_par|der.source3.outlet.m_flow.|source3.outlet.m_flow|source3.outlet.r|source3.outlet.state.T|source3.outlet.state.p|source3.p0|source3.p0_par",fileNamePrefix="ThermofluidStream_dev_ThermofluidStream.Idealized.Tests.Processes.Isochoric.Fixed2") translateModel(ThermofluidStream.Idealized.Tests.Processes.Isochoric.Fixed2,tolerance=1e-06,outputFormat="mat",numberOfIntervals=100,variableFilter="CPUtime|EventCounter|Q_flow|T_in|T_out|T_out2.L|T_out2.P|T_out2.P_out|T_out2.Q_flow|T_out2.Q_flow_in|T_out2.T_out_fixed|T_out2.assertionLevel|T_out2.clip_p_out|T_out2.dT|T_out2.dT_fixed|T_out2.dp|T_out2.dp_start|T_out2.dr_corr|T_out2.du|T_out2.h_in|T_out2.h_out|T_out2.initM_flow|der.T_out2.inlet.m_flow.|T_out2.inlet.m_flow|T_out2.inlet.r|T_out2.inlet.state.T|T_out2.inlet.state.p|T_out2.m_acceleration_0|T_out2.m_flow|T_out2.m_flowStateSelect|T_out2.m_flow_0|T_out2.outlet.m_flow|T_out2.outlet.r|T_out2.outlet.state.T|T_out2.outlet.state.p|T_out2.outletSpec|T_out2.outletSpec_actual|T_out2.outletValueSpec|T_out2.p_in|T_out2.p_min|T_out2.p_out|T_out2.rho|T_out2.singularityRegime|T_out2.systemSpec|T_out2.u_in|T_out2.u_out|T_out2.w_p|T_out2c.L|T_out2c.P|T_out2c.Q_flow|T_out2c.Q_flow_in|T_out2c.T_out_fixed|T_out2c.assertionLevel|T_out2c.clip_p_out|T_out2c.dT|T_out2c.dT_fixed|T_out2c.dp|T_out2c.dp_start|T_out2c.dr_corr|T_out2c.du|T_out2c.h_in|T_out2c.h_out|T_out2c.initM_flow|der.T_out2c.inlet.m_flow.|T_out2c.inlet.m_flow|T_out2c.inlet.r|T_out2c.inlet.state.T|T_out2c.inlet.state.p|T_out2c.m_acceleration_0|T_out2c.m_flow|T_out2c.m_flowStateSelect|T_out2c.m_flow_0|T_out2c.outlet.m_flow|T_out2c.outlet.r|T_out2c.outlet.state.T|T_out2c.outlet.state.p|T_out2c.outletSpec|T_out2c.outletSpec_actual|T_out2c.outletValueSpec|T_out2c.p_in|T_out2c.p_min|T_out2c.p_out|T_out2c.rho|T_out2c.singularityRegime|T_out2c.systemSpec|T_out2c.u_in|T_out2c.u_out|T_out2c.w_p|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.|_derdummy|_dummy|cv|dT|dT2.L|dT2.P|dT2.P_out|dT2.Q_flow|dT2.Q_flow_in|dT2.T_out_fixed|dT2.assertionLevel|dT2.clip_p_out|dT2.dT|dT2.dT_fixed|dT2.dp|dT2.dp_start|dT2.dr_corr|dT2.du|dT2.h_in|dT2.h_out|dT2.initM_flow|der.dT2.inlet.m_flow.|dT2.inlet.m_flow|dT2.inlet.r|dT2.inlet.state.T|dT2.inlet.state.p|dT2.m_acceleration_0|dT2.m_flow|dT2.m_flowStateSelect|dT2.m_flow_0|dT2.outlet.m_flow|dT2.outlet.r|dT2.outlet.state.T|dT2.outlet.state.p|dT2.outletSpec|dT2.outletSpec_actual|dT2.outletValueSpec|dT2.p_in|dT2.p_min|dT2.p_out|dT2.rho|dT2.singularityRegime|dT2.systemSpec|dT2.u_in|dT2.u_out|dT2.w_p|dT2c.L|dT2c.P|dT2c.Q_flow|dT2c.Q_flow_in|dT2c.T_out_fixed|dT2c.assertionLevel|dT2c.clip_p_out|dT2c.dT|dT2c.dT_fixed|dT2c.dp|dT2c.dp_start|dT2c.dr_corr|dT2c.du|dT2c.h_in|dT2c.h_out|dT2c.initM_flow|der.dT2c.inlet.m_flow.|dT2c.inlet.m_flow|dT2c.inlet.r|dT2c.inlet.state.T|dT2c.inlet.state.p|dT2c.m_acceleration_0|dT2c.m_flow|dT2c.m_flowStateSelect|dT2c.m_flow_0|dT2c.outlet.m_flow|dT2c.outlet.r|dT2c.outlet.state.T|dT2c.outlet.state.p|dT2c.outletSpec|dT2c.outletSpec_actual|dT2c.outletValueSpec|dT2c.p_in|dT2c.p_min|dT2c.p_out|dT2c.rho|dT2c.singularityRegime|dT2c.systemSpec|dT2c.u_in|dT2c.u_out|dT2c.w_p|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|energyFlowSource.E_flow|energyFlowSource.E_flow_out|m_flow|p_in|sink.L|der.sink.inlet.m_flow.|sink.inlet.m_flow|sink.inlet.r|sink.inlet.state.T|sink.inlet.state.p|sink1.L|der.sink1.inlet.m_flow.|sink1.inlet.m_flow|sink1.inlet.r|sink1.inlet.state.T|sink1.inlet.state.p|sink2.L|der.sink2.inlet.m_flow.|sink2.inlet.m_flow|sink2.inlet.r|sink2.inlet.state.T|sink2.inlet.state.p|sink3.L|der.sink3.inlet.m_flow.|sink3.inlet.m_flow|sink3.inlet.r|sink3.inlet.state.T|sink3.inlet.state.p|source.L|source.T0|source.T0_par|source.h0|source.h0_par|der.source.outlet.m_flow.|source.outlet.m_flow|source.outlet.r|source.outlet.state.T|source.outlet.state.p|source.p0|source.p0_par|source1.L|source1.T0|source1.T0_par|source1.h0|source1.h0_par|der.source1.outlet.m_flow.|source1.outlet.m_flow|source1.outlet.r|source1.outlet.state.T|source1.outlet.state.p|source1.p0|source1.p0_par|source2.L|source2.T0|source2.T0_par|source2.h0|source2.h0_par|der.source2.outlet.m_flow.|source2.outlet.m_flow|source2.outlet.r|source2.outlet.state.T|source2.outlet.state.p|source2.p0|source2.p0_par|source3.L|source3.T0|source3.T0_par|source3.h0|source3.h0_par|der.source3.outlet.m_flow.|source3.outlet.m_flow|source3.outlet.r|source3.outlet.state.T|source3.outlet.state.p|source3.p0|source3.p0_par",fileNamePrefix="ThermofluidStream_dev_ThermofluidStream.Idealized.Tests.Processes.Isochoric.Fixed2") [Timeout 660] "Notification: Performance of FrontEnd - Absyn->SCode: time 2.369e-05/2.369e-05, allocations: 2.312 kB / 0.5548 GB, free: 12.65 MB / 490.7 MB Notification: Performance of NFInst.instantiate(ThermofluidStream.Idealized.Tests.Processes.Isochoric.Fixed2): time 0.4193/0.4194, allocations: 179.5 MB / 0.7301 GB, free: 80 kB / 0.573 GB Notification: Performance of NFInst.instExpressions: time 0.0047/0.4241, allocations: 3.194 MB / 0.7332 GB, free: 13.49 MB / 0.5886 GB Notification: Performance of NFInst.updateImplicitVariability: time 0.001292/0.4254, allocations: 79.78 kB / 0.7333 GB, free: 13.44 MB / 0.5886 GB Notification: Performance of NFTyping.typeComponents: time 0.001148/0.4265, allocations: 458.6 kB / 0.7337 GB, free: 13.06 MB / 0.5886 GB Notification: Performance of NFTyping.typeBindings: time 0.003225/0.4297, allocations: 1.286 MB / 0.7349 GB, free: 12.01 MB / 0.5886 GB Notification: Performance of NFTyping.typeClassSections: time 0.003038/0.4328, allocations: 1.416 MB / 0.7363 GB, free: 10.97 MB / 0.5886 GB Notification: Performance of NFFlatten.flatten: time 0.002333/0.4351, allocations: 2.183 MB / 0.7385 GB, free: 9.617 MB / 0.5886 GB Notification: Performance of NFFlatten.resolveConnections: time 0.0004334/0.4355, allocations: 152 kB / 0.7386 GB, free: 9.516 MB / 0.5886 GB Notification: Performance of NFEvalConstants.evaluate: time 0.00349/0.439, allocations: 1.708 MB / 0.7403 GB, free: 8.438 MB / 0.5886 GB Notification: Performance of NFSimplifyModel.simplify: time 0.0006951/0.4397, allocations: 399.7 kB / 0.7407 GB, free: 8.238 MB / 0.5886 GB Notification: Performance of NFPackage.collectConstants: time 0.0001255/0.4398, allocations: 62.25 kB / 0.7407 GB, free: 8.234 MB / 0.5886 GB Notification: Performance of NFFlatten.collectFunctions: time 0.003122/0.443, allocations: 1.143 MB / 0.7418 GB, free: 7.711 MB / 0.5886 GB Notification: Performance of combineBinaries: time 0.001266/0.4442, allocations: 1.846 MB / 0.7436 GB, free: 6.473 MB / 0.5886 GB Notification: Performance of replaceArrayConstructors: time 0.001008/0.4452, allocations: 1.281 MB / 0.7449 GB, free: 5.645 MB / 0.5886 GB Notification: Performance of NFVerifyModel.verify: time 0.000246/0.4455, allocations: 98.75 kB / 0.745 GB, free: 5.645 MB / 0.5886 GB Notification: Performance of FrontEnd: time 0.0005554/0.446, allocations: 242.5 kB / 0.7452 GB, free: 5.5 MB / 0.5886 GB Notification: Model statistics after passing the front-end and creating the data structures used by the back-end: * Number of equations: 163 (155) * Number of variables: 163 (163) Notification: Performance of [SIM] Bindings: time 0.004042/0.4501, allocations: 4.42 MB / 0.7495 GB, free: 2.445 MB / 0.5886 GB Notification: Performance of [SIM] FunctionAlias: time 0.001012/0.4511, allocations: 0.8405 MB / 0.7503 GB, free: 1.812 MB / 0.5886 GB Notification: Performance of [SIM] Early Inline: time 0.002327/0.4534, allocations: 2.858 MB / 0.7531 GB, free: 15.66 MB / 0.6042 GB Notification: Performance of [SIM] Simplify 1: time 0.0003395/0.4538, allocations: 297.2 kB / 0.7534 GB, free: 15.45 MB / 0.6042 GB Notification: Performance of [SIM] Alias: time 0.00365/0.4574, allocations: 3.716 MB / 0.7571 GB, free: 12.52 MB / 0.6042 GB Notification: Performance of [SIM] Simplify 2: time 0.0002352/0.4576, allocations: 226.6 kB / 0.7573 GB, free: 12.35 MB / 0.6042 GB Notification: Performance of [SIM] Remove Stream: time 0.0001557/0.4578, allocations: 216.6 kB / 0.7575 GB, free: 12.16 MB / 0.6042 GB Notification: Performance of [SIM] Detect States: time 0.0006741/0.4585, allocations: 0.7141 MB / 0.7582 GB, free: 11.54 MB / 0.6042 GB Notification: Performance of [SIM] Events: time 6.639e-05/0.4585, allocations: 67.64 kB / 0.7582 GB, free: 11.49 MB / 0.6042 GB Notification: Performance of [SIM] Partitioning: time 0.0008291/0.4594, allocations: 0.9639 MB / 0.7592 GB, free: 10.89 MB / 0.6042 GB Error: Internal error NBSorting.tarjan failed to sort system: System Variables (54/56) ************************** (1|1) [ALGB] (1) Real source.outlet.r (2|2) [DSTA] (1) input Real dT2c.inlet.state.p (start = 1e6, min = 0.0, max = 1e8, nominal = 1e6) (3|3) [ALGB] (1) Real dT2c.w_p = (dT2c.p_out - dT2c.p_in) / dT2c.rho (4|4) [DSTA] (1) Real $FUN_2.p (5|5) [DSTA] (1) Real $FUN_1.p (6|6) [DSTA] (1) Real dT2c.T_out (start = 500.0, min = 200.0, max = 6000.0, nominal = 500.0) (7|7) [ALGB] (1) Real sink.r (8|8) [DSTA] (1) output Real source.outlet.state.T (start = 500.0, min = 200.0, max = 6000.0, nominal = 500.0) (9|9) [DSTA] (1) Real dT2c.T_in = ThermofluidStream.Idealized.Tests.Processes.Isochoric.Fixed2.dT2c.Medium.temperature(dT2c.inlet.state) (start = 500.0, min = 200.0, max = 6000.0, nominal = 500.0) (10|10) [DSTA] (1) Real dT2c.rho = ThermofluidStream.Idealized.Tests.Processes.Isochoric.Fixed2.dT2c.Medium.density(dT2c.inlet.state) (start = 10.0, min = 0.0, max = 1e5, nominal = 10.0) (11|11) [ALGB] (1) Real dT2c.dp (start = dT2c.dp_start) (12|12) [ALGB] (1) output Real dT2c.outlet.state.T (start = 500.0, min = 200.0, max = 6000.0, nominal = 500.0) (13|13) [DDER] (1) Real $DER.dT2c.m_flow (StateSelect = avoid) (14|14) [DSTA] (1) input Real dT2c.inlet.state.T (start = 500.0, min = 200.0, max = 6000.0, nominal = 500.0) (15|15) [ALGB] (1) Real $FUN_7.T (16|16) [DSTA] (1) Real $FUN_2.T (17|17) [DSTA] (1) Real $FUN_1.T (18|18) [DSTA] (1) Real dT2c.p_out (start = 1e6, min = 0.0, max = 1e8, nominal = 1e6) (19|19) [ALGB] (1) input Real sink.inlet.state.p (start = 1e6, min = 0.0, max = 1e8, nominal = 1e6) (20|20) [DSTA] (1) output Real source.outlet.state.p (start = 1e6, min = 0.0, max = 1e8, nominal = 1e6) (21|21) [ALGB] (1) output Real dT2c.outlet.state.p (start = 1e6, min = 0.0, max = 1e8, nominal = 1e6) (22|22) [DSTA] (1) Real dT2c.du = dT2c.u_out - dT2c.u_in (min = -1e8, max = 1e8, nominal = 1e6) (23|23) [DSTA] (1) Real dT2c.u_in = dT2c.h_in - dT2c.p_in / dT2c.rho (min = -1e8, max = 1e8, nominal = 1e6) (24|24) [DSTA] (1) Real dT2c.u_out = dT2c.h_out - dT2c.p_out / dT2c.rho (min = -1e8, max = 1e8, nominal = 1e6) (25|25) [DSTA] (1) Real dT2c.h_in = ThermofluidStream.Idealized.Tests.Processes.Isochoric.Fixed2.dT2c.Medium.specificEnthalpy(dT2c.inlet.state) (start = 298609.6803431054, min = -1e10, max = 1e10, nominal = 1e5) (26|26) [DSTA] (1) Real dT2c.p_in = ThermofluidStream.Idealized.Tests.Processes.Isochoric.Fixed2.dT2c.Medium.pressure(dT2c.inlet.state) (start = 1e6, min = 0.0, max = 1e8, nominal = 1e6) (27|27) [ALGB] (1) Real dT2c.outlet.r (28|28) [ALGB] (1) input Real sink.inlet.state.T (start = 500.0, min = 200.0, max = 6000.0, nominal = 500.0) (29|29) [DSTA] (1) Real dT2c.h_out (start = 298609.6803431054, min = -1e10, max = 1e10, nominal = 1e5) (30|30) [ALGB] (1) Real dT2c.singularityRegime (31|31) [ALGB] (1) Real $FUN_6 (32|32) [ALGB] (1) Real $FUN_5 (33|33) [ALGB] (1) Real $FUN_7.p (34|34) [DDER] (1) Real $DER.$FUN_1.p (StateSelect = avoid) (35|35) [DDER] (1) Real $DER.$FUN_1.T (StateSelect = avoid) (36|36) [DDER] (1) Real $DER.$FUN_2.p (StateSelect = avoid) (37|37) [DDER] (1) Real $DER.dT2c.T_in (StateSelect = avoid) (38|38) [DDER] (1) Real $DER.dT2c.T_out (StateSelect = avoid) (39|39) [DDER] (1) Real $DER.dT2c.du (StateSelect = avoid) (40|40) [DER-] (2) source.Medium.ThermodynamicState $DER.$FUN_1 (41|42) [DER-] (2) source.outlet.Medium.ThermodynamicState $DER.source.outlet.state (42|44) [DDER] (1) Real $DER.dT2c.h_in (StateSelect = avoid) (43|45) [DDER] (1) Real $DER.dT2c.u_in (StateSelect = avoid) (44|46) [DDER] (1) Real $DER.dT2c.p_in (StateSelect = avoid) (45|47) [DDER] (1) Real $DER.dT2c.rho (StateSelect = avoid) (46|48) [DDER] (1) Real $DER.dT2c.p_out (StateSelect = avoid) (47|49) [DDER] (1) Real $DER.dT2c.u_out (StateSelect = avoid) (48|50) [DDER] (1) Real $DER.$FUN_2.T (StateSelect = avoid) (49|51) [DDER] (1) Real $DER.dT2c.h_out (StateSelect = avoid) (50|52) [DDER] (1) input Real $DER.dT2c.inlet.state.T (StateSelect = avoid) (51|53) [DDER] (1) output Real $DER.source.outlet.state.T (StateSelect = avoid) (52|54) [DDER] (1) input Real $DER.dT2c.inlet.state.p (StateSelect = avoid) (53|55) [DDER] (1) output Real $DER.source.outlet.state.p (StateSelect = avoid) (54|56) [DSTA] (1) Real dT2c.m_flow = dT2c.m_flow (StateSelect = default) System Equations (49/52) ************************** (1|1) [SCAL] (1) dT2c.h_in = ThermofluidStream.Media.myMedia.IdealGases.Common.Functions.h_T(ThermofluidStream.Media.myMedia.IdealGases.Common.DataRecord(\"Air\", 0.0289651159, -4333.833858403446, 298609.6803431054, 1000.0, {10099.5016, -196.827561, 5.00915511, -0.00576101373, 1.06685993e-5, -7.94029797e-9, 2.18523191e-12}, {-176.796731, -3.921504225}, {241521.443, -1257.8746, 5.14455867, -2.13854179e-4, 7.06522784e-8, -1.07148349e-11, 6.57780015e-16}, {6462.26319, -8.147411905}, 287.0512249529787), dT2c.inlet.state.T, true, ThermofluidStream.Media.myMedia.Interfaces.Choices.ReferenceEnthalpy.ZeroAt0K, 0.0) ($RES_AUX_160) (2|2) [SCAL] (1) dT2c.T_in = dT2c.inlet.state.T ($RES_AUX_161) (3|3) [SCAL] (1) dT2c.rho = (0.0034836987724536205 * dT2c.inlet.state.p) / dT2c.inlet.state.T ($RES_AUX_162) (4|4) [SCAL] (1) $FUN_1.p = source.p0_par ($RES_SIM_205) (5|5) [SCAL] (1) $FUN_1.T = source.T0_par ($RES_SIM_206) (6|6) [SCAL] (1) $FUN_2.p = 287.0512249529787 * dT2c.rho * dT2c.T_out ($RES_SIM_207) (7|7) [SCAL] (1) dT2c.dT_fixed = dT2c.T_out - dT2c.T_in ($RES_BND_118) (8|8) [SCAL] (1) $FUN_2.T = dT2c.T_out ($RES_SIM_208) (9|9) [SCAL] (1) dT2c.du = dT2c.u_out - dT2c.u_in ($RES_BND_119) (10|10) [SCAL] (1) $FUN_7.p = dT2c.p_out ($RES_SIM_209) (11|11) [SCAL] (1) $DER.dT2c.m_flow * sink.L = dT2c.outlet.r - sink.r ($RES_SIM_71) (12|12) [RECD] (2) source.outlet.state = $FUN_1 ($RES_SIM_72) (13|14) [SCAL] (1) source.L * (-$DER.dT2c.m_flow) = source.outlet.r ($RES_SIM_73) (14|15) [RECD] (2) dT2c.outlet.state = $FUN_7 ($RES_SIM_58) (15|17) [SCAL] (1) dT2c.outlet.state.T = sink.inlet.state.T ($RES_SIM_107) (16|18) [SCAL] (1) dT2c.outlet.state.p = sink.inlet.state.p ($RES_SIM_108) (17|19) [SCAL] (1) dT2c.u_in = dT2c.h_in - dT2c.p_in / dT2c.rho ($RES_BND_120) (18|20) [SCAL] (1) $FUN_7.T = ThermofluidStream.Idealized.Tests.Processes.Isochoric.Fixed2.dT2c.Medium.T_h(dT2c.h_out) ($RES_SIM_210) (19|21) [SCAL] (1) dT2c.p_in = dT2c.inlet.state.p ($RES_AUX_159) (20|22) [SCAL] (1) dT2c.u_out = dT2c.h_out - dT2c.p_out / dT2c.rho ($RES_BND_121) (21|23) [SCAL] (1) dT2c.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), $FUN_2.T, true, ThermofluidStream.Media.myMedia.Interfaces.Choices.ReferenceEnthalpy.ZeroAt0K, 0.0) ($RES_AUX_200) (22|24) [SCAL] (1) dT2c.w_p = (dT2c.p_out - dT2c.p_in) / dT2c.rho ($RES_BND_122) (23|25) [SCAL] (1) dT2c.p_out = dT2c.p_in + dT2c.dp ($RES_SIM_60) (24|26) [SCAL] (1) dT2c.outlet.r = source.outlet.r - $DER.dT2c.m_flow * dT2c.L ($RES_SIM_61) (25|27) [SCAL] (1) source.outlet.state.T = dT2c.inlet.state.T ($RES_SIM_110) (26|28) [SCAL] (1) $FUN_6 = abs(dT2c.du) ($RES_AUX_197) (27|29) [SCAL] (1) source.outlet.state.p = dT2c.inlet.state.p ($RES_SIM_111) (28|30) [SCAL] (1) dT2c.singularityRegime = if noEvent($FUN_5 > 2.220446049250313e-16 and $FUN_6 < 2.220446049250313e-16) then -1.0 else 0.0 ($RES_SIM_64) (29|31) [SCAL] (1) $FUN_5 = abs(energyFlowSource.E_flow) ($RES_AUX_198) (30|32) [SCAL] (1) dT2c.p_out = $FUN_2.p ($RES_AUX_199) (31|33) [SCAL] (1) dT2c.m_flow = (dT2c.du * energyFlowSource.E_flow) / (4.930380657631324e-32 + dT2c.du ^ 2.0) ($RES_SIM_66) (32|34) [SCAL] (1) $DER.dT2c.h_in = $fDER0.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), dT2c.inlet.state.T, true, ThermofluidStream.Media.myMedia.Interfaces.Choices.ReferenceEnthalpy.ZeroAt0K, 0.0, $DER.dT2c.inlet.state.T, 0.0) ($RES_SIM_231) (33|35) [SCAL] (1) $DER.dT2c.p_out = $DER.$FUN_2.p ($RES_SIM_232) (34|36) [SCAL] (1) $DER.dT2c.T_in = $DER.dT2c.inlet.state.T ($RES_SIM_233) (35|37) [SCAL] (1) $DER.dT2c.m_flow = (($DER.dT2c.du * energyFlowSource.E_flow) * (4.930380657631324e-32 + dT2c.du ^ 2.0) - (2.0 * dT2c.du * $DER.dT2c.du) * dT2c.du * energyFlowSource.E_flow) / (4.930380657631324e-32 + dT2c.du ^ 2.0) ^ 2.0 ($RES_SIM_234) (36|38) [SCAL] (1) $DER.dT2c.rho = ((0.0034836987724536205 * $DER.dT2c.inlet.state.p) * dT2c.inlet.state.T - 0.0034836987724536205 * $DER.dT2c.inlet.state.T * dT2c.inlet.state.p) / dT2c.inlet.state.T ^ 2.0 ($RES_SIM_235) (37|39) [SCAL] (1) $DER.$FUN_1.p = 0.0 ($RES_SIM_236) (38|40) [SCAL] (1) $DER.$FUN_1.T = 0.0 ($RES_SIM_237) (39|41) [SCAL] (1) $DER.$FUN_2.p = 287.0512249529787 * $DER.dT2c.rho * dT2c.T_out + 287.0512249529787 * dT2c.rho * $DER.dT2c.T_out ($RES_SIM_238) (40|42) [SCAL] (1) 0.0 = $DER.dT2c.T_out - $DER.dT2c.T_in ($RES_SIM_239) (41|43) [SCAL] (1) $DER.$FUN_2.T = $DER.dT2c.T_out ($RES_SIM_240) (42|44) [SCAL] (1) $DER.dT2c.du = $DER.dT2c.u_out - $DER.dT2c.u_in ($RES_SIM_241) (43|45) [RECD] (2) $DER.source.outlet.state = $DER.$FUN_1 ($RES_SIM_242) (44|47) [SCAL] (1) $DER.dT2c.u_in = $DER.dT2c.h_in - ($DER.dT2c.p_in * dT2c.rho - dT2c.p_in * $DER.dT2c.rho) / dT2c.rho ^ 2.0 ($RES_SIM_243) (45|48) [SCAL] (1) $DER.dT2c.p_in = $DER.dT2c.inlet.state.p ($RES_SIM_244) (46|49) [SCAL] (1) $DER.dT2c.u_out = $DER.dT2c.h_out - ($DER.dT2c.p_out * dT2c.rho - dT2c.p_out * $DER.dT2c.rho) / dT2c.rho ^ 2.0 ($RES_SIM_245) (47|50) [SCAL] (1) $DER.dT2c.h_out = $fDER0.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), $FUN_2.T, true, ThermofluidStream.Media.myMedia.Interfaces.Choices.ReferenceEnthalpy.ZeroAt0K, 0.0, $DER.$FUN_2.T, 0.0) ($RES_SIM_246) (48|51) [SCAL] (1) $DER.source.outlet.state.T = $DER.dT2c.inlet.state.T ($RES_SIM_247) (49|52) [SCAL] (1) $DER.source.outlet.state.p = $DER.dT2c.inlet.state.p ($RES_SIM_248) =================== Scalar Matching =================== variable to equation ********************** var 1 --> eqn 14 var 2 --> eqn 3 var 3 --> eqn 24 var 4 --> eqn 32 var 5 --> eqn 4 var 6 --> eqn 7 var 7 --> eqn -1 var 8 --> eqn 27 var 9 --> eqn 2 var 10 --> eqn 6 var 11 --> eqn 25 var 12 --> eqn 16 var 13 --> eqn 26 var 14 --> eqn 1 var 15 --> eqn 20 var 16 --> eqn 8 var 17 --> eqn 5 var 18 --> eqn 10 var 19 --> eqn 18 var 20 --> eqn 29 var 21 --> eqn -1 var 22 --> eqn 28 var 23 --> eqn 9 var 24 --> eqn 22 var 25 --> eqn 19 var 26 --> eqn 21 var 27 --> eqn 11 var 28 --> eqn 17 var 29 --> eqn 23 var 30 --> eqn 30 var 31 --> eqn -1 var 32 --> eqn 31 var 33 --> eqn 15 var 34 --> eqn 39 var 35 --> eqn 40 var 36 --> eqn 35 var 37 --> eqn 36 var 38 --> eqn 42 var 39 --> eqn 37 var 40 --> eqn 45 var 41 --> eqn 46 var 42 --> eqn -1 var 43 --> eqn -1 var 44 --> eqn 34 var 45 --> eqn -1 var 46 --> eqn 47 var 47 --> eqn 41 var 48 --> eqn 49 var 49 --> eqn 44 var 50 --> eqn 43 var 51 --> eqn 50 var 52 --> eqn 38 var 53 --> eqn 51 var 54 --> eqn 48 var 55 --> eqn 52 var 56 --> eqn 33 equation to variable ********************** eqn 1 --> var 14 eqn 2 --> var 9 eqn 3 --> var 2 eqn 4 --> var 5 eqn 5 --> var 17 eqn 6 --> var 10 eqn 7 --> var 6 eqn 8 --> var 16 eqn 9 --> var 23 eqn 10 --> var 18 eqn 11 --> var 27 eqn 12 --> var -1 eqn 13 --> var -1 eqn 14 --> var 1 eqn 15 --> var 33 eqn 16 --> var 12 eqn 17 --> var 28 eqn 18 --> var 19 eqn 19 --> var 25 eqn 20 --> var 15 eqn 21 --> var 26 eqn 22 --> var 24 eqn 23 --> var 29 eqn 24 --> var 3 eqn 25 --> var 11 eqn 26 --> var 13 eqn 27 --> var 8 eqn 28 --> var 22 eqn 29 --> var 20 eqn 30 --> var 30 eqn 31 --> var 32 eqn 32 --> var 4 eqn 33 --> var 56 eqn 34 --> var 44 eqn 35 --> var 36 eqn 36 --> var 37 eqn 37 --> var 39 eqn 38 --> var 52 eqn 39 --> var 34 eqn 40 --> var 35 eqn 41 --> var 47 eqn 42 --> var 38 eqn 43 --> var 50 eqn 44 --> var 49 eqn 45 --> var 40 eqn 46 --> var 41 eqn 47 --> var 46 eqn 48 --> var 54 eqn 49 --> var 48 eqn 50 --> var 51 eqn 51 --> var 53 eqn 52 --> var 55 " [Timeout remaining time 659] [Calling sys.exit(0), Time elapsed: 2.8365365117788315] Failed to read output from testmodel.py, exit status != 0: 0.5526596661657095 0.560016866 0.11171881799999994 Calling exit ...