Running: ./testmodel.py --libraries=/home/hudson/saved_omc/libraries/.openmodelica/libraries --ompython_omhome=/usr ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AirCycle.Step5Splitter.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 0.0007971/0.0007971, allocations: 84.23 kB / 20.06 MB, free: 4.465 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 0.000739/0.000739, allocations: 173.9 kB / 23.36 MB, free: 1.16 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 0.8495/0.8495, allocations: 177.1 MB / 203.7 MB, free: 5.73 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 0.6232/0.6232, allocations: 116 MB / 376.2 MB, free: 4.168 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.Examples.AirCycle.Step5Splitter,tolerance=1e-06,outputFormat="mat",numberOfIntervals=100,variableFilter="CPUtime|EventCounter|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|airSink.L|der.airSink.inlet.m_flow.|airSink.inlet.m_flow|airSink.inlet.r|airSink.inlet.state.T|airSink.inlet.state.p|airSink1.L|der.airSink1.inlet.m_flow.|airSink1.inlet.m_flow|airSink1.inlet.r|airSink1.inlet.state.T|airSink1.inlet.state.p|airSource.L|airSource.T0|airSource.T0_par|airSource.h0|airSource.h0_par|der.airSource.outlet.m_flow.|airSource.outlet.m_flow|airSource.outlet.r|airSource.outlet.state.T|airSource.outlet.state.p|airSource.p0|airSource.p0_par|coefficientOfPerformance.displayVariablefinal|coefficientOfPerformance.showNumber|coefficientOfPerformance.significantDigits|compressor.L|compressor.P|compressor.P_nom|compressor.TC|compressor.adiabaticModel.eta_is|compressor.adiabaticModel.h_in|compressor.adiabaticModel.h_out|compressor.adiabaticModel.h_out_is|compressor.adiabaticModel.p_out|compressor.adiabaticModel.s_in|compressor.adiabaticModel.state_in.T|compressor.adiabaticModel.state_in.p|compressor.adiabaticModel.w_t|compressor.adiabaticModel.w_t_is|compressor.assertionLevel|compressor.clip_p_out|compressor.dh|compressor.dp|compressor.dp_fixed|compressor.dp_nom|compressor.dp_start|compressor.dr_corr|compressor.etaSpec|compressor.eta_actual|compressor.eta_fixed|compressor.eta_is|compressor.h_in|compressor.h_out|compressor.initM_flow|der.compressor.inlet.m_flow.|compressor.inlet.m_flow|compressor.inlet.r|compressor.inlet.state.T|compressor.inlet.state.p|compressor.m_acceleration_0|compressor.m_flow|compressor.m_flowStateSelect|compressor.m_flow_0|compressor.outlet.m_flow|compressor.outlet.r|compressor.outlet.state.T|compressor.outlet.state.p|compressor.outletSpec|compressor.outletSpec_actual|compressor.outletValueSpec|compressor.pRatio|compressor.pRatio_fixed|compressor.p_in|compressor.p_min|compressor.p_out|compressor.p_out_fixed|compressor.singularityRegime|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|heatExchangerSideA.L|heatExchangerSideA.P|heatExchangerSideA.Q_flow|heatExchangerSideA.T_out_fixed|heatExchangerSideA.assertionLevel|heatExchangerSideA.clip_p_out|heatExchangerSideA.dT|heatExchangerSideA.dT_fixed|heatExchangerSideA.dh|heatExchangerSideA.dh_fixed|heatExchangerSideA.dp|heatExchangerSideA.dr_corr|heatExchangerSideA.du|heatExchangerSideA.h_in|heatExchangerSideA.h_out|heatExchangerSideA.h_out_fixed|heatExchangerSideA.initM_flow|der.heatExchangerSideA.inlet.m_flow.|heatExchangerSideA.inlet.m_flow|heatExchangerSideA.inlet.r|heatExchangerSideA.inlet.state.T|heatExchangerSideA.inlet.state.p|heatExchangerSideA.m_acceleration_0|heatExchangerSideA.m_flow|heatExchangerSideA.m_flowStateSelect|heatExchangerSideA.m_flow_0|heatExchangerSideA.outlet.m_flow|heatExchangerSideA.outlet.r|heatExchangerSideA.outlet.state.T|heatExchangerSideA.outlet.state.p|heatExchangerSideA.outletSpec|heatExchangerSideA.outletSpec_actual|heatExchangerSideA.outletValueSpec|heatExchangerSideA.p|heatExchangerSideA.p_in|heatExchangerSideA.p_inf|heatExchangerSideA.p_min|heatExchangerSideA.p_out|heatExchangerSideA.q|heatExchangerSideA.rho_in|heatExchangerSideA.rho_out|heatExchangerSideA.singularityRegime|heatExchangerSideA.systemSpec|heatExchangerSideA.u_in|heatExchangerSideA.u_out|heatExchangerSideA.v_in|heatExchangerSideA.v_out|heatExchangerSideA.w_amb|heatExchangerSideA.w_exp|heatExchangerSideA.w_exp_net|inletEnthalpyFlowRate.TC|inletEnthalpyFlowRate.digits|inletEnthalpyFlowRate.direct_value|inletEnthalpyFlowRate.init|inletEnthalpyFlowRate.inlet.m_flow|inletEnthalpyFlowRate.inlet.r|inletEnthalpyFlowRate.inlet.state.T|inletEnthalpyFlowRate.inlet.state.p|inletEnthalpyFlowRate.m_flow|inletEnthalpyFlowRate.outlet.m_flow|inletEnthalpyFlowRate.outlet.r|inletEnthalpyFlowRate.outlet.state.T|inletEnthalpyFlowRate.outlet.state.p|inletEnthalpyFlowRate.quantity|inletEnthalpyFlowRate.rho_min|inletEnthalpyFlowRate.value|inletEnthalpyFlowRate.value_0|massFlowRateIn.L|massFlowRateIn.clip_p_out|massFlowRateIn.dp|massFlowRateIn.dr_corr|massFlowRateIn.h_in|massFlowRateIn.h_out|massFlowRateIn.initM_flow|der.massFlowRateIn.inlet.m_flow.|massFlowRateIn.inlet.m_flow|massFlowRateIn.inlet.r|massFlowRateIn.inlet.state.T|massFlowRateIn.inlet.state.p|massFlowRateIn.m_acceleration_0|massFlowRateIn.m_flow|massFlowRateIn.m_flowSpec|massFlowRateIn.m_flowStateSelect|massFlowRateIn.m_flow_0|massFlowRateIn.m_flow_actual|massFlowRateIn.m_flow_fixed|massFlowRateIn.outlet.m_flow|massFlowRateIn.outlet.r|massFlowRateIn.outlet.state.T|massFlowRateIn.outlet.state.p|massFlowRateIn.p_in|massFlowRateIn.p_min|massFlowRateIn.p_out|massFlowRateValve.L|massFlowRateValve.clip_p_out|massFlowRateValve.dp|massFlowRateValve.dr_corr|massFlowRateValve.h_in|massFlowRateValve.h_out|massFlowRateValve.initM_flow|der.massFlowRateValve.inlet.m_flow.|massFlowRateValve.inlet.m_flow|massFlowRateValve.inlet.r|massFlowRateValve.inlet.state.T|massFlowRateValve.inlet.state.p|massFlowRateValve.m_acceleration_0|massFlowRateValve.m_flow|massFlowRateValve.m_flowSpec|massFlowRateValve.m_flowStateSelect|massFlowRateValve.m_flow_0|massFlowRateValve.m_flow_actual|massFlowRateValve.m_flow_fixed|massFlowRateValve.m_flow_prescribed|massFlowRateValve.outlet.m_flow|massFlowRateValve.outlet.r|massFlowRateValve.outlet.state.T|massFlowRateValve.outlet.state.p|massFlowRateValve.p_in|massFlowRateValve.p_min|massFlowRateValve.p_out|massFlowRateValveRamp.duration|massFlowRateValveRamp.height|massFlowRateValveRamp.offset|massFlowRateValveRamp.startTime|massFlowRateValveRamp.y|outlet1EnthalpyFlowRate.TC|outlet1EnthalpyFlowRate.digits|outlet1EnthalpyFlowRate.direct_value|outlet1EnthalpyFlowRate.init|outlet1EnthalpyFlowRate.inlet.m_flow|outlet1EnthalpyFlowRate.inlet.r|outlet1EnthalpyFlowRate.inlet.state.T|outlet1EnthalpyFlowRate.inlet.state.p|outlet1EnthalpyFlowRate.m_flow|outlet1EnthalpyFlowRate.outlet.m_flow|outlet1EnthalpyFlowRate.outlet.r|outlet1EnthalpyFlowRate.outlet.state.T|outlet1EnthalpyFlowRate.outlet.state.p|outlet1EnthalpyFlowRate.quantity|outlet1EnthalpyFlowRate.rho_min|outlet1EnthalpyFlowRate.value|outlet1EnthalpyFlowRate.value_0|outlet2EnthalpyFlowRate.TC|outlet2EnthalpyFlowRate.digits|outlet2EnthalpyFlowRate.direct_value|outlet2EnthalpyFlowRate.init|outlet2EnthalpyFlowRate.inlet.m_flow|outlet2EnthalpyFlowRate.inlet.r|outlet2EnthalpyFlowRate.inlet.state.T|outlet2EnthalpyFlowRate.inlet.state.p|outlet2EnthalpyFlowRate.m_flow|outlet2EnthalpyFlowRate.outlet.m_flow|outlet2EnthalpyFlowRate.outlet.r|outlet2EnthalpyFlowRate.outlet.state.T|outlet2EnthalpyFlowRate.outlet.state.p|outlet2EnthalpyFlowRate.quantity|outlet2EnthalpyFlowRate.rho_min|outlet2EnthalpyFlowRate.value|outlet2EnthalpyFlowRate.value_0|splitter.L|splitter.inlet.m_flow|splitter.inlet.r|splitter.inlet.state.T|splitter.inlet.state.p|splitter.outletA.m_flow|splitter.outletA.r|splitter.outletA.state.T|splitter.outletA.state.p|splitter.outletB.m_flow|splitter.outletB.r|splitter.outletB.state.T|splitter.outletB.state.p|splitter.splitterN.L|splitter.splitterN.N|der.splitter.splitterN.inlet.m_flow.|splitter.splitterN.inlet.m_flow|splitter.splitterN.inlet.r|splitter.splitterN.inlet.state.T|splitter.splitterN.inlet.state.p|der.splitter.splitterN.outlets.1..m_flow.|splitter.splitterN.outlets.1..m_flow|splitter.splitterN.outlets.1..r|splitter.splitterN.outlets.1..state.T|splitter.splitterN.outlets.1..state.p|der.splitter.splitterN.outlets.2..m_flow.|splitter.splitterN.outlets.2..m_flow|splitter.splitterN.outlets.2..r|splitter.splitterN.outlets.2..state.T|splitter.splitterN.outlets.2..state.p|splitter.splitterN.r_mix|turbine.L|turbine.P|turbine.P_nom|turbine.TC|turbine.adiabaticModel.eta_is|turbine.adiabaticModel.h_in|turbine.adiabaticModel.h_out|turbine.adiabaticModel.h_out_is|turbine.adiabaticModel.p_out|turbine.adiabaticModel.s_in|turbine.adiabaticModel.state_in.T|turbine.adiabaticModel.state_in.p|turbine.adiabaticModel.w_t|turbine.adiabaticModel.w_t_is|turbine.assertionLevel|turbine.clip_p_out|turbine.dh|turbine.dp|turbine.dp_fixed|turbine.dp_nom|turbine.dp_start|turbine.dr_corr|turbine.etaSpec|turbine.eta_actual|turbine.eta_fixed|turbine.eta_is|turbine.h_in|turbine.h_out|turbine.initM_flow|der.turbine.inlet.m_flow.|turbine.inlet.m_flow|turbine.inlet.r|turbine.inlet.state.T|turbine.inlet.state.p|turbine.m_acceleration_0|turbine.m_flow|turbine.m_flowStateSelect|turbine.m_flow_0|turbine.outlet.m_flow|turbine.outlet.r|turbine.outlet.state.T|turbine.outlet.state.p|turbine.outletSpec|turbine.outletSpec_actual|turbine.outletValueSpec|turbine.pRatio|turbine.pRatio_fixed|turbine.p_in|turbine.p_min|turbine.p_out|turbine.p_out_fixed|turbine.singularityRegime|valve.L|valve.assertionLevel|valve.clip_p_out|valve.dp|valve.dpLoss|valve.dpLoss_fixed|valve.dpLoss_set|valve.dr_corr|valve.h_in|valve.h_out|valve.initM_flow|der.valve.inlet.m_flow.|valve.inlet.m_flow|valve.inlet.r|valve.inlet.state.T|valve.inlet.state.p|valve.isDPLossAligned|valve.isDPLossSetAligned|valve.m_acceleration_0|valve.m_flow|valve.m_flowStateSelect|valve.m_flow_0|valve.outlet.m_flow|valve.outlet.r|valve.outlet.state.T|valve.outlet.state.p|valve.outletSpec|valve.outletSpec_actual|valve.outletValueSpec|valve.p_in|valve.p_min|valve.p_out|valve.p_out_fixed|valve.prLoss|valve.prLoss_fixed",fileNamePrefix="ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AirCycle.Step5Splitter") translateModel(ThermofluidStream.Idealized.Examples.AirCycle.Step5Splitter,tolerance=1e-06,outputFormat="mat",numberOfIntervals=100,variableFilter="CPUtime|EventCounter|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|airSink.L|der.airSink.inlet.m_flow.|airSink.inlet.m_flow|airSink.inlet.r|airSink.inlet.state.T|airSink.inlet.state.p|airSink1.L|der.airSink1.inlet.m_flow.|airSink1.inlet.m_flow|airSink1.inlet.r|airSink1.inlet.state.T|airSink1.inlet.state.p|airSource.L|airSource.T0|airSource.T0_par|airSource.h0|airSource.h0_par|der.airSource.outlet.m_flow.|airSource.outlet.m_flow|airSource.outlet.r|airSource.outlet.state.T|airSource.outlet.state.p|airSource.p0|airSource.p0_par|coefficientOfPerformance.displayVariablefinal|coefficientOfPerformance.showNumber|coefficientOfPerformance.significantDigits|compressor.L|compressor.P|compressor.P_nom|compressor.TC|compressor.adiabaticModel.eta_is|compressor.adiabaticModel.h_in|compressor.adiabaticModel.h_out|compressor.adiabaticModel.h_out_is|compressor.adiabaticModel.p_out|compressor.adiabaticModel.s_in|compressor.adiabaticModel.state_in.T|compressor.adiabaticModel.state_in.p|compressor.adiabaticModel.w_t|compressor.adiabaticModel.w_t_is|compressor.assertionLevel|compressor.clip_p_out|compressor.dh|compressor.dp|compre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ate.p|outlet1EnthalpyFlowRate.quantity|outlet1EnthalpyFlowRate.rho_min|outlet1EnthalpyFlowRate.value|outlet1EnthalpyFlowRate.value_0|outlet2EnthalpyFlowRate.TC|outlet2EnthalpyFlowRate.digits|outlet2EnthalpyFlowRate.direct_value|outlet2EnthalpyFlowRate.init|outlet2EnthalpyFlowRate.inlet.m_flow|outlet2EnthalpyFlowRate.inlet.r|outlet2EnthalpyFlowRate.inlet.state.T|outlet2EnthalpyFlowRate.inlet.state.p|outlet2EnthalpyFlowRate.m_flow|outlet2EnthalpyFlowRate.outlet.m_flow|outlet2EnthalpyFlowRate.outlet.r|outlet2EnthalpyFlowRate.outlet.state.T|outlet2EnthalpyFlowRate.outlet.state.p|outlet2EnthalpyFlowRate.quantity|outlet2EnthalpyFlowRate.rho_min|outlet2EnthalpyFlowRate.value|outlet2EnthalpyFlowRate.value_0|splitter.L|splitter.inlet.m_flow|splitter.inlet.r|splitter.inlet.state.T|splitter.inlet.state.p|splitter.outletA.m_flow|splitter.outletA.r|splitter.outletA.state.T|splitter.outletA.state.p|splitter.outletB.m_flow|splitter.outletB.r|splitter.outletB.state.T|splitter.outletB.state.p|splitter.splitterN.L|splitter.splitterN.N|der.splitter.splitterN.inlet.m_flow.|splitter.splitterN.inlet.m_flow|splitter.splitterN.inlet.r|splitter.splitterN.inlet.state.T|splitter.splitterN.inlet.state.p|der.splitter.splitterN.outlets.1..m_flow.|splitter.splitterN.outlets.1..m_flow|splitter.splitterN.outlets.1..r|splitter.splitterN.outlets.1..state.T|splitter.splitterN.outlets.1..state.p|der.splitter.splitterN.outlets.2..m_flow.|splitter.splitterN.outlets.2..m_flow|splitter.splitterN.outlets.2..r|splitter.splitterN.outlets.2..state.T|splitter.splitterN.outlets.2..state.p|splitter.splitterN.r_mix|turbine.L|turbine.P|turbine.P_nom|turbine.TC|turbine.adiabaticModel.eta_is|turbine.adiabaticModel.h_in|turbine.adiabaticModel.h_out|turbine.adiabaticModel.h_out_is|turbine.adiabaticModel.p_out|turbine.adiabaticModel.s_in|turbine.adiabaticModel.state_in.T|turbine.adiabaticModel.state_in.p|turbine.adiabaticModel.w_t|turbine.adiabaticModel.w_t_is|turbine.assertionLevel|turbine.clip_p_out|turbine.dh|turbine.dp|turbine.dp_fixed|turbine.dp_nom|turbine.dp_start|turbine.dr_corr|turbine.etaSpec|turbine.eta_actual|turbine.eta_fixed|turbine.eta_is|turbine.h_in|turbine.h_out|turbine.initM_flow|der.turbine.inlet.m_flow.|turbine.inlet.m_flow|turbine.inlet.r|turbine.inlet.state.T|turbine.inlet.state.p|turbine.m_acceleration_0|turbine.m_flow|turbine.m_flowStateSelect|turbine.m_flow_0|turbine.outlet.m_flow|turbine.outlet.r|turbine.outlet.state.T|turbine.outlet.state.p|turbine.outletSpec|turbine.outletSpec_actual|turbine.outletValueSpec|turbine.pRatio|turbine.pRatio_fixed|turbine.p_in|turbine.p_min|turbine.p_out|turbine.p_out_fixed|turbine.singularityRegime|valve.L|valve.assertionLevel|valve.clip_p_out|valve.dp|valve.dpLoss|valve.dpLoss_fixed|valve.dpLoss_set|valve.dr_corr|valve.h_in|valve.h_out|valve.initM_flow|der.valve.inlet.m_flow.|valve.inlet.m_flow|valve.inlet.r|valve.inlet.state.T|valve.inlet.state.p|valve.isDPLossAligned|valve.isDPLossSetAligned|valve.m_acceleration_0|valve.m_flow|valve.m_flowStateSelect|valve.m_flow_0|valve.outlet.m_flow|valve.outlet.r|valve.outlet.state.T|valve.outlet.state.p|valve.outletSpec|valve.outletSpec_actual|valve.outletValueSpec|valve.p_in|valve.p_min|valve.p_out|valve.p_out_fixed|valve.prLoss|valve.prLoss_fixed",fileNamePrefix="ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AirCycle.Step5Splitter") [Timeout 660] "Notification: Performance of FrontEnd - Absyn->SCode: time 2.221e-05/2.221e-05, allocations: 10.19 kB / 0.5548 GB, free: 12.7 MB / 490.7 MB Notification: Performance of NFInst.instantiate(ThermofluidStream.Idealized.Examples.AirCycle.Step5Splitter): time 0.4738/0.4739, allocations: 206 MB / 0.756 GB, free: 11.53 MB / 0.6042 GB Notification: Performance of NFInst.instExpressions: time 0.01007/0.4839, allocations: 11.28 MB / 0.767 GB, free: 2.66 MB / 0.6042 GB Notification: Performance of NFInst.updateImplicitVariability: time 0.001382/0.4853, allocations: 66 kB / 0.7671 GB, free: 2.621 MB / 0.6042 GB Notification: Performance of NFTyping.typeComponents: time 0.001338/0.4866, allocations: 0.6239 MB / 0.7677 GB, free: 2.109 MB / 0.6042 GB Notification: Performance of NFTyping.typeBindings: time 0.004087/0.4907, allocations: 1.82 MB / 0.7694 GB, free: 0.6719 MB / 0.6042 GB Notification: Performance of NFTyping.typeClassSections: time 0.002975/0.4937, allocations: 1.419 MB / 0.7708 GB, free: 15.6 MB / 0.6198 GB Notification: Performance of NFFlatten.flatten: time 0.002596/0.4963, allocations: 2.55 MB / 0.7733 GB, free: 13.51 MB / 0.6198 GB Notification: Performance of NFFlatten.resolveConnections: time 0.0004296/0.4967, allocations: 208.3 kB / 0.7735 GB, free: 13.29 MB / 0.6198 GB Notification: Performance of NFEvalConstants.evaluate: time 0.002002/0.4987, allocations: 1.578 MB / 0.7751 GB, free: 11.71 MB / 0.6198 GB Notification: Performance of NFSimplifyModel.simplify: time 0.0004688/0.4992, allocations: 0.5061 MB / 0.7756 GB, free: 11.2 MB / 0.6198 GB Notification: Performance of NFPackage.collectConstants: time 8.833e-05/0.4993, allocations: 92 kB / 0.7756 GB, free: 11.11 MB / 0.6198 GB Notification: Performance of NFFlatten.collectFunctions: time 0.003635/0.5029, allocations: 1.778 MB / 0.7774 GB, free: 9.332 MB / 0.6198 GB Notification: Performance of combineBinaries: time 0.001198/0.5041, allocations: 2.356 MB / 0.7797 GB, free: 6.953 MB / 0.6198 GB Notification: Performance of replaceArrayConstructors: time 0.0006152/0.5047, allocations: 1.55 MB / 0.7812 GB, free: 5.383 MB / 0.6198 GB Notification: Performance of NFVerifyModel.verify: time 0.000171/0.5049, allocations: 132 kB / 0.7813 GB, free: 5.254 MB / 0.6198 GB Notification: Performance of FrontEnd: time 0.0006026/0.5055, allocations: 303.2 kB / 0.7816 GB, free: 4.957 MB / 0.6198 GB Notification: Model statistics after passing the front-end and creating the data structures used by the back-end: * Number of equations: 237 (221) * Number of variables: 237 (233) Notification: Performance of [SIM] Bindings: time 0.004153/0.5097, allocations: 6.006 MB / 0.7875 GB, free: 14.73 MB / 0.6355 GB Notification: Performance of [SIM] FunctionAlias: time 0.0008758/0.5105, allocations: 1.087 MB / 0.7885 GB, free: 13.58 MB / 0.6355 GB Notification: Performance of [SIM] Early Inline: time 0.003055/0.5136, allocations: 4.066 MB / 0.7925 GB, free: 9.523 MB / 0.6355 GB Notification: Performance of [SIM] Simplify 1: time 0.0004509/0.5141, allocations: 444.8 kB / 0.7929 GB, free: 9.031 MB / 0.6355 GB Notification: Performance of [SIM] Alias: time 0.004223/0.5183, allocations: 5.134 MB / 0.7979 GB, free: 3.27 MB / 0.6355 GB Notification: Performance of [SIM] Simplify 2: time 0.0002972/0.5186, allocations: 316.4 kB / 0.7982 GB, free: 2.922 MB / 0.6355 GB Notification: Performance of [SIM] Remove Stream: time 0.0001702/0.5187, allocations: 256.1 kB / 0.7985 GB, free: 2.633 MB / 0.6355 GB Notification: Performance of [SIM] Detect States: time 0.000706/0.5194, allocations: 0.8452 MB / 0.7993 GB, free: 1.703 MB / 0.6355 GB Notification: Performance of [SIM] Events: time 0.0001683/0.5196, allocations: 157.5 kB / 0.7995 GB, free: 1.547 MB / 0.6355 GB Notification: Performance of [SIM] Partitioning: time 0.0009938/0.5206, allocations: 1.222 MB / 0.8007 GB, free: 260 kB / 0.6355 GB Error: Internal error NBResolveSingularities.indexReduction failed because slicing during index reduction is not yet supported. Sliced Dummies: [STAT] (2) flow Real[2] splitter.splitterN.outlets.m_flow slice: {1} " [Timeout remaining time 659] [Calling sys.exit(0), Time elapsed: 2.813250553794205] Failed to read output from testmodel.py, exit status != 0: 0.5283512994647026 0.535441936 0.028168706 Calling exit ...