Running: ./testmodel.py --libraries=/home/hudson/saved_omc/libraries/.openmodelica/libraries --ompython_omhome=/usr ThermofluidStream_ThermofluidStream.Idealized.Examples.AirCycle.Step6Junction.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 0.001793/0.001793, allocations: 84.89 kB / 20.22 MB, free: 4.203 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 0.002147/0.002147, allocations: 165.6 kB / 23.53 MB, free: 0.8828 MB / 18.57 MB
"
[Timeout remaining time 180]
loadFile("/home/hudson/saved_omc/libraries/.openmodelica/libraries/Modelica 4.1.0+maint.om/package.mo", uses=false) [Timeout 180]
"Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/Modelica 4.1.0+maint.om/package.mo): time 1.466/1.466, allocations: 177.1 MB / 203.9 MB, free: 5.605 MB / 186.7 MB
"
[Timeout remaining time 178]
loadFile("/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermofluidStream 1.4.0/package.mo", uses=false) [Timeout 180]
"Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermofluidStream 1.4.0/package.mo): time 0.9856/0.9856, allocations: 118.6 MB / 379 MB, free: 1.484 MB / 346.7 MB
"
[Timeout remaining time 179]
Using package ThermofluidStream with version 1.4.0 (/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermofluidStream 1.4.0/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.Step6Junction,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|airSink.m_flow|airSink.m_flowSpec|airSink.m_flow_fixed|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|junction.L|junction.assertionLevel|der.junction.m_flowA.|der.junction.m_flowB.|junction.dp_AB_rel|junction.free|junction.hA|junction.hB|junction.h_mix|junction.inletA.m_flow|junction.inletA.r|junction.inletA.state.T|junction.inletA.state.p|junction.inletB.m_flow|junction.inletB.r|junction.inletB.state.T|junction.inletB.state.p|junction.isDPWithinTol|junction.m_flowA|junction.m_flowA_reg|junction.m_flowB|junction.m_flowB_reg|junction.m_flow_eps|der.junction.outlet.m_flow.|junction.outlet.m_flow|junction.outlet.r|junction.outlet.state.T|junction.outlet.state.p|junction.pA|junction.pB|junction.p_mix|junction.rA|junction.rA2|junction.rB|junction.rB2|junction.r_mix|junction.relTol_dp_AB|junction.stateA.T|junction.stateA.p|junction.stateB.T|junction.stateB.p|junction.wA|junction.wB|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|outletEnthalpyFlowRate.TC|outletEnthalpyFlowRate.digits|outletEnthalpyFlowRate.direct_value|outletEnthalpyFlowRate.init|outletEnthalpyFlowRate.inlet.m_flow|outletEnthalpyFlowRate.inlet.r|outletEnthalpyFlowRate.inlet.state.T|outletEnthalpyFlowRate.inlet.state.p|outletEnthalpyFlowRate.m_flow|outletEnthalpyFlowRate.outlet.m_flow|outletEnthalpyFlowRate.outlet.r|outletEnthalpyFlowRate.outlet.state.T|outletEnthalpyFlowRate.outlet.state.p|outletEnthalpyFlowRate.quantity|outletEnthalpyFlowRate.rho_min|outletEnthalpyFlowRate.value|outletEnthalpyFlowRate.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_ThermofluidStream.Idealized.Examples.AirCycle.Step6Junction")
translateModel(ThermofluidStream.Idealized.Examples.AirCycle.Step6Junction,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|airSink.m_flow|airSink.m_flowSpec|airSink.m_flow_fixed|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|junction.L|junction.assertionLevel|der.junction.m_flowA.|der.junction.m_flowB.|junction.dp_AB_rel|junction.free|junction.hA|junction.hB|junction.h_mix|junction.inletA.m_flow|junction.inletA.r|junction.inletA.state.T|junction.inletA.state.p|junction.inletB.m_flow|junction.inletB.r|junction.inletB.state.T|junction.inletB.state.p|junction.isDPWithinTol|junction.m_flowA|junction.m_flowA_reg|junction.m_flowB|junction.m_flowB_reg|junction.m_flow_eps|der.junction.outlet.m_flow.|junction.outlet.m_flow|junction.outlet.r|junction.outlet.state.T|junction.outlet.state.p|junction.pA|junction.pB|junction.p_mix|junction.rA|junction.rA2|junction.rB|junction.rB2|junction.r_mix|junction.relTol_dp_AB|junction.stateA.T|junction.stateA.p|junction.stateB.T|junction.stateB.p|junction.wA|junction.wB|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|outletEnthalpyFlowRate.TC|outletEnthalpyFlowRate.digits|outletEnthalpyFlowRate.direct_value|outletEnthalpyFlowRate.init|outletEnthalpyFlowRate.inlet.m_flow|outletEnthalpyFlowRate.inlet.r|outletEnthalpyFlowRate.inlet.state.T|outletEnthalpyFlowRate.inlet.state.p|outletEnthalpyFlowRate.m_flow|outletEnthalpyFlowRate.outlet.m_flow|outletEnthalpyFlowRate.outlet.r|outletEnthalpyFlowRate.outlet.state.T|outletEnthalpyFlowRate.outlet.state.p|outletEnthalpyFlowRate.quantity|outletEnthalpyFlowRate.rho_min|outletEnthalpyFlowRate.value|outletEnthalpyFlowRate.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_ThermofluidStream.Idealized.Examples.AirCycle.Step6Junction") [Timeout 660]
"Notification: Performance of FrontEnd - Absyn->SCode: time 9.067e-06/9.067e-06, allocations: 2.312 kB / 483.7 MB, free: 8.219 MB / 410.7 MB
Notification: Performance of NFInst.instantiate(ThermofluidStream.Idealized.Examples.AirCycle.Step6Junction): time 0.4414/0.4415, allocations: 202.2 MB / 0.6698 GB, free: 10.39 MB / 0.5573 GB
Notification: Performance of NFInst.instExpressions: time 0.009447/0.4509, allocations: 9.099 MB / 0.6787 GB, free: 10.33 MB / 0.5573 GB
Notification: Performance of NFInst.updateImplicitVariability: time 0.0009419/0.4518, allocations: 62.88 kB / 0.6788 GB, free: 10.33 MB / 0.5573 GB
Notification: Performance of NFTyping.typeComponents: time 0.001315/0.4532, allocations: 0.608 MB / 0.6794 GB, free: 10.31 MB / 0.5573 GB
Notification: Performance of NFTyping.typeBindings: time 0.003833/0.457, allocations: 1.856 MB / 0.6812 GB, free: 10.25 MB / 0.5573 GB
Notification: Performance of NFTyping.typeClassSections: time 0.002731/0.4597, allocations: 1.328 MB / 0.6825 GB, free: 10.16 MB / 0.5573 GB
Notification: Performance of NFFlatten.flatten: time 0.002202/0.4619, allocations: 2.574 MB / 0.685 GB, free: 9.559 MB / 0.5573 GB
Notification: Performance of NFFlatten.resolveConnections: time 0.0004084/0.4623, allocations: 210.4 kB / 0.6852 GB, free: 9.504 MB / 0.5573 GB
Notification: Performance of NFEvalConstants.evaluate: time 0.002033/0.4644, allocations: 1.58 MB / 0.6867 GB, free: 9.363 MB / 0.5573 GB
Notification: Performance of NFSimplifyModel.simplify: time 0.0006718/0.465, allocations: 0.5246 MB / 0.6872 GB, free: 9.289 MB / 0.5573 GB
Notification: Performance of NFPackage.collectConstants: time 0.0001537/0.4652, allocations: 90.12 kB / 0.6873 GB, free: 9.289 MB / 0.5573 GB
Notification: Performance of NFFlatten.collectFunctions: time 0.003457/0.4686, allocations: 1.735 MB / 0.689 GB, free: 9.188 MB / 0.5573 GB
Notification: Performance of combineBinaries: time 0.00136/0.47, allocations: 2.419 MB / 0.6914 GB, free: 8.191 MB / 0.5573 GB
Notification: Performance of replaceArrayConstructors: time 0.000569/0.4706, allocations: 1.563 MB / 0.6929 GB, free: 7.352 MB / 0.5573 GB
Notification: Performance of NFVerifyModel.verify: time 0.0001411/0.4707, allocations: 126.6 kB / 0.693 GB, free: 7.352 MB / 0.5573 GB
Notification: Performance of FrontEnd: time 0.0005317/0.4713, allocations: 311.2 kB / 0.6933 GB, free: 7.324 MB / 0.5573 GB
Notification: Model statistics after passing the front-end and creating the data structures used by the back-end:
 * Number of equations: 242 (225)
 * Number of variables: 242 (238)
Notification: Performance of [SIM] Bindings: time 0.00421/0.4755, allocations: 6.076 MB / 0.6993 GB, free: 21.1 MB / 0.573 GB
Notification: Performance of [SIM] FunctionAlias: time 0.0009881/0.4764, allocations: 1.135 MB / 0.7004 GB, free: 20.71 MB / 0.573 GB
Notification: Performance of [SIM] Early Inline: time 0.00474/0.4812, allocations: 5.429 MB / 0.7057 GB, free: 20.14 MB / 0.573 GB
Notification: Performance of [SIM] Simplify 1: time 0.0005982/0.4818, allocations: 464.5 kB / 0.7061 GB, free: 20 MB / 0.573 GB
Notification: Performance of [SIM] Alias: time 0.005264/0.4871, allocations: 5.693 MB / 0.7117 GB, free: 18.03 MB / 0.573 GB
Notification: Performance of [SIM] Simplify 2: time 0.0004039/0.4875, allocations: 358.8 kB / 0.712 GB, free: 17.88 MB / 0.573 GB
Notification: Performance of [SIM] Remove Stream: time 0.0002145/0.4877, allocations: 251.7 kB / 0.7123 GB, free: 17.79 MB / 0.573 GB
Notification: Performance of [SIM] Detect States: time 0.0006353/0.4883, allocations: 0.7853 MB / 0.713 GB, free: 17.62 MB / 0.573 GB
Notification: Performance of [SIM] Events: time 0.0002809/0.4886, allocations: 347.5 kB / 0.7134 GB, free: 17.6 MB / 0.573 GB
Notification: Performance of [SIM] Partitioning: time 0.001217/0.4898, allocations: 1.248 MB / 0.7146 GB, free: 17.36 MB / 0.573 GB
Error: NBCausalize.checkSystemVariabilities failed. The following strong component has conflicting types: Real != Integer
BLOCK: Single Strong Component (status = Solve.UNPROCESSED, size = 1)
-----------------------------------------------------------------------
### Variable:
	Real valve.isDPLossAligned = CAST(Real, sign(valve.m_flow * valve.dpLoss))
### Equation:
	[SCAL] (1) valve.isDPLossAligned = sign(valve.m_flow * valve.dpLoss); ($RES_AUX_253)
Error: NBCausalize.checkSystemVariabilities failed. The following strong component has conflicting types: Real != Integer
BLOCK: Single Strong Component (status = Solve.UNPROCESSED, size = 1)
-----------------------------------------------------------------------
### Variable:
	Real junction.isDPWithinTol
### Equation:
	[SCAL] (1) junction.isDPWithinTol = sign(junction.relTol_dp_AB - junction.dp_AB_rel); ($RES_AUX_262)
Error: NBCausalize.checkSystemVariabilities failed. The following strong component has conflicting types: Real != Integer
BLOCK: Single Strong Component (status = Solve.UNPROCESSED, size = 1)
-----------------------------------------------------------------------
### Variable:
	Real valve.isDPLossSetAligned = CAST(Real, sign(valve.m_flow * valve.dpLoss))
### Equation:
	[SCAL] (1) valve.isDPLossSetAligned = sign(valve.m_flow * valve.dpLoss); ($RES_AUX_252)
"
[Timeout remaining time 660]
[Calling sys.exit(0), Time elapsed: 3.7994431340048322]