Running: ./testmodel.py --libraries=/home/hudson/saved_omc/libraries/.openmodelica/libraries --ompython_omhome=/usr ThermofluidStream_dev_ThermofluidStream.Idealized.Tests.Processes.Isochoric.Warnings2.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 0.0007512/0.0007512, allocations: 80.25 kB / 20.05 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 0.0007353/0.0007353, allocations: 178.3 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 0.8245/0.8245, allocations: 177.1 MB / 203.7 MB, free: 5.227 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 0.6139/0.6139, allocations: 116 MB / 376.2 MB, free: 4.137 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.Warnings2,tolerance=1e-06,outputFormat="mat",numberOfIntervals=100,variableFilter="CPUtime|EventCounter|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|der.T_out2.du.|der.T_out2.h_out.|der.T_out2.p_out.|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.outletSpec_prescribed|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|der.T_out2c.du.|der.T_out2c.h_out.|der.T_out2c.p_out.|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.outletSpec_prescribed|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|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|der.dT2.du.|der.dT2.h_out.|der.dT2.p_out.|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.outletSpec_prescribed|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|der.dT2c.du.|der.dT2c.h_out.|der.dT2c.p_out.|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.outletSpec_prescribed|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|der.dT.|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|der.energyFlowSource.E_flow.|heatFlowRate.T_falling|heatFlowRate.T_rising|heatFlowRate.T_start|heatFlowRate.T_width|heatFlowRate.amplitude|heatFlowRate.count|heatFlowRate.falling|heatFlowRate.nperiod|heatFlowRate.offset|heatFlowRate.period|heatFlowRate.rising|heatFlowRate.startTime|heatFlowRate.width|heatFlowRate.y|outletTemperature.y|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|temperatureDifference.T_falling|temperatureDifference.T_rising|temperatureDifference.T_start|temperatureDifference.T_width|temperatureDifference.amplitude|temperatureDifference.count|temperatureDifference.falling|temperatureDifference.nperiod|temperatureDifference.offset|temperatureDifference.period|temperatureDifference.rising|temperatureDifference.startTime|temperatureDifference.width|temperatureDifference.y",fileNamePrefix="ThermofluidStream_dev_ThermofluidStream.Idealized.Tests.Processes.Isochoric.Warnings2") translateModel(ThermofluidStream.Idealized.Tests.Processes.Isochoric.Warnings2,tolerance=1e-06,outputFormat="mat",numberOfIntervals=100,variableFilter="CPUtime|EventCounter|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|der.T_out2.du.|der.T_out2.h_out.|der.T_out2.p_out.|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.outletSpec_prescribed|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|der.T_out2c.du.|der.T_out2c.h_out.|der.T_out2c.p_out.|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.outletSpec_prescribed|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|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|der.dT2.du.|der.dT2.h_out.|der.dT2.p_out.|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.outletSpec_prescribed|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|der.dT2c.du.|der.dT2c.h_out.|der.dT2c.p_out.|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.outletSpec_prescribed|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|der.dT.|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|der.energyFlowSource.E_flow.|heatFlowRate.T_falling|heatFlowRate.T_rising|heatFlowRate.T_start|heatFlowRate.T_width|heatFlowRate.amplitude|heatFlowRate.count|heatFlowRate.falling|heatFlowRate.nperiod|heatFlowRate.offset|heatFlowRate.period|heatFlowRate.rising|heatFlowRate.startTime|heatFlowRate.width|heatFlowRate.y|outletTemperature.y|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|temperatureDifference.T_falling|temperatureDifference.T_rising|temperatureDifference.T_start|temperatureDifference.T_width|temperatureDifference.amplitude|temperatureDifference.count|temperatureDifference.falling|temperatureDifference.nperiod|temperatureDifference.offset|temperatureDifference.period|temperatureDifference.rising|temperatureDifference.startTime|temperatureDifference.width|temperatureDifference.y",fileNamePrefix="ThermofluidStream_dev_ThermofluidStream.Idealized.Tests.Processes.Isochoric.Warnings2") [Timeout 660] "Notification: Performance of FrontEnd - Absyn->SCode: time 2.281e-05/2.281e-05, allocations: 6.25 kB / 0.5548 GB, free: 12.71 MB / 490.7 MB Notification: Performance of NFInst.instantiate(ThermofluidStream.Idealized.Tests.Processes.Isochoric.Warnings2): time 0.4565/0.4566, allocations: 179.7 MB / 0.7303 GB, free: 15.96 MB / 0.5886 GB Notification: Performance of NFInst.instExpressions: time 0.005175/0.4617, allocations: 2.982 MB / 0.7332 GB, free: 13.54 MB / 0.5886 GB Notification: Performance of NFInst.updateImplicitVariability: time 0.001183/0.4629, allocations: 87.06 kB / 0.7333 GB, free: 13.48 MB / 0.5886 GB Notification: Performance of NFTyping.typeComponents: time 0.001136/0.4641, allocations: 463.2 kB / 0.7337 GB, free: 13.1 MB / 0.5886 GB Notification: Performance of NFTyping.typeBindings: time 0.002927/0.467, allocations: 1.186 MB / 0.7349 GB, free: 12.12 MB / 0.5886 GB Notification: Performance of NFTyping.typeClassSections: time 0.00531/0.4723, allocations: 1.468 MB / 0.7363 GB, free: 11.03 MB / 0.5886 GB Notification: Performance of NFFlatten.flatten: time 0.003084/0.4754, allocations: 2.324 MB / 0.7386 GB, free: 9.59 MB / 0.5886 GB Notification: Performance of NFFlatten.resolveConnections: time 0.0004962/0.4759, allocations: 166.2 kB / 0.7387 GB, free: 9.484 MB / 0.5886 GB Notification: Performance of NFEvalConstants.evaluate: time 0.003708/0.4796, allocations: 1.808 MB / 0.7405 GB, free: 8.34 MB / 0.5886 GB Notification: Performance of NFSimplifyModel.simplify: time 0.0008288/0.4804, allocations: 456 kB / 0.7409 GB, free: 8.102 MB / 0.5886 GB Notification: Performance of NFPackage.collectConstants: time 0.000101/0.4805, allocations: 69.19 kB / 0.741 GB, free: 8.102 MB / 0.5886 GB Notification: Performance of NFFlatten.collectFunctions: time 0.002975/0.4835, allocations: 1.046 MB / 0.742 GB, free: 7.637 MB / 0.5886 GB Notification: Performance of combineBinaries: time 0.001444/0.4849, allocations: 2.028 MB / 0.744 GB, free: 6.262 MB / 0.5886 GB Notification: Performance of replaceArrayConstructors: time 0.0008197/0.4857, allocations: 1.353 MB / 0.7453 GB, free: 5.387 MB / 0.5886 GB Notification: Performance of NFVerifyModel.verify: time 0.0003953/0.4861, allocations: 107.3 kB / 0.7454 GB, free: 5.387 MB / 0.5886 GB Notification: Performance of FrontEnd: time 0.0005969/0.4867, allocations: 246.6 kB / 0.7457 GB, free: 5.238 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: 177 (169) * Number of variables: 177 (177) Notification: Performance of [SIM] Bindings: time 0.003841/0.4906, allocations: 4.885 MB / 0.7504 GB, free: 1.855 MB / 0.5886 GB Notification: Performance of [SIM] FunctionAlias: time 0.0009685/0.4915, allocations: 0.8928 MB / 0.7513 GB, free: 1.176 MB / 0.5886 GB Notification: Performance of [SIM] Early Inline: time 0.002366/0.4939, allocations: 3.133 MB / 0.7544 GB, free: 14.8 MB / 0.6042 GB Notification: Performance of [SIM] Simplify 1: time 0.0004383/0.4943, allocations: 342.4 kB / 0.7547 GB, free: 14.57 MB / 0.6042 GB Notification: Performance of [SIM] Alias: time 0.004254/0.4986, allocations: 4.181 MB / 0.7588 GB, free: 11.39 MB / 0.6042 GB Notification: Performance of [SIM] Simplify 2: time 0.0003037/0.4989, allocations: 288.9 kB / 0.759 GB, free: 11.18 MB / 0.6042 GB Notification: Performance of [SIM] Remove Stream: time 0.0002163/0.4991, allocations: 261.4 kB / 0.7593 GB, free: 10.96 MB / 0.6042 GB Notification: Performance of [SIM] Detect States: time 0.0008643/0.5, allocations: 0.8384 MB / 0.7601 GB, free: 10.21 MB / 0.6042 GB Notification: Performance of [SIM] Events: time 0.0002108/0.5002, allocations: 187.4 kB / 0.7603 GB, free: 10.03 MB / 0.6042 GB Notification: Performance of [SIM] Partitioning: time 0.001037/0.5012, allocations: 1.129 MB / 0.7614 GB, free: 8.828 MB / 0.6042 GB Error: Internal error NBSorting.tarjan failed to sort system: System Variables (232/240) **************************** (1|1) [DSTA] (1) Real T_out2.h_in = ThermofluidStream.Idealized.Tests.Processes.Isochoric.Warnings2.T_out2.Medium.specificEnthalpy(T_out2.inlet.state) (start = 298609.6803431054, min = -1e10, max = 1e10, nominal = 1e5) (2|2) [DSTA] (1) Real dT2c.p_out (start = 1e6, min = 0.0, max = 1e8, nominal = 1e6) (3|3) [DSTA] (1) output Real source3.outlet.state.p (start = 1e6, min = 0.0, max = 1e8, nominal = 1e6) (4|4) [DSTA] (1) output Real source2.outlet.state.p (start = 1e6, min = 0.0, max = 1e8, nominal = 1e6) (5|5) [ALGB] (1) Real T_out2.P_out = -(-T_out2.P_out) (6|6) [DSTA] (1) output Real source1.outlet.state.p (start = 1e6, min = 0.0, max = 1e8, nominal = 1e6) (7|7) [ALGB] (1) output Real T_out2.outlet.state.T (start = 500.0, min = 200.0, max = 6000.0, nominal = 500.0) (8|8) [ALGB] (1) Real T_out2.dT = T_in + dT - T_out2.T_in (9|9) [DSTA] (1) Real dT2c.T_in = ThermofluidStream.Idealized.Tests.Processes.Isochoric.Warnings2.dT2c.Medium.temperature(dT2c.inlet.state) (start = 500.0, min = 200.0, max = 6000.0, nominal = 500.0) (10|10) [DDER] (1) Real $DER.dT2c.m_flow (StateSelect = avoid) (11|11) [ALGB] (1) Real sink3.r (12|12) [ALGB] (1) Real sink2.r (13|13) [ALGB] (1) Real sink1.r (14|14) [ALGB] (1) Real dT2c.dp (start = dT2c.dp_start) (15|15) [DSTA] (1) Real $FUN_9.p (16|16) [DSTA] (1) Real $FUN_8.p (17|17) [DSTA] (1) input Real dT2.inlet.state.T (start = 500.0, min = 200.0, max = 6000.0, nominal = 500.0) (18|18) [ALGB] (1) Real $FUN_7.p (19|19) [DSTA] (1) Real $FUN_2.p (20|20) [DSTA] (1) Real $FUN_1.p (21|21) [DDER] (1) Real $DER.T_out2.m_flow (StateSelect = avoid) (22|22) [ALGB] (1) Real $FUN_28.T (23|23) [ALGB] (1) Real source.outlet.r (24|24) [ALGB] (1) Real dT2.w_p = (dT2.p_out - dT2.p_in) / dT2.rho (25|25) [DSTA] (1) Real $FUN_23.T (26|26) [DSTA] (1) Real $FUN_22.T (27|27) [ALGB] (1) Real $FUN_21.T (28|28) [DSTA] (1) output Real source3.outlet.state.T (start = 500.0, min = 200.0, max = 6000.0, nominal = 500.0) (29|29) [DSTA] (1) Real dT2c.u_in = dT2c.h_in - dT2c.p_in / dT2c.rho (min = -1e8, max = 1e8, nominal = 1e6) (30|30) [DSTA] (1) output Real source2.outlet.state.T (start = 500.0, min = 200.0, max = 6000.0, nominal = 500.0) (31|31) [DSTA] (1) output Real source1.outlet.state.T (start = 500.0, min = 200.0, max = 6000.0, nominal = 500.0) (32|32) [ALGB] (1) output Real dT2c.outlet.state.T (start = 500.0, min = 200.0, max = 6000.0, nominal = 500.0) (33|33) [DSTA] (1) Real T_out2c.p_out (start = 1e6, min = 0.0, max = 1e8, nominal = 1e6) (34|34) [ALGB] (1) input Real sink.inlet.state.T (start = 500.0, min = 200.0, max = 6000.0, nominal = 500.0) (35|35) [ALGB] (1) Real T_out2c.T_in = ThermofluidStream.Idealized.Tests.Processes.Isochoric.Warnings2.T_out2c.Medium.temperature(T_out2c.inlet.state) (start = 500.0, min = 200.0, max = 6000.0, nominal = 500.0) (36|36) [DSTA] (1) output Real source.outlet.state.p (start = 1e6, min = 0.0, max = 1e8, nominal = 1e6) (37|37) [DSTA] (1) Real dT2.h_out (start = 298609.6803431054, min = -1e10, max = 1e10, nominal = 1e5) (38|38) [DSTA] (1) Real T_out2c.p_in = ThermofluidStream.Idealized.Tests.Processes.Isochoric.Warnings2.T_out2c.Medium.pressure(T_out2c.inlet.state) (start = 1e6, min = 0.0, max = 1e8, nominal = 1e6) (39|39) [DISS] (1) protected Integer temperatureDifference.count (40|40) [ALGB] (1) Real dT2c.outlet.r (41|41) [ALGB] (1) input Real sink.inlet.state.p (start = 1e6, min = 0.0, max = 1e8, nominal = 1e6) (42|42) [ALGB] (1) Real T_out2.singularityRegime (43|43) [DSTA] (1) Real dT2c.p_in = ThermofluidStream.Idealized.Tests.Processes.Isochoric.Warnings2.dT2c.Medium.pressure(dT2c.inlet.state) (start = 1e6, min = 0.0, max = 1e8, nominal = 1e6) (44|44) [DSTA] (1) Real $FUN_16.T (45|45) [ALGB] (1) Real $FUN_6 (46|46) [DSTA] (1) input Real T_out2c.inlet.state.T (start = 500.0, min = 200.0, max = 6000.0, nominal = 500.0) (47|47) [DSTA] (1) Real $FUN_15.T (48|48) [ALGB] (1) Real $FUN_5 (49|49) [ALGB] (1) Real $FUN_14.T (50|50) [DSTA] (1) Real dT2c.T_out (start = 500.0, min = 200.0, max = 6000.0, nominal = 500.0) (51|51) [ALGB] (1) Real $FUN_27 (52|52) [ALGB] (1) Real $FUN_26 (53|53) [DSTA] (1) input Real dT2.inlet.state.p (start = 1e6, min = 0.0, max = 1e8, nominal = 1e6) (54|54) [ALGB] (1) Real source1.outlet.r (55|55) [ALGB] (1) Real dT2.P_out = -(-dT2.P_out) (56|56) [ALGB] (1) Real $FUN_20 (57|57) [ALGB] (1) Real source2.outlet.r (58|58) [ALGB] (1) Real source3.outlet.r (59|59) [DSTA] (1) Real T_out2.h_out (start = 298609.6803431054, min = -1e10, max = 1e10, nominal = 1e5) (60|60) [DSTA] (1) Real dT2.T_in = ThermofluidStream.Idealized.Tests.Processes.Isochoric.Warnings2.dT2.Medium.temperature(dT2.inlet.state) (start = 500.0, min = 200.0, max = 6000.0, nominal = 500.0) (61|61) [DISS] (1) protected Integer heatFlowRate.count (62|62) [DSTA] (1) input Real T_out2c.inlet.state.p (start = 1e6, min = 0.0, max = 1e8, nominal = 1e6) (63|63) [ALGB] (1) Real T_out2c.singularityRegime (64|64) [ALGB] (1) Real $FUN_28.p (65|65) [ALGB] (1) Real T_out2c.dT = T_in + dT - T_out2c.T_in (66|66) [ALGB] (1) output Real dT2.outlet.state.T (start = 500.0, min = 200.0, max = 6000.0, nominal = 500.0) (67|67) [DSTA] (1) Real $FUN_23.p (68|68) [DSTA] (1) Real $FUN_22.p (69|69) [ALGB] (1) Real $FUN_21.p (70|70) [DSTA] (1) Real T_out2.u_out = T_out2.h_out - T_out2.p_out / T_out2.rho (min = -1e8, max = 1e8, nominal = 1e6) (71|71) [ALGB] (1) Real $FUN_19 (72|72) [DSTA] (1) input Real dT2c.inlet.state.T (start = 500.0, min = 200.0, max = 6000.0, nominal = 500.0) (73|73) [ALGB] (1) output Real T_out2c.outlet.state.p (start = 1e6, min = 0.0, max = 1e8, nominal = 1e6) (74|74) [ALGB] (1) Real $FUN_13 (75|75) [ALGB] (1) Real $FUN_12 (76|76) [DSTA] (1) Real T_out2.rho = ThermofluidStream.Idealized.Tests.Processes.Isochoric.Warnings2.T_out2.Medium.density(T_out2.inlet.state) (start = 10.0, min = 0.0, max = 1e5, nominal = 10.0) (77|77) [ALGB] (1) output Real dT2.outlet.state.p (start = 1e6, min = 0.0, max = 1e8, nominal = 1e6) (78|78) [DSTA] (1) Real dT2.h_in = ThermofluidStream.Idealized.Tests.Processes.Isochoric.Warnings2.dT2.Medium.specificEnthalpy(dT2.inlet.state) (start = 298609.6803431054, min = -1e10, max = 1e10, nominal = 1e5) (79|79) [ALGB] (1) input Real sink3.inlet.state.T (start = 500.0, min = 200.0, max = 6000.0, nominal = 500.0) (80|80) [ALGB] (1) input Real sink2.inlet.state.T (start = 500.0, min = 200.0, max = 6000.0, nominal = 500.0) (81|81) [ALGB] (1) input Real sink1.inlet.state.T (start = 500.0, min = 200.0, max = 6000.0, nominal = 500.0) (82|82) [DISC] (1) Boolean $SEV_9 (83|83) [DISC] (1) Boolean $SEV_8 (84|84) [DSTA] (1) input Real dT2c.inlet.state.p (start = 1e6, min = 0.0, max = 1e8, nominal = 1e6) (85|85) [DISC] (1) Boolean $SEV_7 (86|86) [DISC] (1) Boolean $SEV_6 (87|87) [DISC] (1) Boolean $SEV_5 (88|88) [DISC] (1) Boolean $SEV_4 (89|89) [ALGB] (1) Real dT2c.w_p = (dT2c.p_out - dT2c.p_in) / dT2c.rho (90|90) [DISC] (1) Boolean $SEV_3 (91|91) [DSTA] (1) Real T_out2c.rho = ThermofluidStream.Idealized.Tests.Processes.Isochoric.Warnings2.T_out2c.Medium.density(T_out2c.inlet.state) (start = 10.0, min = 0.0, max = 1e5, nominal = 10.0) (92|92) [DISC] (1) Boolean $SEV_2 (93|93) [ALGB] (1) Real dT2c.singularityRegime (94|94) [DISC] (1) Boolean $SEV_1 (95|95) [DISC] (1) Boolean $SEV_0 (96|96) [DSTA] (1) Real $FUN_16.p (97|97) [DSTA] (1) Real $FUN_15.p (98|98) [DSTA] (1) Real T_out2c.du = T_out2c.u_out - T_out2c.u_in (min = -1e8, max = 1e8, nominal = 1e6) (99|99) [ALGB] (1) Real $FUN_14.p (100|100) [DDER] (1) Real $DER.dT2.m_flow (StateSelect = avoid) (101|101) [DSTA] (1) Real $FUN_9.T (102|102) [DSTA] (1) Real $FUN_8.T (103|103) [ALGB] (1) Real $FUN_7.T (104|104) [DISS] (1) protected Real heatFlowRate.T_start (105|105) [DSTA] (1) Real $FUN_2.T (106|106) [DSTA] (1) Real $FUN_1.T (107|107) [DSTA] (1) Real dT2c.Q_flow (108|108) [DSTA] (1) Real dT = dT (min = max(200.0 - T_in, 200.0 - T_in, 200.0 - T_in), max = max(6000.0 - T_in, 6000.0 - T_in, 6000.0 - T_in)) (109|109) [DSTA] (1) output Real source.outlet.state.T (start = 500.0, min = 200.0, max = 6000.0, nominal = 500.0) (110|110) [DSTA] (1) input Real T_out2.inlet.state.p (start = 1e6, min = 0.0, max = 1e8, nominal = 1e6) (111|111) [ALGB] (1) Real T_out2.dp (start = T_out2.dp_start) (112|112) [ALGB] (1) Real dT2.singularityRegime (113|113) [ALGB] (1) Real dT2.outlet.r (114|114) [ALGB] (1) output Real T_out2c.outlet.state.T (start = 500.0, min = 200.0, max = 6000.0, nominal = 500.0) (115|115) [DSTA] (1) Real T_out2.du = T_out2.u_out - T_out2.u_in (min = -1e8, max = 1e8, nominal = 1e6) (116|116) [ALGB] (1) output Real dT2c.outlet.state.p (start = 1e6, min = 0.0, max = 1e8, nominal = 1e6) (117|117) [ALGB] (1) Real T_out2c.dp (start = T_out2c.dp_start) (118|118) [DSTA] (1) Real dT2.T_out (start = 500.0, min = 200.0, max = 6000.0, nominal = 500.0) (119|119) [DSTA] (1) Real dT2c.h_in = ThermofluidStream.Idealized.Tests.Processes.Isochoric.Warnings2.dT2c.Medium.specificEnthalpy(dT2c.inlet.state) (start = 298609.6803431054, min = -1e10, max = 1e10, nominal = 1e5) (120|120) [DSTA] (1) Real T_out2c.u_out = T_out2c.h_out - T_out2c.p_out / T_out2c.rho (min = -1e8, max = 1e8, nominal = 1e6) (121|121) [DSTA] (1) Real dT2.du = dT2.u_out - dT2.u_in (min = -1e8, max = 1e8, nominal = 1e6) (122|122) [DSTA] (1) Real dT2.rho = ThermofluidStream.Idealized.Tests.Processes.Isochoric.Warnings2.dT2.Medium.density(dT2.inlet.state) (start = 10.0, min = 0.0, max = 1e5, nominal = 10.0) (123|123) [DSTA] (1) Real dT2c.u_out = dT2c.h_out - dT2c.p_out / dT2c.rho (min = -1e8, max = 1e8, nominal = 1e6) (124|124) [ALGB] (1) Real T_out2.T_in = ThermofluidStream.Idealized.Tests.Processes.Isochoric.Warnings2.T_out2.Medium.temperature(T_out2.inlet.state) (start = 500.0, min = 200.0, max = 6000.0, nominal = 500.0) (125|125) [DSTA] (1) Real dT2c.du = dT2c.u_out - dT2c.u_in (min = -1e8, max = 1e8, nominal = 1e6) (126|126) [DSTA] (1) Real T_out2c.h_out (start = 298609.6803431054, min = -1e10, max = 1e10, nominal = 1e5) (127|127) [ALGB] (1) Real T_out2.w_p = (T_out2.p_out - T_out2.p_in) / T_out2.rho (128|128) [ALGB] (1) Real T_out2c.w_p = (T_out2c.p_out - T_out2c.p_in) / T_out2c.rho (129|129) [ALGB] (1) Real T_out2.outlet.r (130|130) [DSTA] (1) input Real T_out2.inlet.state.T (start = 500.0, min = 200.0, max = 6000.0, nominal = 500.0) (131|131) [DSTA] (1) Real T_out2.u_in = T_out2.h_in - T_out2.p_in / T_out2.rho (min = -1e8, max = 1e8, nominal = 1e6) (132|132) [DSTA] (1) Real T_out2.p_out (start = 1e6, min = 0.0, max = 1e8, nominal = 1e6) (133|133) [DSTA] (1) Real dT2.u_out = dT2.h_out - dT2.p_out / dT2.rho (min = -1e8, max = 1e8, nominal = 1e6) (134|134) [ALGB] (1) output Real T_out2.outlet.state.p (start = 1e6, min = 0.0, max = 1e8, nominal = 1e6) (135|135) [DSTA] (1) Real dT2c.rho = ThermofluidStream.Idealized.Tests.Processes.Isochoric.Warnings2.dT2c.Medium.density(dT2c.inlet.state) (start = 10.0, min = 0.0, max = 1e5, nominal = 10.0) (136|136) [DSTA] (1) Real T_out2c.h_in = ThermofluidStream.Idealized.Tests.Processes.Isochoric.Warnings2.T_out2c.Medium.specificEnthalpy(T_out2c.inlet.state) (start = 298609.6803431054, min = -1e10, max = 1e10, nominal = 1e5) (137|137) [ALGB] (1) Real dT2.dp (start = dT2.dp_start) (138|138) [DISS] (1) protected Real temperatureDifference.T_start (139|139) [DDER] (1) Real $DER.T_out2c.m_flow (StateSelect = avoid) (140|140) [ALGB] (1) Real sink.r (141|141) [DSTA] (1) Real dT2.p_out (start = 1e6, min = 0.0, max = 1e8, nominal = 1e6) (142|142) [ALGB] (1) Real T_out2c.outlet.r (143|143) [ALGB] (1) input Real sink3.inlet.state.p (start = 1e6, min = 0.0, max = 1e8, nominal = 1e6) (144|144) [ALGB] (1) input Real sink2.inlet.state.p (start = 1e6, min = 0.0, max = 1e8, nominal = 1e6) (145|145) [DSTA] (1) Real T_out2c.u_in = T_out2c.h_in - T_out2c.p_in / T_out2c.rho (min = -1e8, max = 1e8, nominal = 1e6) (146|146) [ALGB] (1) input Real sink1.inlet.state.p (start = 1e6, min = 0.0, max = 1e8, nominal = 1e6) (147|147) [DSTA] (1) Real T_out2.p_in = ThermofluidStream.Idealized.Tests.Processes.Isochoric.Warnings2.T_out2.Medium.pressure(T_out2.inlet.state) (start = 1e6, min = 0.0, max = 1e8, nominal = 1e6) (148|148) [DSTA] (1) Real dT2.p_in = ThermofluidStream.Idealized.Tests.Processes.Isochoric.Warnings2.dT2.Medium.pressure(dT2.inlet.state) (start = 1e6, min = 0.0, max = 1e8, nominal = 1e6) (149|149) [DSTA] (1) Real dT2c.h_out (start = 298609.6803431054, min = -1e10, max = 1e10, nominal = 1e5) (150|150) [DSTA] (1) Real dT2.u_in = dT2.h_in - dT2.p_in / dT2.rho (min = -1e8, max = 1e8, nominal = 1e6) (151|151) [DER-] (2) source.Medium.ThermodynamicState $DER.$FUN_1 (152|153) [DER-] (2) source.outlet.Medium.ThermodynamicState $DER.source.outlet.state (153|155) [DDER] (1) Real $DER.T_out2.u_in (StateSelect = avoid) (154|156) [DDER] (1) output Real $DER.source2.outlet.state.T (StateSelect = avoid) (155|157) [DDER] (1) output Real $DER.source.outlet.state.p (StateSelect = avoid) (156|158) [DDER] (1) output Real $DER.source2.outlet.state.p (StateSelect = avoid) (157|159) [DDER] (1) Real $DER.T_out2.u_out (StateSelect = avoid) (158|160) [DDER] (1) input Real $DER.T_out2c.inlet.state.T (StateSelect = avoid) (159|161) [DDER] (1) output Real $DER.source.outlet.state.T (StateSelect = avoid) (160|162) [DDER] (1) input Real $DER.dT2c.inlet.state.T (StateSelect = avoid) (161|163) [DDER] (1) input Real $DER.dT2c.inlet.state.p (StateSelect = avoid) (162|164) [DDER] (1) Real $DER.T_out2.p_in (StateSelect = avoid) (163|165) [DDER] (1) input Real $DER.T_out2c.inlet.state.p (StateSelect = avoid) (164|166) [DDER] (1) Real $DER.T_out2.h_in (StateSelect = avoid) (165|167) [DDER] (1) Real $DER.T_out2.du (StateSelect = avoid) (166|168) [DER-] (2) source3.Medium.ThermodynamicState $DER.$FUN_22 (167|170) [DER-] (2) source3.outlet.Medium.ThermodynamicState $DER.source3.outlet.state (168|172) [DDER] (1) Real $DER.$FUN_1.p (StateSelect = avoid) (169|173) [DDER] (1) Real $DER.T_out2.p_out (StateSelect = avoid) (170|174) [DDER] (1) Real $DER.T_out2.h_out (StateSelect = avoid) (171|175) [DDER] (1) Real $DER.$FUN_1.T (StateSelect = avoid) (172|176) [DDER] (1) Real $DER.$FUN_8.p (StateSelect = avoid) (173|177) [DDER] (1) Real $DER.$FUN_8.T (StateSelect = avoid) (174|178) [DDER] (1) Real $DER.$FUN_9.p (StateSelect = avoid) (175|179) [DDER] (1) Real $DER.$FUN_9.T (StateSelect = avoid) (176|180) [DDER] (1) Real $DER.$FUN_15.p (StateSelect = avoid) (177|181) [DDER] (1) Real $DER.$FUN_15.T (StateSelect = avoid) (178|182) [DDER] (1) Real $DER.$FUN_16.p (StateSelect = avoid) (179|183) [DDER] (1) Real $DER.$FUN_16.T (StateSelect = avoid) (180|184) [DER-] (2) source1.Medium.ThermodynamicState $DER.$FUN_15 (181|186) [DER-] (2) source1.outlet.Medium.ThermodynamicState $DER.source1.outlet.state (182|188) [DDER] (1) Real $DER.$FUN_22.p (StateSelect = avoid) (183|189) [DDER] (1) Real $DER.$FUN_22.T (StateSelect = avoid) (184|190) [DDER] (1) Real $DER.T_out2.rho (StateSelect = avoid) (185|191) [DDER] (1) Real $DER.$FUN_23.p (StateSelect = avoid) (186|192) [DDER] (1) Real $DER.$FUN_2.p (StateSelect = avoid) (187|193) [DDER] (1) Real $DER.$FUN_2.T (StateSelect = avoid) (188|194) [DDER] (1) Real $DER.$FUN_23.T (StateSelect = avoid) (189|195) [DDER] (1) Real $DER.dT2c.T_in (StateSelect = avoid) (190|196) [DDER] (1) Real $DER.dT2c.T_out (StateSelect = avoid) (191|197) [DDER] (1) Real $DER.dT2c.p_in (StateSelect = avoid) (192|198) [DDER] (1) Real $DER.dT2c.h_in (StateSelect = avoid) (193|199) [DDER] (1) Real $DER.dT2c.u_in (StateSelect = avoid) (194|200) [DDER] (1) Real $DER.dT2c.rho (StateSelect = avoid) (195|201) [DDER] (1) Real $DER.dT2c.p_out (StateSelect = avoid) (196|202) [DDER] (1) Real $DER.dT2c.h_out (StateSelect = avoid) (197|203) [DDER] (1) Real $DER.dT2c.u_out (StateSelect = avoid) (198|204) [DER-] (2) source2.Medium.ThermodynamicState $DER.$FUN_8 (199|206) [DER-] (2) source2.outlet.Medium.ThermodynamicState $DER.source2.outlet.state (200|208) [DDER] (1) Real $DER.T_out2c.du (StateSelect = avoid) (201|209) [DDER] (1) Real $DER.T_out2c.p_in (StateSelect = avoid) (202|210) [DDER] (1) Real $DER.T_out2c.h_in (StateSelect = avoid) (203|211) [DDER] (1) Real $DER.T_out2c.u_in (StateSelect = avoid) (204|212) [DDER] (1) Real $DER.T_out2c.rho (StateSelect = avoid) (205|213) [DDER] (1) Real $DER.T_out2c.p_out (StateSelect = avoid) (206|214) [DDER] (1) Real $DER.T_out2c.h_out (StateSelect = avoid) (207|215) [DDER] (1) Real $DER.T_out2c.u_out (StateSelect = avoid) (208|216) [DDER] (1) input Real $DER.T_out2.inlet.state.T (StateSelect = avoid) (209|217) [DDER] (1) output Real $DER.source3.outlet.state.T (StateSelect = avoid) (210|218) [DDER] (1) input Real $DER.T_out2.inlet.state.p (StateSelect = avoid) (211|219) [DDER] (1) output Real $DER.source3.outlet.state.p (StateSelect = avoid) (212|220) [DDER] (1) Real $DER.dT2.T_in (StateSelect = avoid) (213|221) [DDER] (1) Real $DER.dT2.T_out (StateSelect = avoid) (214|222) [DDER] (1) Real $DER.dT (StateSelect = avoid) (215|223) [DDER] (1) Real $DER.dT2c.Q_flow (StateSelect = avoid) (216|224) [DDER] (1) Real $DER.dT2c.du (StateSelect = avoid) (217|225) [DDER] (1) Real $DER.dT2.du (StateSelect = avoid) (218|226) [DDER] (1) input Real $DER.dT2.inlet.state.T (StateSelect = avoid) (219|227) [DDER] (1) output Real $DER.source1.outlet.state.T (StateSelect = avoid) (220|228) [DDER] (1) Real $DER.dT2.p_in (StateSelect = avoid) (221|229) [DDER] (1) Real $DER.dT2.h_in (StateSelect = avoid) (222|230) [DDER] (1) Real $DER.dT2.u_in (StateSelect = avoid) (223|231) [DDER] (1) input Real $DER.dT2.inlet.state.p (StateSelect = avoid) (224|232) [DDER] (1) output Real $DER.source1.outlet.state.p (StateSelect = avoid) (225|233) [DDER] (1) Real $DER.dT2.rho (StateSelect = avoid) (226|234) [DDER] (1) Real $DER.dT2.p_out (StateSelect = avoid) (227|235) [DDER] (1) Real $DER.dT2.h_out (StateSelect = avoid) (228|236) [DDER] (1) Real $DER.dT2.u_out (StateSelect = avoid) (229|237) [DSTA] (1) Real dT2.m_flow = dT2.m_flow (StateSelect = default) (230|238) [DSTA] (1) Real T_out2.m_flow = T_out2.m_flow (StateSelect = default) (231|239) [DSTA] (1) Real dT2c.m_flow = dT2c.m_flow (StateSelect = default) (232|240) [DSTA] (1) Real T_out2c.m_flow = T_out2c.m_flow (StateSelect = default) System Equations (212/224) **************************** (1|1) [SCAL] (1) T_out2.du = T_out2.u_out - T_out2.u_in ($RES_BND_170) (2|2) [WHEN] (1) ($RES_SIM_80) (2|2) [----] when $SEV_0 then (2|2) [----] temperatureDifference.count := 1 + $PRE.temperatureDifference.count (2|2) [----] end when; (3|3) [SCAL] (1) T_out2.u_in = T_out2.h_in - T_out2.p_in / T_out2.rho ($RES_BND_171) (4|4) [SCAL] (1) source.outlet.state.p = dT2c.inlet.state.p ($RES_SIM_120) (5|5) [SCAL] (1) T_out2.u_out = T_out2.h_out - T_out2.p_out / T_out2.rho ($RES_BND_172) (6|6) [SCAL] (1) T_out2.w_p = (T_out2.p_out - T_out2.p_in) / T_out2.rho ($RES_BND_173) (7|7) [SCAL] (1) T_out2c.h_in = ThermofluidStream.Media.myMedia.IdealGases.Common.Functions.h_T(ThermofluidStream.Media.myMedia.IdealGases.Common.DataRecord(\"Air\", 0.0289651159, -4333.833858403446, 298609.6803431054, 1000.0, {10099.5016, -196.827561, 5.00915511, -0.00576101373, 1.06685993e-5, -7.94029797e-9, 2.18523191e-12}, {-176.796731, -3.921504225}, {241521.443, -1257.8746, 5.14455867, -2.13854179e-4, 7.06522784e-8, -1.07148349e-11, 6.57780015e-16}, {6462.26319, -8.147411905}, 287.0512249529787), T_out2c.inlet.state.T, true, ThermofluidStream.Media.myMedia.Interfaces.Choices.ReferenceEnthalpy.ZeroAt0K, 0.0) ($RES_AUX_180) (8|8) [SCAL] (1) T_out2c.T_in = T_out2c.inlet.state.T ($RES_AUX_181) (9|9) [SCAL] (1) T_out2c.rho = (0.0034836987724536205 * T_out2c.inlet.state.p) / T_out2c.inlet.state.T ($RES_AUX_182) (10|10) [SCAL] (1) dT2.p_in = dT2.inlet.state.p ($RES_AUX_183) (11|11) [SCAL] (1) dT2.h_in = ThermofluidStream.Media.myMedia.IdealGases.Common.Functions.h_T(ThermofluidStream.Media.myMedia.IdealGases.Common.DataRecord(\"Air\", 0.0289651159, -4333.833858403446, 298609.6803431054, 1000.0, {10099.5016, -196.827561, 5.00915511, -0.00576101373, 1.06685993e-5, -7.94029797e-9, 2.18523191e-12}, {-176.796731, -3.921504225}, {241521.443, -1257.8746, 5.14455867, -2.13854179e-4, 7.06522784e-8, -1.07148349e-11, 6.57780015e-16}, {6462.26319, -8.147411905}, 287.0512249529787), dT2.inlet.state.T, true, ThermofluidStream.Media.myMedia.Interfaces.Choices.ReferenceEnthalpy.ZeroAt0K, 0.0) ($RES_AUX_184) (12|12) [SCAL] (1) dT2.T_in = dT2.inlet.state.T ($RES_AUX_185) (13|13) [SCAL] (1) dT2.rho = (0.0034836987724536205 * dT2.inlet.state.p) / dT2.inlet.state.T ($RES_AUX_186) (14|14) [SCAL] (1) T_out2.p_in = T_out2.inlet.state.p ($RES_AUX_187) (15|15) [SCAL] (1) T_out2.h_in = ThermofluidStream.Media.myMedia.IdealGases.Common.Functions.h_T(ThermofluidStream.Media.myMedia.IdealGases.Common.DataRecord(\"Air\", 0.0289651159, -4333.833858403446, 298609.6803431054, 1000.0, {10099.5016, -196.827561, 5.00915511, -0.00576101373, 1.06685993e-5, -7.94029797e-9, 2.18523191e-12}, {-176.796731, -3.921504225}, {241521.443, -1257.8746, 5.14455867, -2.13854179e-4, 7.06522784e-8, -1.07148349e-11, 6.57780015e-16}, {6462.26319, -8.147411905}, 287.0512249529787), T_out2.inlet.state.T, true, ThermofluidStream.Media.myMedia.Interfaces.Choices.ReferenceEnthalpy.ZeroAt0K, 0.0) ($RES_AUX_188) (16|16) [SCAL] (1) T_out2.T_in = T_out2.inlet.state.T ($RES_AUX_189) (17|17) [SCAL] (1) -T_out2.P_out = T_out2.m_flow * T_out2.w_p ($RES_SIM_10) (18|18) [SCAL] (1) T_out2.singularityRegime = if noEvent($FUN_26 > 2.220446049250313e-16 and $FUN_27 < 2.220446049250313e-16) then -1.0 else 0.0 ($RES_SIM_11) (19|19) [SCAL] (1) T_out2.m_flow = (T_out2.du * dT2c.Q_flow) / (4.930380657631324e-32 + T_out2.du ^ 2.0) ($RES_SIM_13) (20|20) [SCAL] (1) $DER.T_out2.m_flow * sink3.L = T_out2.outlet.r - sink3.r ($RES_SIM_17) (21|21) [RECD] (2) source3.outlet.state = $FUN_22 ($RES_SIM_18) (22|23) [SCAL] (1) source3.L * (-$DER.T_out2.m_flow) = source3.outlet.r ($RES_SIM_19) (23|24) [SCAL] (1) $FUN_1.p = source.p0_par ($RES_SIM_219) (24|25) [SCAL] (1) T_out2.outlet.state.T = sink3.inlet.state.T ($RES_SIM_98) (25|26) [SCAL] (1) T_out2.outlet.state.p = sink3.inlet.state.p ($RES_SIM_99) (26|27) [SCAL] (1) T_out2.rho = (0.0034836987724536205 * T_out2.inlet.state.p) / T_out2.inlet.state.T ($RES_AUX_190) (27|28) [SCAL] (1) $FUN_27 = abs(T_out2.du) ($RES_AUX_192) (28|29) [SCAL] (1) $FUN_26 = abs(dT2c.Q_flow) ($RES_AUX_193) (29|30) [SCAL] (1) T_out2.p_out = $FUN_23.p ($RES_AUX_194) (30|31) [SCAL] (1) T_out2.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), $FUN_23.T, true, ThermofluidStream.Media.myMedia.Interfaces.Choices.ReferenceEnthalpy.ZeroAt0K, 0.0) ($RES_AUX_195) (31|32) [SCAL] (1) $FUN_20 = abs(dT2.du) ($RES_AUX_199) (32|33) [SCAL] (1) $FUN_1.T = source.T0_par ($RES_SIM_220) (33|34) [SCAL] (1) $FUN_2.p = 287.0512249529787 * dT2c.rho * dT2c.T_out ($RES_SIM_221) (34|35) [RECD] (2) dT2.outlet.state = $FUN_21 ($RES_SIM_23) (35|37) [SCAL] (1) $FUN_2.T = dT2c.T_out ($RES_SIM_222) (36|38) [SCAL] (1) $FUN_7.p = dT2c.p_out ($RES_SIM_223) (37|39) [SCAL] (1) dT2.p_out = dT2.p_in + dT2.dp ($RES_SIM_25) (38|40) [SCAL] (1) $FUN_7.T = ThermofluidStream.Idealized.Tests.Processes.Isochoric.Warnings2.dT2c.Medium.T_h(dT2c.h_out) ($RES_SIM_224) (39|41) [SCAL] (1) dT2.outlet.r = source1.outlet.r - $DER.dT2.m_flow * dT2.L ($RES_SIM_26) (40|42) [SCAL] (1) $FUN_8.p = source2.p0_par ($RES_SIM_225) (41|43) [SCAL] (1) $FUN_8.T = source2.T0_par ($RES_SIM_226) (42|44) [SCAL] (1) -dT2.P_out = dT2.m_flow * dT2.w_p ($RES_SIM_28) (43|45) [SCAL] (1) $FUN_9.p = 287.0512249529787 * T_out2c.rho * (T_in + dT) ($RES_SIM_227) (44|46) [SCAL] (1) dT2.singularityRegime = if noEvent($FUN_19 > 2.220446049250313e-16 and $FUN_20 < 2.220446049250313e-16) then -1.0 else 0.0 ($RES_SIM_29) (45|47) [SCAL] (1) $FUN_19 = abs(dT2c.Q_flow) ($RES_AUX_200) (46|48) [SCAL] (1) $FUN_9.T = T_in + dT ($RES_SIM_228) (47|49) [SCAL] (1) dT2.p_out = $FUN_16.p ($RES_AUX_201) (48|50) [SCAL] (1) $FUN_14.p = T_out2c.p_out ($RES_SIM_229) (49|51) [SCAL] (1) dT2.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), $FUN_16.T, true, ThermofluidStream.Media.myMedia.Interfaces.Choices.ReferenceEnthalpy.ZeroAt0K, 0.0) ($RES_AUX_202) (50|52) [SCAL] (1) $FUN_13 = abs(T_out2c.du) ($RES_AUX_206) (51|53) [SCAL] (1) $FUN_12 = abs(dT2c.Q_flow) ($RES_AUX_207) (52|54) [SCAL] (1) T_out2c.p_out = $FUN_9.p ($RES_AUX_208) (53|55) [SCAL] (1) T_out2c.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), $FUN_9.T, true, ThermofluidStream.Media.myMedia.Interfaces.Choices.ReferenceEnthalpy.ZeroAt0K, 0.0) ($RES_AUX_209) (54|56) [SCAL] (1) dT2.m_flow = (dT2.du * dT2c.Q_flow) / (4.930380657631324e-32 + dT2.du ^ 2.0) ($RES_SIM_31) (55|57) [SCAL] (1) $FUN_14.T = ThermofluidStream.Idealized.Tests.Processes.Isochoric.Warnings2.T_out2c.Medium.T_h(T_out2c.h_out) ($RES_SIM_230) (56|58) [SCAL] (1) $FUN_15.p = source1.p0_par ($RES_SIM_231) (57|59) [SCAL] (1) $FUN_15.T = source1.T0_par ($RES_SIM_232) (58|60) [SCAL] (1) $FUN_16.p = 287.0512249529787 * dT2.rho * dT2.T_out ($RES_SIM_233) (59|61) [SCAL] (1) $DER.dT2.m_flow * sink1.L = dT2.outlet.r - sink1.r ($RES_SIM_35) (60|62) [SCAL] (1) $FUN_16.T = dT2.T_out ($RES_SIM_234) (61|63) [RECD] (2) source1.outlet.state = $FUN_15 ($RES_SIM_36) (62|65) [SCAL] (1) $FUN_21.p = dT2.p_out ($RES_SIM_235) (63|66) [SCAL] (1) source1.L * (-$DER.dT2.m_flow) = source1.outlet.r ($RES_SIM_37) (64|67) [SCAL] (1) $FUN_21.T = ThermofluidStream.Idealized.Tests.Processes.Isochoric.Warnings2.dT2.Medium.T_h(dT2.h_out) ($RES_SIM_236) (65|68) [SCAL] (1) $FUN_22.p = source3.p0_par ($RES_SIM_237) (66|69) [SCAL] (1) $FUN_22.T = source3.T0_par ($RES_SIM_238) (67|70) [SCAL] (1) $FUN_23.p = 287.0512249529787 * T_out2.rho * (T_in + dT) ($RES_SIM_239) (68|71) [SCAL] (1) $FUN_6 = abs(dT2c.du) ($RES_AUX_213) (69|72) [SCAL] (1) $FUN_5 = abs(dT2c.Q_flow) ($RES_AUX_214) (70|73) [SCAL] (1) dT2c.p_out = $FUN_2.p ($RES_AUX_215) (71|74) [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_216) (72|75) [RECD] (2) T_out2c.outlet.state = $FUN_14 ($RES_SIM_41) (73|77) [SCAL] (1) $FUN_23.T = T_in + dT ($RES_SIM_240) (74|78) [SCAL] (1) T_out2c.p_out = T_out2c.p_in + T_out2c.dp ($RES_SIM_43) (75|79) [SCAL] (1) dT = dT2c.T_out - dT2c.T_in ($RES_BND_134) (76|80) [SCAL] (1) $FUN_28.p = T_out2.p_out ($RES_SIM_241) (77|81) [SCAL] (1) T_out2c.outlet.r = source2.outlet.r - $DER.T_out2c.m_flow * T_out2c.L ($RES_SIM_44) (78|82) [SCAL] (1) dT2c.du = dT2c.u_out - dT2c.u_in ($RES_BND_135) (79|83) [SCAL] (1) $FUN_28.T = ThermofluidStream.Idealized.Tests.Processes.Isochoric.Warnings2.T_out2.Medium.T_h(T_out2.h_out) ($RES_SIM_242) (80|84) [SCAL] (1) dT2c.u_in = dT2c.h_in - dT2c.p_in / dT2c.rho ($RES_BND_136) (81|85) [SCAL] (1) dT2c.u_out = dT2c.h_out - dT2c.p_out / dT2c.rho ($RES_BND_137) (82|86) [SCAL] (1) T_out2c.singularityRegime = if noEvent($FUN_12 > 2.220446049250313e-16 and $FUN_13 < 2.220446049250313e-16) then -1.0 else 0.0 ($RES_SIM_47) (83|87) [SCAL] (1) dT2c.w_p = (dT2c.p_out - dT2c.p_in) / dT2c.rho ($RES_BND_138) (84|88) [SCAL] (1) T_out2c.m_flow = (T_out2c.du * dT2c.Q_flow) / (4.930380657631324e-32 + T_out2c.du ^ 2.0) ($RES_SIM_49) (85|89) [SCAL] (1) $SEV_0 = time >= ((CAST(Real, 1 + $PRE.temperatureDifference.count)) * temperatureDifference.period + temperatureDifference.startTime) ($RES_EVT_251) (86|90) [SCAL] (1) $SEV_1 = (time < temperatureDifference.startTime or temperatureDifference.nperiod == 0) or temperatureDifference.nperiod > 0 and temperatureDifference.count >= temperatureDifference.nperiod ($RES_EVT_252) (87|91) [SCAL] (1) $SEV_2 = time < (temperatureDifference.T_start + temperatureDifference.T_rising) ($RES_EVT_253) (88|92) [SCAL] (1) $SEV_3 = time < (temperatureDifference.T_start + temperatureDifference.T_width) ($RES_EVT_254) (89|93) [SCAL] (1) $SEV_4 = time < (temperatureDifference.T_start + temperatureDifference.T_falling) ($RES_EVT_255) (90|94) [SCAL] (1) $SEV_5 = time >= ((CAST(Real, 1 + $PRE.heatFlowRate.count)) * heatFlowRate.period + heatFlowRate.startTime) ($RES_EVT_256) (91|95) [SCAL] (1) $SEV_6 = (time < heatFlowRate.startTime or heatFlowRate.nperiod == 0) or heatFlowRate.nperiod > 0 and heatFlowRate.count >= heatFlowRate.nperiod ($RES_EVT_257) (92|96) [SCAL] (1) $SEV_7 = time < (heatFlowRate.T_start + heatFlowRate.T_rising) ($RES_EVT_258) (93|97) [SCAL] (1) $SEV_8 = time < (heatFlowRate.T_start + heatFlowRate.T_width) ($RES_EVT_259) (94|98) [SCAL] (1) $DER.T_out2c.m_flow * sink2.L = T_out2c.outlet.r - sink2.r ($RES_SIM_53) (95|99) [RECD] (2) source2.outlet.state = $FUN_8 ($RES_SIM_54) (96|101) [SCAL] (1) T_out2c.dT = T_in + dT - T_out2c.T_in ($RES_BND_145) (97|102) [SCAL] (1) T_out2.outlet.r = source3.outlet.r - $DER.T_out2.m_flow * T_out2.L ($RES_SIM_8) (98|103) [SCAL] (1) source2.L * (-$DER.T_out2c.m_flow) = source2.outlet.r ($RES_SIM_55) (99|104) [SCAL] (1) T_out2c.du = T_out2c.u_out - T_out2c.u_in ($RES_BND_146) (100|105) [SCAL] (1) T_out2.p_out = T_out2.p_in + T_out2.dp ($RES_SIM_7) (101|106) [SCAL] (1) T_out2c.u_in = T_out2c.h_in - T_out2c.p_in / T_out2c.rho ($RES_BND_147) (102|107) [SCAL] (1) T_out2c.u_out = T_out2c.h_out - T_out2c.p_out / T_out2c.rho ($RES_BND_148) (103|108) [RECD] (2) T_out2.outlet.state = $FUN_28 ($RES_SIM_5) (104|110) [SCAL] (1) T_out2c.w_p = (T_out2c.p_out - T_out2c.p_in) / T_out2c.rho ($RES_BND_149) (105|111) [WHEN] (1) ($RES_SIM_4) (105|111) [----] when $SEV_5 then (105|111) [----] heatFlowRate.count := 1 + $PRE.heatFlowRate.count (105|111) [----] end when; (106|112) [RECD] (2) dT2c.outlet.state = $FUN_7 ($RES_SIM_59) (107|114) [WHEN] (1) ($RES_SIM_3) (107|114) [----] when $SEV_5 then (107|114) [----] heatFlowRate.T_start := time (107|114) [----] end when; (108|115) [SCAL] (1) dT2c.Q_flow = heatFlowRate.offset + (if $SEV_6 then 0.0 else if $SEV_7 then ((time - heatFlowRate.T_start) * heatFlowRate.amplitude) / heatFlowRate.rising else if $SEV_8 then heatFlowRate.amplitude else if $SEV_9 then (((heatFlowRate.T_falling + heatFlowRate.T_start) - time) * heatFlowRate.amplitude) / heatFlowRate.falling else 0.0) ($RES_SIM_2) (109|116) [SCAL] (1) $SEV_9 = time < (heatFlowRate.T_start + heatFlowRate.T_falling) ($RES_EVT_260) (110|117) [SCAL] (1) dT2c.p_out = dT2c.p_in + dT2c.dp ($RES_SIM_61) (111|118) [SCAL] (1) source3.outlet.state.T = T_out2.inlet.state.T ($RES_SIM_101) (112|119) [SCAL] (1) dT2c.outlet.r = source.outlet.r - $DER.dT2c.m_flow * dT2c.L ($RES_SIM_62) (113|120) [SCAL] (1) source3.outlet.state.p = T_out2.inlet.state.p ($RES_SIM_102) (114|121) [SCAL] (1) dT2.outlet.state.T = sink1.inlet.state.T ($RES_SIM_104) (115|122) [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_65) (116|123) [SCAL] (1) dT2.outlet.state.p = sink1.inlet.state.p ($RES_SIM_105) (117|124) [SCAL] (1) dT = dT2.T_out - dT2.T_in ($RES_BND_157) (118|125) [SCAL] (1) dT2c.m_flow = (dT2c.du * dT2c.Q_flow) / (4.930380657631324e-32 + dT2c.du ^ 2.0) ($RES_SIM_67) (119|126) [SCAL] (1) dT2.du = dT2.u_out - dT2.u_in ($RES_BND_158) (120|127) [SCAL] (1) source1.outlet.state.T = dT2.inlet.state.T ($RES_SIM_107) (121|128) [SCAL] (1) dT2.u_in = dT2.h_in - dT2.p_in / dT2.rho ($RES_BND_159) (122|129) [SCAL] (1) source1.outlet.state.p = dT2.inlet.state.p ($RES_SIM_108) (123|130) [SCAL] (1) dT2.u_out = dT2.h_out - dT2.p_out / dT2.rho ($RES_BND_160) (124|131) [SCAL] (1) dT2.w_p = (dT2.p_out - dT2.p_in) / dT2.rho ($RES_BND_161) (125|132) [SCAL] (1) T_out2c.outlet.state.T = sink2.inlet.state.T ($RES_SIM_110) (126|133) [SCAL] (1) $DER.dT2c.m_flow * sink.L = dT2c.outlet.r - sink.r ($RES_SIM_71) (127|134) [SCAL] (1) T_out2c.outlet.state.p = sink2.inlet.state.p ($RES_SIM_111) (128|135) [RECD] (2) source.outlet.state = $FUN_1 ($RES_SIM_72) (129|137) [SCAL] (1) source.L * (-$DER.dT2c.m_flow) = source.outlet.r ($RES_SIM_73) (130|138) [SCAL] (1) source2.outlet.state.T = T_out2c.inlet.state.T ($RES_SIM_113) (131|139) [SCAL] (1) source2.outlet.state.p = T_out2c.inlet.state.p ($RES_SIM_114) (132|140) [SCAL] (1) dT2c.outlet.state.T = sink.inlet.state.T ($RES_SIM_116) (133|141) [SCAL] (1) dT2c.outlet.state.p = sink.inlet.state.p ($RES_SIM_117) (134|142) [SCAL] (1) dT = temperatureDifference.offset + (if $SEV_1 then 0.0 else if $SEV_2 then ((time - temperatureDifference.T_start) * temperatureDifference.amplitude) / temperatureDifference.rising else if $SEV_3 then temperatureDifference.amplitude else if $SEV_4 then (((temperatureDifference.T_falling + temperatureDifference.T_start) - time) * temperatureDifference.amplitude) / temperatureDifference.falling else 0.0) ($RES_SIM_78) (135|143) [SCAL] (1) T_out2.dT = T_in + dT - T_out2.T_in ($RES_BND_169) (136|144) [WHEN] (1) ($RES_SIM_79) (136|144) [----] when $SEV_0 then (136|144) [----] temperatureDifference.T_start := time (136|144) [----] end when; (137|145) [SCAL] (1) source.outlet.state.T = dT2c.inlet.state.T ($RES_SIM_119) (138|146) [SCAL] (1) dT2c.p_in = dT2c.inlet.state.p ($RES_AUX_175) (139|147) [SCAL] (1) dT2c.h_in = ThermofluidStream.Media.myMedia.IdealGases.Common.Functions.h_T(ThermofluidStream.Media.myMedia.IdealGases.Common.DataRecord(\"Air\", 0.0289651159, -4333.833858403446, 298609.6803431054, 1000.0, {10099.5016, -196.827561, 5.00915511, -0.00576101373, 1.06685993e-5, -7.94029797e-9, 2.18523191e-12}, {-176.796731, -3.921504225}, {241521.443, -1257.8746, 5.14455867, -2.13854179e-4, 7.06522784e-8, -1.07148349e-11, 6.57780015e-16}, {6462.26319, -8.147411905}, 287.0512249529787), dT2c.inlet.state.T, true, ThermofluidStream.Media.myMedia.Interfaces.Choices.ReferenceEnthalpy.ZeroAt0K, 0.0) ($RES_AUX_176) (140|148) [SCAL] (1) dT2c.T_in = dT2c.inlet.state.T ($RES_AUX_177) (141|149) [SCAL] (1) dT2c.rho = (0.0034836987724536205 * dT2c.inlet.state.p) / dT2c.inlet.state.T ($RES_AUX_178) (142|150) [SCAL] (1) T_out2c.p_in = T_out2c.inlet.state.p ($RES_AUX_179) (143|151) [SCAL] (1) $DER.T_out2.du = $DER.T_out2.u_out - $DER.T_out2.u_in ($RES_SIM_261) (144|152) [RECD] (2) $DER.source.outlet.state = $DER.$FUN_1 ($RES_SIM_262) (145|154) [SCAL] (1) $DER.T_out2.u_in = $DER.T_out2.h_in - ($DER.T_out2.p_in * T_out2.rho - T_out2.p_in * $DER.T_out2.rho) / T_out2.rho ^ 2.0 ($RES_SIM_263) (146|155) [SCAL] (1) $DER.source2.outlet.state.T = $DER.T_out2c.inlet.state.T ($RES_SIM_264) (147|156) [SCAL] (1) $DER.source.outlet.state.p = $DER.dT2c.inlet.state.p ($RES_SIM_265) (148|157) [SCAL] (1) $DER.source2.outlet.state.p = $DER.T_out2c.inlet.state.p ($RES_SIM_266) (149|158) [SCAL] (1) $DER.T_out2.u_out = $DER.T_out2.h_out - ($DER.T_out2.p_out * T_out2.rho - T_out2.p_out * $DER.T_out2.rho) / T_out2.rho ^ 2.0 ($RES_SIM_267) (150|159) [SCAL] (1) $DER.dT = if $SEV_1 then 0.0 else if $SEV_2 then (temperatureDifference.amplitude * temperatureDifference.rising) / temperatureDifference.rising ^ 2.0 else if $SEV_3 then 0.0 else if $SEV_4 then -(temperatureDifference.amplitude * temperatureDifference.falling) / temperatureDifference.falling ^ 2.0 else 0.0 ($RES_SIM_268) (151|160) [SCAL] (1) $DER.T_out2c.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), T_out2c.inlet.state.T, true, ThermofluidStream.Media.myMedia.Interfaces.Choices.ReferenceEnthalpy.ZeroAt0K, 0.0, $DER.T_out2c.inlet.state.T, 0.0) ($RES_SIM_269) (152|161) [SCAL] (1) $DER.T_out2c.rho = ((0.0034836987724536205 * $DER.T_out2c.inlet.state.p) * T_out2c.inlet.state.T - 0.0034836987724536205 * $DER.T_out2c.inlet.state.T * T_out2c.inlet.state.p) / T_out2c.inlet.state.T ^ 2.0 ($RES_SIM_270) (153|162) [SCAL] (1) $DER.source.outlet.state.T = $DER.dT2c.inlet.state.T ($RES_SIM_271) (154|163) [SCAL] (1) $DER.dT2.p_in = $DER.dT2.inlet.state.p ($RES_SIM_272) (155|164) [SCAL] (1) $DER.dT2c.p_in = $DER.dT2c.inlet.state.p ($RES_SIM_273) (156|165) [SCAL] (1) $DER.dT2.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), dT2.inlet.state.T, true, ThermofluidStream.Media.myMedia.Interfaces.Choices.ReferenceEnthalpy.ZeroAt0K, 0.0, $DER.dT2.inlet.state.T, 0.0) ($RES_SIM_274) (157|166) [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_275) (158|167) [SCAL] (1) $DER.dT2.T_in = $DER.dT2.inlet.state.T ($RES_SIM_276) (159|168) [SCAL] (1) $DER.dT2c.T_in = $DER.dT2c.inlet.state.T ($RES_SIM_277) (160|169) [SCAL] (1) $DER.dT2.rho = ((0.0034836987724536205 * $DER.dT2.inlet.state.p) * dT2.inlet.state.T - 0.0034836987724536205 * $DER.dT2.inlet.state.T * dT2.inlet.state.p) / dT2.inlet.state.T ^ 2.0 ($RES_SIM_278) (161|170) [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_279) (162|171) [SCAL] (1) $DER.T_out2.p_in = $DER.T_out2.inlet.state.p ($RES_SIM_280) (163|172) [SCAL] (1) $DER.T_out2c.p_in = $DER.T_out2c.inlet.state.p ($RES_SIM_281) (164|173) [SCAL] (1) $DER.T_out2.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), T_out2.inlet.state.T, true, ThermofluidStream.Media.myMedia.Interfaces.Choices.ReferenceEnthalpy.ZeroAt0K, 0.0, $DER.T_out2.inlet.state.T, 0.0) ($RES_SIM_282) (165|174) [SCAL] (1) $DER.T_out2.m_flow = (($DER.T_out2.du * dT2c.Q_flow + T_out2.du * $DER.dT2c.Q_flow) * (4.930380657631324e-32 + T_out2.du ^ 2.0) - (2.0 * T_out2.du * $DER.T_out2.du) * T_out2.du * dT2c.Q_flow) / (4.930380657631324e-32 + T_out2.du ^ 2.0) ^ 2.0 ($RES_SIM_283) (166|175) [RECD] (2) $DER.source3.outlet.state = $DER.$FUN_22 ($RES_SIM_284) (167|177) [SCAL] (1) $DER.$FUN_1.p = 0.0 ($RES_SIM_285) (168|178) [SCAL] (1) $DER.T_out2.rho = ((0.0034836987724536205 * $DER.T_out2.inlet.state.p) * T_out2.inlet.state.T - 0.0034836987724536205 * $DER.T_out2.inlet.state.T * T_out2.inlet.state.p) / T_out2.inlet.state.T ^ 2.0 ($RES_SIM_286) (169|179) [SCAL] (1) $DER.T_out2.p_out = $DER.$FUN_23.p ($RES_SIM_287) (170|180) [SCAL] (1) $DER.T_out2.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_23.T, true, ThermofluidStream.Media.myMedia.Interfaces.Choices.ReferenceEnthalpy.ZeroAt0K, 0.0, $DER.$FUN_23.T, 0.0) ($RES_SIM_288) (171|181) [SCAL] (1) $DER.$FUN_1.T = 0.0 ($RES_SIM_289) (172|182) [SCAL] (1) $DER.$FUN_2.p = 287.0512249529787 * $DER.dT2c.rho * dT2c.T_out + 287.0512249529787 * dT2c.rho * $DER.dT2c.T_out ($RES_SIM_290) (173|183) [SCAL] (1) $DER.$FUN_2.T = $DER.dT2c.T_out ($RES_SIM_291) (174|184) [SCAL] (1) $DER.$FUN_8.p = 0.0 ($RES_SIM_292) (175|185) [SCAL] (1) $DER.$FUN_8.T = 0.0 ($RES_SIM_293) (176|186) [SCAL] (1) $DER.$FUN_9.p = 287.0512249529787 * $DER.T_out2c.rho * (T_in + dT) + 287.0512249529787 * T_out2c.rho * $DER.dT ($RES_SIM_294) (177|187) [SCAL] (1) $DER.$FUN_9.T = $DER.dT ($RES_SIM_295) (178|188) [SCAL] (1) $DER.dT2.p_out = $DER.$FUN_16.p ($RES_SIM_296) (179|189) [SCAL] (1) $DER.dT2.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_16.T, true, ThermofluidStream.Media.myMedia.Interfaces.Choices.ReferenceEnthalpy.ZeroAt0K, 0.0, $DER.$FUN_16.T, 0.0) ($RES_SIM_297) (180|190) [SCAL] (1) $DER.T_out2c.p_out = $DER.$FUN_9.p ($RES_SIM_298) (181|191) [SCAL] (1) $DER.T_out2c.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_9.T, true, ThermofluidStream.Media.myMedia.Interfaces.Choices.ReferenceEnthalpy.ZeroAt0K, 0.0, $DER.$FUN_9.T, 0.0) ($RES_SIM_299) (182|192) [SCAL] (1) $DER.dT2.m_flow = (($DER.dT2.du * dT2c.Q_flow + dT2.du * $DER.dT2c.Q_flow) * (4.930380657631324e-32 + dT2.du ^ 2.0) - (2.0 * dT2.du * $DER.dT2.du) * dT2.du * dT2c.Q_flow) / (4.930380657631324e-32 + dT2.du ^ 2.0) ^ 2.0 ($RES_SIM_300) (183|193) [SCAL] (1) $DER.$FUN_15.p = 0.0 ($RES_SIM_301) (184|194) [SCAL] (1) $DER.$FUN_15.T = 0.0 ($RES_SIM_302) (185|195) [SCAL] (1) $DER.$FUN_16.p = 287.0512249529787 * $DER.dT2.rho * dT2.T_out + 287.0512249529787 * dT2.rho * $DER.dT2.T_out ($RES_SIM_303) (186|196) [SCAL] (1) $DER.$FUN_16.T = $DER.dT2.T_out ($RES_SIM_304) (187|197) [RECD] (2) $DER.source1.outlet.state = $DER.$FUN_15 ($RES_SIM_305) (188|199) [SCAL] (1) $DER.$FUN_22.p = 0.0 ($RES_SIM_306) (189|200) [SCAL] (1) $DER.$FUN_22.T = 0.0 ($RES_SIM_307) (190|201) [SCAL] (1) $DER.$FUN_23.p = 287.0512249529787 * $DER.T_out2.rho * (T_in + dT) + 287.0512249529787 * T_out2.rho * $DER.dT ($RES_SIM_308) (191|202) [SCAL] (1) $DER.dT2c.p_out = $DER.$FUN_2.p ($RES_SIM_309) (192|203) [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_310) (193|204) [SCAL] (1) $DER.$FUN_23.T = $DER.dT ($RES_SIM_311) (194|205) [SCAL] (1) $DER.dT = $DER.dT2c.T_out - $DER.dT2c.T_in ($RES_SIM_312) (195|206) [SCAL] (1) $DER.dT2c.du = $DER.dT2c.u_out - $DER.dT2c.u_in ($RES_SIM_313) (196|207) [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_314) (197|208) [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_315) (198|209) [SCAL] (1) $DER.T_out2c.m_flow = (($DER.T_out2c.du * dT2c.Q_flow + T_out2c.du * $DER.dT2c.Q_flow) * (4.930380657631324e-32 + T_out2c.du ^ 2.0) - (2.0 * T_out2c.du * $DER.T_out2c.du) * T_out2c.du * dT2c.Q_flow) / (4.930380657631324e-32 + T_out2c.du ^ 2.0) ^ 2.0 ($RES_SIM_316) (199|210) [RECD] (2) $DER.source2.outlet.state = $DER.$FUN_8 ($RES_SIM_317) (200|212) [SCAL] (1) $DER.T_out2c.du = $DER.T_out2c.u_out - $DER.T_out2c.u_in ($RES_SIM_318) (201|213) [SCAL] (1) $DER.T_out2c.u_in = $DER.T_out2c.h_in - ($DER.T_out2c.p_in * T_out2c.rho - T_out2c.p_in * $DER.T_out2c.rho) / T_out2c.rho ^ 2.0 ($RES_SIM_319) (202|214) [SCAL] (1) $DER.T_out2c.u_out = $DER.T_out2c.h_out - ($DER.T_out2c.p_out * T_out2c.rho - T_out2c.p_out * $DER.T_out2c.rho) / T_out2c.rho ^ 2.0 ($RES_SIM_320) (203|215) [SCAL] (1) $DER.dT2c.Q_flow = if $SEV_6 then 0.0 else if $SEV_7 then (heatFlowRate.amplitude * heatFlowRate.rising) / heatFlowRate.rising ^ 2.0 else if $SEV_8 then 0.0 else if $SEV_9 then -(heatFlowRate.amplitude * heatFlowRate.falling) / heatFlowRate.falling ^ 2.0 else 0.0 ($RES_SIM_321) (204|216) [SCAL] (1) $DER.source3.outlet.state.T = $DER.T_out2.inlet.state.T ($RES_SIM_322) (205|217) [SCAL] (1) $DER.source3.outlet.state.p = $DER.T_out2.inlet.state.p ($RES_SIM_323) (206|218) [SCAL] (1) $DER.dT = $DER.dT2.T_out - $DER.dT2.T_in ($RES_SIM_324) (207|219) [SCAL] (1) $DER.dT2c.m_flow = (($DER.dT2c.du * dT2c.Q_flow + dT2c.du * $DER.dT2c.Q_flow) * (4.930380657631324e-32 + dT2c.du ^ 2.0) - (2.0 * dT2c.du * $DER.dT2c.du) * dT2c.du * dT2c.Q_flow) / (4.930380657631324e-32 + dT2c.du ^ 2.0) ^ 2.0 ($RES_SIM_325) (208|220) [SCAL] (1) $DER.dT2.du = $DER.dT2.u_out - $DER.dT2.u_in ($RES_SIM_326) (209|221) [SCAL] (1) $DER.source1.outlet.state.T = $DER.dT2.inlet.state.T ($RES_SIM_327) (210|222) [SCAL] (1) $DER.dT2.u_in = $DER.dT2.h_in - ($DER.dT2.p_in * dT2.rho - dT2.p_in * $DER.dT2.rho) / dT2.rho ^ 2.0 ($RES_SIM_328) (211|223) [SCAL] (1) $DER.source1.outlet.state.p = $DER.dT2.inlet.state.p ($RES_SIM_329) (212|224) [SCAL] (1) $DER.dT2.u_out = $DER.dT2.h_out - ($DER.dT2.p_out * dT2.rho - dT2.p_out * $DER.dT2.rho) / dT2.rho ^ 2.0 ($RES_SIM_330) =================== Scalar Matching =================== variable to equation ********************** var 1 --> eqn 3 var 2 --> eqn 73 var 3 --> eqn 120 var 4 --> eqn 139 var 5 --> eqn 17 var 6 --> eqn 129 var 7 --> eqn 109 var 8 --> eqn 143 var 9 --> eqn 79 var 10 --> eqn 137 var 11 --> eqn -1 var 12 --> eqn -1 var 13 --> eqn 61 var 14 --> eqn 117 var 15 --> eqn 45 var 16 --> eqn 42 var 17 --> eqn 169 var 18 --> eqn 38 var 19 --> eqn 34 var 20 --> eqn 24 var 21 --> eqn 23 var 22 --> eqn 83 var 23 --> eqn 119 var 24 --> eqn 131 var 25 --> eqn 77 var 26 --> eqn 69 var 27 --> eqn 67 var 28 --> eqn 118 var 29 --> eqn 84 var 30 --> eqn -1 var 31 --> eqn 127 var 32 --> eqn 113 var 33 --> eqn 54 var 34 --> eqn 140 var 35 --> eqn 8 var 36 --> eqn -1 var 37 --> eqn 51 var 38 --> eqn 78 var 39 --> eqn 2 var 40 --> eqn 133 var 41 --> eqn 141 var 42 --> eqn 18 var 43 --> eqn 146 var 44 --> eqn 62 var 45 --> eqn -1 var 46 --> eqn 138 var 47 --> eqn 59 var 48 --> eqn 72 var 49 --> eqn 57 var 50 --> eqn 37 var 51 --> eqn 28 var 52 --> eqn 29 var 53 --> eqn 13 var 54 --> eqn 41 var 55 --> eqn -1 var 56 --> eqn 32 var 57 --> eqn 81 var 58 --> eqn 102 var 59 --> eqn 31 var 60 --> eqn 12 var 61 --> eqn 111 var 62 --> eqn 150 var 63 --> eqn 86 var 64 --> eqn 80 var 65 --> eqn 101 var 66 --> eqn 36 var 67 --> eqn 70 var 68 --> eqn 68 var 69 --> eqn 65 var 70 --> eqn 5 var 71 --> eqn 47 var 72 --> eqn 148 var 73 --> eqn 75 var 74 --> eqn 52 var 75 --> eqn 53 var 76 --> eqn 27 var 77 --> eqn 35 var 78 --> eqn 11 var 79 --> eqn 25 var 80 --> eqn 132 var 81 --> eqn 121 var 82 --> eqn 116 var 83 --> eqn 97 var 84 --> eqn 4 var 85 --> eqn 96 var 86 --> eqn 95 var 87 --> eqn 94 var 88 --> eqn 93 var 89 --> eqn 87 var 90 --> eqn 92 var 91 --> eqn 9 var 92 --> eqn 91 var 93 --> eqn 122 var 94 --> eqn 90 var 95 --> eqn 89 var 96 --> eqn 49 var 97 --> eqn 58 var 98 --> eqn 104 var 99 --> eqn 50 var 100 --> eqn 66 var 101 --> eqn 48 var 102 --> eqn 43 var 103 --> eqn 40 var 104 --> eqn 114 var 105 --> eqn 74 var 106 --> eqn 33 var 107 --> eqn 115 var 108 --> eqn 142 var 109 --> eqn 145 var 110 --> eqn 14 var 111 --> eqn 105 var 112 --> eqn 46 var 113 --> eqn -1 var 114 --> eqn 76 var 115 --> eqn 19 var 116 --> eqn 112 var 117 --> eqn -1 var 118 --> eqn 124 var 119 --> eqn 147 var 120 --> eqn 107 var 121 --> eqn 56 var 122 --> eqn 60 var 123 --> eqn 82 var 124 --> eqn 16 var 125 --> eqn 71 var 126 --> eqn 55 var 127 --> eqn -1 var 128 --> eqn 110 var 129 --> eqn 20 var 130 --> eqn 15 var 131 --> eqn 1 var 132 --> eqn 30 var 133 --> eqn 126 var 134 --> eqn 108 var 135 --> eqn 149 var 136 --> eqn 7 var 137 --> eqn 39 var 138 --> eqn 144 var 139 --> eqn 103 var 140 --> eqn -1 var 141 --> eqn 130 var 142 --> eqn 98 var 143 --> eqn 26 var 144 --> eqn 134 var 145 --> eqn 106 var 146 --> eqn 123 var 147 --> eqn 6 var 148 --> eqn 10 var 149 --> eqn 85 var 150 --> eqn 128 var 151 --> eqn 152 var 152 --> eqn 153 var 153 --> eqn -1 var 154 --> eqn -1 var 155 --> eqn 154 var 156 --> eqn -1 var 157 --> eqn 156 var 158 --> eqn 157 var 159 --> eqn 151 var 160 --> eqn 155 var 161 --> eqn 162 var 162 --> eqn -1 var 163 --> eqn 170 var 164 --> eqn 171 var 165 --> eqn 172 var 166 --> eqn 173 var 167 --> eqn 174 var 168 --> eqn 175 var 169 --> eqn 176 var 170 --> eqn -1 var 171 --> eqn -1 var 172 --> eqn 177 var 173 --> eqn 179 var 174 --> eqn 180 var 175 --> eqn 181 var 176 --> eqn 184 var 177 --> eqn 185 var 178 --> eqn 186 var 179 --> eqn 187 var 180 --> eqn 193 var 181 --> eqn 194 var 182 --> eqn 188 var 183 --> eqn 196 var 184 --> eqn 197 var 185 --> eqn 198 var 186 --> eqn -1 var 187 --> eqn -1 var 188 --> eqn 199 var 189 --> eqn 200 var 190 --> eqn 158 var 191 --> eqn 201 var 192 --> eqn 202 var 193 --> eqn 183 var 194 --> eqn 204 var 195 --> eqn 168 var 196 --> eqn 205 var 197 --> eqn 164 var 198 --> eqn 166 var 199 --> eqn 207 var 200 --> eqn 182 var 201 --> eqn 208 var 202 --> eqn 203 var 203 --> eqn 206 var 204 --> eqn -1 var 205 --> eqn -1 var 206 --> eqn 210 var 207 --> eqn 211 var 208 --> eqn 209 var 209 --> eqn 213 var 210 --> eqn 160 var 211 --> eqn 212 var 212 --> eqn 161 var 213 --> eqn 190 var 214 --> eqn 191 var 215 --> eqn 214 var 216 --> eqn 178 var 217 --> eqn 216 var 218 --> eqn 217 var 219 --> eqn -1 var 220 --> eqn 218 var 221 --> eqn 195 var 222 --> eqn 159 var 223 --> eqn 215 var 224 --> eqn 219 var 225 --> eqn 192 var 226 --> eqn 167 var 227 --> eqn 221 var 228 --> eqn 222 var 229 --> eqn 165 var 230 --> eqn 220 var 231 --> eqn 163 var 232 --> eqn 223 var 233 --> eqn -1 var 234 --> eqn 224 var 235 --> eqn 189 var 236 --> eqn -1 var 237 --> eqn 44 var 238 --> eqn -1 var 239 --> eqn 125 var 240 --> eqn 88 equation to variable ********************** eqn 1 --> var 131 eqn 2 --> var 39 eqn 3 --> var 1 eqn 4 --> var 84 eqn 5 --> var 70 eqn 6 --> var 147 eqn 7 --> var 136 eqn 8 --> var 35 eqn 9 --> var 91 eqn 10 --> var 148 eqn 11 --> var 78 eqn 12 --> var 60 eqn 13 --> var 53 eqn 14 --> var 110 eqn 15 --> var 130 eqn 16 --> var 124 eqn 17 --> var 5 eqn 18 --> var 42 eqn 19 --> var 115 eqn 20 --> var 129 eqn 21 --> var -1 eqn 22 --> var -1 eqn 23 --> var 21 eqn 24 --> var 20 eqn 25 --> var 79 eqn 26 --> var 143 eqn 27 --> var 76 eqn 28 --> var 51 eqn 29 --> var 52 eqn 30 --> var 132 eqn 31 --> var 59 eqn 32 --> var 56 eqn 33 --> var 106 eqn 34 --> var 19 eqn 35 --> var 77 eqn 36 --> var 66 eqn 37 --> var 50 eqn 38 --> var 18 eqn 39 --> var 137 eqn 40 --> var 103 eqn 41 --> var 54 eqn 42 --> var 16 eqn 43 --> var 102 eqn 44 --> var 237 eqn 45 --> var 15 eqn 46 --> var 112 eqn 47 --> var 71 eqn 48 --> var 101 eqn 49 --> var 96 eqn 50 --> var 99 eqn 51 --> var 37 eqn 52 --> var 74 eqn 53 --> var 75 eqn 54 --> var 33 eqn 55 --> var 126 eqn 56 --> var 121 eqn 57 --> var 49 eqn 58 --> var 97 eqn 59 --> var 47 eqn 60 --> var 122 eqn 61 --> var 13 eqn 62 --> var 44 eqn 63 --> var -1 eqn 64 --> var -1 eqn 65 --> var 69 eqn 66 --> var 100 eqn 67 --> var 27 eqn 68 --> var 68 eqn 69 --> var 26 eqn 70 --> var 67 eqn 71 --> var 125 eqn 72 --> var 48 eqn 73 --> var 2 eqn 74 --> var 105 eqn 75 --> var 73 eqn 76 --> var 114 eqn 77 --> var 25 eqn 78 --> var 38 eqn 79 --> var 9 eqn 80 --> var 64 eqn 81 --> var 57 eqn 82 --> var 123 eqn 83 --> var 22 eqn 84 --> var 29 eqn 85 --> var 149 eqn 86 --> var 63 eqn 87 --> var 89 eqn 88 --> var 240 eqn 89 --> var 95 eqn 90 --> var 94 eqn 91 --> var 92 eqn 92 --> var 90 eqn 93 --> var 88 eqn 94 --> var 87 eqn 95 --> var 86 eqn 96 --> var 85 eqn 97 --> var 83 eqn 98 --> var 142 eqn 99 --> var -1 eqn 100 --> var -1 eqn 101 --> var 65 eqn 102 --> var 58 eqn 103 --> var 139 eqn 104 --> var 98 eqn 105 --> var 111 eqn 106 --> var 145 eqn 107 --> var 120 eqn 108 --> var 134 eqn 109 --> var 7 eqn 110 --> var 128 eqn 111 --> var 61 eqn 112 --> var 116 eqn 113 --> var 32 eqn 114 --> var 104 eqn 115 --> var 107 eqn 116 --> var 82 eqn 117 --> var 14 eqn 118 --> var 28 eqn 119 --> var 23 eqn 120 --> var 3 eqn 121 --> var 81 eqn 122 --> var 93 eqn 123 --> var 146 eqn 124 --> var 118 eqn 125 --> var 239 eqn 126 --> var 133 eqn 127 --> var 31 eqn 128 --> var 150 eqn 129 --> var 6 eqn 130 --> var 141 eqn 131 --> var 24 eqn 132 --> var 80 eqn 133 --> var 40 eqn 134 --> var 144 eqn 135 --> var -1 eqn 136 --> var -1 eqn 137 --> var 10 eqn 138 --> var 46 eqn 139 --> var 4 eqn 140 --> var 34 eqn 141 --> var 41 eqn 142 --> var 108 eqn 143 --> var 8 eqn 144 --> var 138 eqn 145 --> var 109 eqn 146 --> var 43 eqn 147 --> var 119 eqn 148 --> var 72 eqn 149 --> var 135 eqn 150 --> var 62 eqn 151 --> var 159 eqn 152 --> var 151 eqn 153 --> var 152 eqn 154 --> var 155 eqn 155 --> var 160 eqn 156 --> var 157 eqn 157 --> var 158 eqn 158 --> var 190 eqn 159 --> var 222 eqn 160 --> var 210 eqn 161 --> var 212 eqn 162 --> var 161 eqn 163 --> var 231 eqn 164 --> var 197 eqn 165 --> var 229 eqn 166 --> var 198 eqn 167 --> var 226 eqn 168 --> var 195 eqn 169 --> var 17 eqn 170 --> var 163 eqn 171 --> var 164 eqn 172 --> var 165 eqn 173 --> var 166 eqn 174 --> var 167 eqn 175 --> var 168 eqn 176 --> var 169 eqn 177 --> var 172 eqn 178 --> var 216 eqn 179 --> var 173 eqn 180 --> var 174 eqn 181 --> var 175 eqn 182 --> var 200 eqn 183 --> var 193 eqn 184 --> var 176 eqn 185 --> var 177 eqn 186 --> var 178 eqn 187 --> var 179 eqn 188 --> var 182 eqn 189 --> var 235 eqn 190 --> var 213 eqn 191 --> var 214 eqn 192 --> var 225 eqn 193 --> var 180 eqn 194 --> var 181 eqn 195 --> var 221 eqn 196 --> var 183 eqn 197 --> var 184 eqn 198 --> var 185 eqn 199 --> var 188 eqn 200 --> var 189 eqn 201 --> var 191 eqn 202 --> var 192 eqn 203 --> var 202 eqn 204 --> var 194 eqn 205 --> var 196 eqn 206 --> var 203 eqn 207 --> var 199 eqn 208 --> var 201 eqn 209 --> var 208 eqn 210 --> var 206 eqn 211 --> var 207 eqn 212 --> var 211 eqn 213 --> var 209 eqn 214 --> var 215 eqn 215 --> var 223 eqn 216 --> var 217 eqn 217 --> var 218 eqn 218 --> var 220 eqn 219 --> var 224 eqn 220 --> var 230 eqn 221 --> var 227 eqn 222 --> var 228 eqn 223 --> var 232 eqn 224 --> var 234 " [Timeout remaining time 659] [Calling sys.exit(0), Time elapsed: 2.9879587469622493] Failed to read output from testmodel.py, exit status != 0: 0.612084036692977 0.6221426710000001 0.13203401 Calling exit ...