Running: ./testmodel.py --libraries=/home/hudson/saved_omc/libraries/.openmodelica/libraries --ompython_omhome=/usr ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased.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 0.001344/0.001344, allocations: 80.2 kB / 19.18 MB, free: 2.527 MB / 14.72 MB
"
[Timeout remaining time 180]
loadFile("/home/hudson/saved_omc/libraries/.openmodelica/libraries/Complex 4.1.0+maint.om/package.mo", uses=false) [Timeout 180]
"Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/Complex 4.1.0+maint.om/package.mo): time 0.001461/0.001461, allocations: 171.5 kB / 22.46 MB, free: 5.352 MB / 14.72 MB
"
[Timeout remaining time 180]
loadFile("/home/hudson/saved_omc/libraries/.openmodelica/libraries/Modelica 4.1.0+maint.om/package.mo", uses=false) [Timeout 180]
"Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/Modelica 4.1.0+maint.om/package.mo): time 1.464/1.464, allocations: 177.1 MB / 202.8 MB, free: 9.191 MB / 190.1 MB
"
[Timeout remaining time 178]
loadFile("/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermofluidStream main/package.mo", uses=false) [Timeout 180]
"Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermofluidStream main/package.mo): time 0.9738/0.9738, allocations: 116 MB / 375.2 MB, free: 7.52 MB / 350.1 MB
"
[Timeout remaining time 179]
Using package ThermofluidStream with version 1.3.0 (/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermofluidStream main/package.mo)
Using package Modelica with version 4.1.0 (/home/hudson/saved_omc/libraries/.openmodelica/libraries/Modelica 4.1.0+maint.om/package.mo)
Using package Complex with version 4.1.0 (/home/hudson/saved_omc/libraries/.openmodelica/libraries/Complex 4.1.0+maint.om/package.mo)
Using package ModelicaServices with version 4.1.0 (/home/hudson/saved_omc/libraries/.openmodelica/libraries/ModelicaServices 4.1.0+maint.om/package.mo)
Running command: translateModel(ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased,tolerance=1e-06,outputFormat="mat",numberOfIntervals=100,variableFilter="CPUtime|EventCounter|Time|_derdummy|_dummy|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|eta|fullMedium.L|fullMedium.P|fullMedium.P_nom|fullMedium.TC|fullMedium.adiabaticModel.eta_is|fullMedium.adiabaticModel.h_in|fullMedium.adiabaticModel.h_out|fullMedium.adiabaticModel.h_out_is|fullMedium.adiabaticModel.p_out|fullMedium.adiabaticModel.s_in|fullMedium.adiabaticModel.state_in.T|fullMedium.adiabaticModel.state_in.p|fullMedium.adiabaticModel.w_t|fullMedium.adiabaticModel.w_t_is|fullMedium.assertionLevel|fullMedium.clip_p_out|fullMedium.dh|fullMedium.dp|fullMedium.dp_fixed|fullMedium.dp_nom|fullMedium.dp_start|fullMedium.dr_corr|fullMedium.etaSpec|fullMedium.eta_actual|fullMedium.eta_fixed|fullMedium.eta_is|fullMedium.h_in|fullMedium.h_out|fullMedium.initM_flow|der.fullMedium.inlet.m_flow.|fullMedium.inlet.m_flow|fullMedium.inlet.r|fullMedium.inlet.state.T|fullMedium.inlet.state.p|fullMedium.m_acceleration_0|fullMedium.m_flow|fullMedium.m_flowStateSelect|fullMedium.m_flow_0|fullMedium.outlet.m_flow|fullMedium.outlet.r|fullMedium.outlet.state.T|fullMedium.outlet.state.p|fullMedium.outletSpec|fullMedium.outletSpec_actual|fullMedium.outletSpec_prescribed|fullMedium.outletValueSpec|fullMedium.pRatio|fullMedium.pRatio_fixed|fullMedium.p_in|fullMedium.p_min|fullMedium.p_out|fullMedium.p_out_fixed|fullMedium.singularityRegime|incompressibleFluid.L|incompressibleFluid.P|incompressibleFluid.P_nom|incompressibleFluid.TC|incompressibleFluid.adiabaticModel.T_in|incompressibleFluid.adiabaticModel.T_out_is|incompressibleFluid.adiabaticModel.assertionLevel|incompressibleFluid.adiabaticModel.deltaDensityRel|incompressibleFluid.adiabaticModel.eta_is|incompressibleFluid.adiabaticModel.h_in|incompressibleFluid.adiabaticModel.h_out|incompressibleFluid.adiabaticModel.isDensityWithinTol|incompressibleFluid.adiabaticModel.p_out|incompressibleFluid.adiabaticModel.relTolDensity|incompressibleFluid.adiabaticModel.rho_in|incompressibleFluid.adiabaticModel.rho_out|incompressibleFluid.adiabaticModel.state_in.T|incompressibleFluid.adiabaticModel.state_in.p|incompressibleFluid.adiabaticModel.w_t|incompressibleFluid.adiabaticModel.w_t_is|incompressibleFluid.assertionLevel|incompressibleFluid.clip_p_out|incompressibleFluid.dh|incompressibleFluid.dp|incompressibleFluid.dp_fixed|incompressibleFluid.dp_nom|incompressibleFluid.dp_start|incompressibleFluid.dr_corr|incompressibleFluid.etaSpec|incompressibleFluid.eta_actual|incompressibleFluid.eta_fixed|incompressibleFluid.eta_is|incompressibleFluid.h_in|incompressibleFluid.h_out|incompressibleFluid.initM_flow|der.incompressibleFluid.inlet.m_flow.|incompressibleFluid.inlet.m_flow|incompressibleFluid.inlet.r|incompressibleFluid.inlet.state.T|incompressibleFluid.inlet.state.p|incompressibleFluid.m_acceleration_0|incompressibleFluid.m_flow|incompressibleFluid.m_flowStateSelect|incompressibleFluid.m_flow_0|incompressibleFluid.outlet.m_flow|incompressibleFluid.outlet.r|incompressibleFluid.outlet.state.T|incompressibleFluid.outlet.state.p|incompressibleFluid.outletSpec|incompressibleFluid.outletSpec_actual|incompressibleFluid.outletSpec_prescribed|incompressibleFluid.outletValueSpec|incompressibleFluid.pRatio|incompressibleFluid.pRatio_fixed|incompressibleFluid.p_in|incompressibleFluid.p_min|incompressibleFluid.p_out|incompressibleFluid.p_out_fixed|incompressibleFluid.singularityRegime|isothermalReference.L|isothermalReference.P|isothermalReference.P_nom|isothermalReference.TC|isothermalReference.adiabaticModel.T_in|isothermalReference.adiabaticModel.T_out_is|isothermalReference.adiabaticModel.assertionLevel|isothermalReference.adiabaticModel.deltaDensityRel|isothermalReference.adiabaticModel.eta_is|isothermalReference.adiabaticModel.h_in|isothermalReference.adiabaticModel.h_out|isothermalReference.adiabaticModel.h_out_is|isothermalReference.adiabaticModel.isDensityWithinTol|isothermalReference.adiabaticModel.p_out|isothermalReference.adiabaticModel.relTolDensity|isothermalReference.adiabaticModel.rho_in|isothermalReference.adiabaticModel.rho_out|isothermalReference.adiabaticModel.state_in.T|isothermalReference.adiabaticModel.state_in.p|isothermalReference.adiabaticModel.w_t|isothermalReference.adiabaticModel.w_t_is|isothermalReference.assertionLevel|isothermalReference.clip_p_out|isothermalReference.dh|isothermalReference.dp|isothermalReference.dp_fixed|isothermalReference.dp_nom|isothermalReference.dp_start|isothermalReference.dr_corr|isothermalReference.etaSpec|isothermalReference.eta_actual|isothermalReference.eta_fixed|isothermalReference.eta_is|isothermalReference.h_in|isothermalReference.h_out|isothermalReference.initM_flow|der.isothermalReference.inlet.m_flow.|isothermalReference.inlet.m_flow|isothermalReference.inlet.r|isothermalReference.inlet.state.T|isothermalReference.inlet.state.p|isothermalReference.m_acceleration_0|isothermalReference.m_flow|isothermalReference.m_flowStateSelect|isothermalReference.m_flow_0|isothermalReference.outlet.m_flow|isothermalReference.outlet.r|isothermalReference.outlet.state.T|isothermalReference.outlet.state.p|isothermalReference.outletSpec|isothermalReference.outletSpec_actual|isothermalReference.outletSpec_prescribed|isothermalReference.outletValueSpec|isothermalReference.pRatio|isothermalReference.pRatio_fixed|isothermalReference.p_in|isothermalReference.p_min|isothermalReference.p_out|isothermalReference.p_out_fixed|isothermalReference.singularityRegime|pressureDifference.duration|pressureDifference.height|pressureDifference.offset|pressureDifference.startTime|pressureDifference.y|sink.L|der.sink.inlet.m_flow.|sink.inlet.m_flow|sink.inlet.r|sink.inlet.state.T|sink.inlet.state.p|sink.m_flow|sink.m_flowSpec|sink.m_flow_fixed|sink1.L|der.sink1.inlet.m_flow.|sink1.inlet.m_flow|sink1.inlet.r|sink1.inlet.state.T|sink1.inlet.state.p|sink1.m_flow|sink1.m_flowSpec|sink1.m_flow_fixed|sink2.L|der.sink2.inlet.m_flow.|sink2.inlet.m_flow|sink2.inlet.r|sink2.inlet.state.T|sink2.inlet.state.p|sink2.m_flow|sink2.m_flowSpec|sink2.m_flow_fixed|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",fileNamePrefix="ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased")
translateModel(ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased,tolerance=1e-06,outputFormat="mat",numberOfIntervals=100,variableFilter="CPUtime|EventCounter|Time|_derdummy|_dummy|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|eta|fullMedium.L|fullMedium.P|fullMedium.P_nom|fullMedium.TC|fullMedium.adiabaticModel.eta_is|fullMedium.adiabaticModel.h_in|fullMedium.adiabaticModel.h_out|fullMedium.adiabaticModel.h_out_is|fullMedium.adiabaticModel.p_out|fullMedium.adiabaticModel.s_in|fullMedium.adiabaticModel.state_in.T|fullMedium.adiabaticModel.state_in.p|fullMedium.adiabaticModel.w_t|fullMedium.adiabaticModel.w_t_is|fullMedium.assertionLevel|fullMedium.clip_p_out|fullMedium.dh|fullMedium.dp|fullMedium.dp_fixed|fullMedium.dp_nom|fullMedium.dp_start|fullMedium.dr_corr|fullMedium.etaSpec|fullMedium.eta_actual|fullMedium.eta_fixed|fullMedium.eta_is|fullMedium.h_in|fullMedium.h_out|fullMedium.initM_flow|der.fullMedium.inlet.m_flow.|fullMedium.inlet.m_flow|fullMedium.inlet.r|fullMedium.inlet.state.T|fullMedium.inlet.state.p|fullMedium.m_acceleration_0|fullMedium.m_flow|fullMedium.m_flowStateSelect|fullMedium.m_flow_0|fullMedium.outlet.m_flow|fullMedium.outlet.r|fullMedium.outlet.state.T|fullMedium.outlet.state.p|fullMedium.outletSpec|fullMedium.outletSpec_actual|fullMedium.outletSpec_prescribed|fullMedium.outletValueSpec|fullMedium.pRatio|fullMedium.pRatio_fixed|fullMedium.p_in|fullMedium.p_min|fullMedium.p_out|fullMedium.p_out_fixed|fullMedium.singularityRegime|incompressibleFluid.L|incompressibleFluid.P|incompressibleFluid.P_nom|incompressibleFluid.TC|incompressibleFluid.adiabaticModel.T_in|incompressibleFluid.adiabaticModel.T_out_is|incompressibleFluid.adiabaticModel.assertionLevel|incompressibleFluid.adiabaticModel.deltaDensityRel|incompressibleFluid.adiabaticModel.eta_is|incompressibleFluid.adiabaticModel.h_in|incompressibleFluid.adiabaticModel.h_out|incompressibleFluid.adiabaticModel.isDensityWithinTol|incompressibleFluid.adiabaticModel.p_out|incompressibleFluid.adiabaticModel.relTolDensity|incompressibleFluid.adiabaticModel.rho_in|incompressibleFluid.adiabaticModel.rho_out|incompressibleFluid.adiabaticModel.state_in.T|incompressibleFluid.adiabaticModel.state_in.p|incompressibleFluid.adiabaticModel.w_t|incompressibleFluid.adiabaticModel.w_t_is|incompressibleFluid.assertionLevel|incompressibleFluid.clip_p_out|incompressibleFluid.dh|incompressibleFluid.dp|incompressibleFluid.dp_fixed|incompressibleFluid.dp_nom|incompressibleFluid.dp_start|incompressibleFluid.dr_corr|incompressibleFluid.etaSpec|incompressibleFluid.eta_actual|incompressibleFluid.eta_fixed|incompressibleFluid.eta_is|incompressibleFluid.h_in|incompressibleFluid.h_out|incompressibleFluid.initM_flow|der.incompressibleFluid.inlet.m_flow.|incompressibleFluid.inlet.m_flow|incompressibleFluid.inlet.r|incompressibleFluid.inlet.state.T|incompressibleFluid.inlet.state.p|incompressibleFluid.m_acceleration_0|incompressibleFluid.m_flow|incompressibleFluid.m_flowStateSelect|incompressibleFluid.m_flow_0|incompressibleFluid.outlet.m_flow|incompressibleFluid.outlet.r|incompressibleFluid.outlet.state.T|incompressibleFluid.outlet.state.p|incompressibleFluid.outletSpec|incompressibleFluid.outletSpec_actual|incompressibleFluid.outletSpec_prescribed|incompressibleFluid.outletValueSpec|incompressibleFluid.pRatio|incompressibleFluid.pRatio_fixed|incompressibleFluid.p_in|incompressibleFluid.p_min|incompressibleFluid.p_out|incompressibleFluid.p_out_fixed|incompressibleFluid.singularityRegime|isothermalReference.L|isothermalReference.P|isothermalReference.P_nom|isothermalReference.TC|isothermalReference.adiabaticModel.T_in|isothermalReference.adiabaticModel.T_out_is|isothermalReference.adiabaticModel.assertionLevel|isothermalReference.adiabaticModel.deltaDensityRel|isothermalReference.adiabaticModel.eta_is|isothermalReference.adiabaticModel.h_in|isothermalReference.adiabaticModel.h_out|isothermalReference.adiabaticModel.h_out_is|isothermalReference.adiabaticModel.isDensityWithinTol|isothermalReference.adiabaticModel.p_out|isothermalReference.adiabaticModel.relTolDensity|isothermalReference.adiabaticModel.rho_in|isothermalReference.adiabaticModel.rho_out|isothermalReference.adiabaticModel.state_in.T|isothermalReference.adiabaticModel.state_in.p|isothermalReference.adiabaticModel.w_t|isothermalReference.adiabaticModel.w_t_is|isothermalReference.assertionLevel|isothermalReference.clip_p_out|isothermalReference.dh|isothermalReference.dp|isothermalReference.dp_fixed|isothermalReference.dp_nom|isothermalReference.dp_start|isothermalReference.dr_corr|isothermalReference.etaSpec|isothermalReference.eta_actual|isothermalReference.eta_fixed|isothermalReference.eta_is|isothermalReference.h_in|isothermalReference.h_out|isothermalReference.initM_flow|der.isothermalReference.inlet.m_flow.|isothermalReference.inlet.m_flow|isothermalReference.inlet.r|isothermalReference.inlet.state.T|isothermalReference.inlet.state.p|isothermalReference.m_acceleration_0|isothermalReference.m_flow|isothermalReference.m_flowStateSelect|isothermalReference.m_flow_0|isothermalReference.outlet.m_flow|isothermalReference.outlet.r|isothermalReference.outlet.state.T|isothermalReference.outlet.state.p|isothermalReference.outletSpec|isothermalReference.outletSpec_actual|isothermalReference.outletSpec_prescribed|isothermalReference.outletValueSpec|isothermalReference.pRatio|isothermalReference.pRatio_fixed|isothermalReference.p_in|isothermalReference.p_min|isothermalReference.p_out|isothermalReference.p_out_fixed|isothermalReference.singularityRegime|pressureDifference.duration|pressureDifference.height|pressureDifference.offset|pressureDifference.startTime|pressureDifference.y|sink.L|der.sink.inlet.m_flow.|sink.inlet.m_flow|sink.inlet.r|sink.inlet.state.T|sink.inlet.state.p|sink.m_flow|sink.m_flowSpec|sink.m_flow_fixed|sink1.L|der.sink1.inlet.m_flow.|sink1.inlet.m_flow|sink1.inlet.r|sink1.inlet.state.T|sink1.inlet.state.p|sink1.m_flow|sink1.m_flowSpec|sink1.m_flow_fixed|sink2.L|der.sink2.inlet.m_flow.|sink2.inlet.m_flow|sink2.inlet.r|sink2.inlet.state.T|sink2.inlet.state.p|sink2.m_flow|sink2.m_flowSpec|sink2.m_flow_fixed|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",fileNamePrefix="ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased") [Timeout 660]
"Notification: Performance of FrontEnd - loaded program: time 1.563e-06/1.563e-06, allocations: 0 / 0.5538 GB, free: 13.77 MB / 478.1 MB
Notification: Performance of FrontEnd - Absyn->SCode: time 2.763e-05/2.919e-05, allocations: 2.281 kB / 0.5538 GB, free: 13.77 MB / 478.1 MB
Notification: Performance of NFInst.instantiate(ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased): time 0.05547/0.0555, allocations: 43.69 MB / 0.5964 GB, free: 1.926 MB / 0.4981 GB
Notification: Performance of NFInst.instExpressions: time 0.004868/0.06037, allocations: 2.523 MB / 0.5989 GB, free: 15.39 MB / 0.5137 GB
Notification: Performance of NFInst.updateImplicitVariability: time 0.0006537/0.06102, allocations: 67.31 kB / 0.599 GB, free: 15.33 MB / 0.5137 GB
Notification: Performance of NFTyping.typeComponents: time 0.001057/0.06208, allocations: 377.1 kB / 0.5993 GB, free: 14.96 MB / 0.5137 GB
Notification: Performance of NFTyping.typeBindings: time 0.00589/0.06797, allocations: 2.437 MB / 0.6017 GB, free: 12.51 MB / 0.5137 GB
Notification: Performance of NFTyping.typeClassSections: time 0.002979/0.07095, allocations: 1.285 MB / 0.603 GB, free: 11.22 MB / 0.5137 GB
Notification: Performance of NFFlatten.flatten: time 0.002005/0.07295, allocations: 1.533 MB / 0.6045 GB, free: 9.684 MB / 0.5137 GB
Notification: Performance of NFFlatten.resolveConnections: time 0.0003182/0.07327, allocations: 135.6 kB / 0.6046 GB, free: 9.539 MB / 0.5137 GB
Notification: Performance of NFEvalConstants.evaluate: time 0.005856/0.07913, allocations: 2.883 MB / 0.6074 GB, free: 6.648 MB / 0.5137 GB
Notification: Performance of NFSimplifyModel.simplify: time 0.0005646/0.07969, allocations: 350.8 kB / 0.6077 GB, free: 6.305 MB / 0.5137 GB
Notification: Performance of NFPackage.collectConstants: time 0.0001011/0.07979, allocations: 63.94 kB / 0.6078 GB, free: 6.242 MB / 0.5137 GB
Notification: Performance of NFFlatten.collectFunctions: time 0.008016/0.08781, allocations: 4.506 MB / 0.6122 GB, free: 1.727 MB / 0.5137 GB
Notification: Performance of NFScalarize.scalarize: time 0.0002097/0.08802, allocations: 167.1 kB / 0.6124 GB, free: 1.562 MB / 0.5137 GB
Notification: Performance of NFVerifyModel.verify: time 0.0004308/0.08845, allocations: 295.1 kB / 0.6126 GB, free: 1.273 MB / 0.5137 GB
Notification: Performance of NFConvertDAE.convert: time 0.003767/0.09222, allocations: 2.115 MB / 0.6147 GB, free: 15.15 MB / 0.5294 GB
Notification: Performance of FrontEnd - DAE generated: time 3.417e-06/0.09222, allocations: 0 / 0.6147 GB, free: 15.15 MB / 0.5294 GB
Notification: Performance of FrontEnd: time 1.272e-06/0.09222, allocations: 0 / 0.6147 GB, free: 15.15 MB / 0.5294 GB
Notification: Performance of Transformations before backend: time 1.166e-05/0.09223, allocations: 0 / 0.6147 GB, free: 15.15 MB / 0.5294 GB
Notification: Model statistics after passing the front-end and creating the data structures used by the back-end:
 * Number of equations: 157
 * Number of variables: 157
Notification: Performance of Generate backend data structure: time 0.002446/0.09468, allocations: 1.413 MB / 0.6161 GB, free: 13.7 MB / 0.5294 GB
Notification: Performance of prepare preOptimizeDAE: time 3.706e-05/0.09472, allocations: 16.03 kB / 0.6161 GB, free: 13.68 MB / 0.5294 GB
Notification: Performance of preOpt normalInlineFunction (simulation): time 0.001239/0.09596, allocations: 204.1 kB / 0.6163 GB, free: 13.48 MB / 0.5294 GB
Notification: Performance of preOpt evaluateParameters (simulation): time 0.001437/0.09739, allocations: 0.7017 MB / 0.617 GB, free: 12.75 MB / 0.5294 GB
Notification: Performance of preOpt simplifyIfEquations (simulation): time 0.0002134/0.09761, allocations: 219.5 kB / 0.6172 GB, free: 12.5 MB / 0.5294 GB
Notification: Performance of preOpt expandDerOperator (simulation): time 0.0001012/0.09771, allocations: 63.95 kB / 0.6173 GB, free: 12.43 MB / 0.5294 GB
Notification: Performance of preOpt clockPartitioning (simulation): time 0.001428/0.09914, allocations: 0.6976 MB / 0.6179 GB, free: 11.7 MB / 0.5294 GB
Notification: Performance of preOpt findStateOrder (simulation): time 1.626e-05/0.09915, allocations: 0 / 0.6179 GB, free: 11.7 MB / 0.5294 GB
Notification: Performance of preOpt replaceEdgeChange (simulation): time 5.961e-05/0.09921, allocations: 24 kB / 0.618 GB, free: 11.67 MB / 0.5294 GB
Notification: Performance of preOpt inlineArrayEqn (simulation): time 2.408e-05/0.09924, allocations: 16 kB / 0.618 GB, free: 11.66 MB / 0.5294 GB
Notification: Performance of preOpt removeEqualRHS (simulation): time 0.001202/0.1004, allocations: 472.9 kB / 0.6184 GB, free: 11.2 MB / 0.5294 GB
Notification: Performance of preOpt removeSimpleEquations (simulation): time 0.003241/0.1037, allocations: 2.1 MB / 0.6205 GB, free: 9.004 MB / 0.5294 GB
Notification: Performance of preOpt comSubExp (simulation): time 0.001392/0.1051, allocations: 391.2 kB / 0.6208 GB, free: 8.613 MB / 0.5294 GB
Notification: Performance of preOpt resolveLoops (simulation): time 0.0003323/0.1054, allocations: 147.7 kB / 0.621 GB, free: 8.469 MB / 0.5294 GB
Notification: Performance of preOpt evalFunc (simulation): time 0.0004117/0.1058, allocations: 120.2 kB / 0.6211 GB, free: 8.352 MB / 0.5294 GB
Notification: Performance of preOpt encapsulateWhenConditions (simulation): time 4.003e-05/0.1059, allocations: 38.84 kB / 0.6211 GB, free: 8.305 MB / 0.5294 GB
Notification: Performance of pre-optimization done (n=34): time 1.713e-06/0.1059, allocations: 4 kB / 0.6211 GB, free: 8.301 MB / 0.5294 GB
Notification: Performance of matching and sorting (n=34): time 0.001497/0.1074, allocations: 487.6 kB / 0.6216 GB, free: 7.82 MB / 0.5294 GB
Notification: Performance of inlineWhenForInitialization (initialization): time 4.818e-05/0.1074, allocations: 55.41 kB / 0.6217 GB, free: 7.754 MB / 0.5294 GB
Notification: Performance of selectInitializationVariablesDAE (initialization): time 0.0007969/0.1082, allocations: 0.6651 MB / 0.6223 GB, free: 7.074 MB / 0.5294 GB
Notification: Performance of collectPreVariables (initialization): time 4.499e-05/0.1082, allocations: 33.7 kB / 0.6223 GB, free: 7.035 MB / 0.5294 GB
Notification: Performance of collectInitialEqns (initialization): time 0.0003647/0.1086, allocations: 468.4 kB / 0.6228 GB, free: 6.574 MB / 0.5294 GB
Notification: Performance of collectInitialBindings (initialization): time 0.0001026/0.1087, allocations: 123 kB / 0.6229 GB, free: 6.453 MB / 0.5294 GB
Notification: Performance of simplifyInitialFunctions (initialization): time 0.0001627/0.1089, allocations: 94.09 kB / 0.623 GB, free: 6.355 MB / 0.5294 GB
Notification: Performance of setup shared object (initialization): time 0.0001518/0.109, allocations: 329.9 kB / 0.6233 GB, free: 6.027 MB / 0.5294 GB
Notification: Performance of preBalanceInitialSystem (initialization): time 0.0003088/0.1093, allocations: 116.9 kB / 0.6234 GB, free: 5.914 MB / 0.5294 GB
Notification: Performance of partitionIndependentBlocks (initialization): time 0.0003878/0.1097, allocations: 201.5 kB / 0.6236 GB, free: 5.688 MB / 0.5294 GB
Notification: Performance of analyzeInitialSystem (initialization): time 0.0007279/0.1105, allocations: 336.2 kB / 0.6239 GB, free: 5.328 MB / 0.5294 GB
Notification: Performance of solveInitialSystemEqSystem (initialization): time 3.016e-06/0.1105, allocations: 0 / 0.6239 GB, free: 5.328 MB / 0.5294 GB
Notification: Performance of matching and sorting (n=51) (initialization): time 0.0009908/0.1114, allocations: 476.1 kB / 0.6244 GB, free: 4.855 MB / 0.5294 GB
Notification: Performance of prepare postOptimizeDAE: time 1.609e-05/0.1115, allocations: 4 kB / 0.6244 GB, free: 4.852 MB / 0.5294 GB
Notification: Performance of postOpt simplifyComplexFunction (initialization): time 9.297e-06/0.1115, allocations: 4 kB / 0.6244 GB, free: 4.848 MB / 0.5294 GB
Notification: Performance of postOpt tearingSystem (initialization): time 1.931e-05/0.1115, allocations: 4 kB / 0.6244 GB, free: 4.844 MB / 0.5294 GB
Notification: Performance of postOpt solveSimpleEquations (initialization): time 0.000417/0.1119, allocations: 99.88 kB / 0.6245 GB, free: 4.746 MB / 0.5294 GB
Notification: Performance of postOpt calculateStrongComponentJacobians (initialization): time 1.166e-05/0.1119, allocations: 12.2 kB / 0.6245 GB, free: 4.734 MB / 0.5294 GB
Notification: Performance of postOpt simplifyAllExpressions (initialization): time 0.0002928/0.1122, allocations: 51.72 kB / 0.6246 GB, free: 4.684 MB / 0.5294 GB
Notification: Performance of postOpt collapseArrayExpressions (initialization): time 5.267e-05/0.1123, allocations: 23.94 kB / 0.6246 GB, free: 4.66 MB / 0.5294 GB
Notification: Model statistics after passing the back-end for initialization:
 * Number of independent subsystems: 10
 * Number of states: 0 ()
 * Number of discrete variables: 0 ()
 * Number of discrete states: 0 ()
 * Number of clocked states: 0 ()
 * Top-level inputs: 0
Notification: Strong component statistics for initialization (51):
 * Single equations (assignments): 51
 * Array equations: 0
 * Algorithm blocks: 0
 * Record equations: 0
 * When equations: 0
 * If-equations: 0
 * Equation systems (not torn): 0
 * Torn equation systems: 0
 * Mixed (continuous/discrete) equation systems: 0
Notification: Performance of prepare postOptimizeDAE: time 0.0002688/0.1125, allocations: 197.6 kB / 0.6248 GB, free: 4.457 MB / 0.5294 GB
Notification: Performance of postOpt lateInlineFunction (simulation): time 0.0001241/0.1127, allocations: 79.48 kB / 0.6248 GB, free: 4.379 MB / 0.5294 GB
Notification: Performance of postOpt wrapFunctionCalls (simulation): time 0.001326/0.114, allocations: 0.6034 MB / 0.6254 GB, free: 3.773 MB / 0.5294 GB
Notification: Performance of postOpt inlineArrayEqn (simulation): time 8.035e-06/0.114, allocations: 4 kB / 0.6254 GB, free: 3.77 MB / 0.5294 GB
Notification: Performance of postOpt constantLinearSystem (simulation): time 4.639e-06/0.114, allocations: 0 / 0.6254 GB, free: 3.77 MB / 0.5294 GB
Notification: Performance of postOpt simplifysemiLinear (simulation): time 5.25e-06/0.114, allocations: 0 / 0.6254 GB, free: 3.77 MB / 0.5294 GB
Notification: Performance of postOpt removeSimpleEquations (simulation): time 0.0006026/0.1146, allocations: 476.7 kB / 0.6259 GB, free: 3.273 MB / 0.5294 GB
Notification: Performance of postOpt simplifyComplexFunction (simulation): time 2.786e-06/0.1146, allocations: 4 kB / 0.6259 GB, free: 3.27 MB / 0.5294 GB
Notification: Performance of postOpt solveSimpleEquations (simulation): time 0.0003257/0.1149, allocations: 75.89 kB / 0.626 GB, free: 3.195 MB / 0.5294 GB
Notification: Performance of postOpt tearingSystem (simulation): time 2.795e-06/0.1149, allocations: 4 kB / 0.626 GB, free: 3.191 MB / 0.5294 GB
Notification: Performance of postOpt inputDerivativesUsed (simulation): time 2.947e-05/0.115, allocations: 11.98 kB / 0.626 GB, free: 3.18 MB / 0.5294 GB
Notification: Performance of postOpt calculateStrongComponentJacobians (simulation): time 2.154e-06/0.115, allocations: 0 / 0.626 GB, free: 3.18 MB / 0.5294 GB
Notification: Performance of postOpt calculateStateSetsJacobians (simulation): time 8.92e-07/0.115, allocations: 0 / 0.626 GB, free: 3.18 MB / 0.5294 GB
Notification: Performance of postOpt symbolicJacobian (simulation): time 0.0008408/0.1158, allocations: 429.2 kB / 0.6264 GB, free: 2.742 MB / 0.5294 GB
Notification: Performance of postOpt removeConstants (simulation): time 0.000196/0.116, allocations: 107.3 kB / 0.6265 GB, free: 2.637 MB / 0.5294 GB
Notification: Performance of postOpt simplifyTimeIndepFuncCalls (simulation): time 7.765e-05/0.1161, allocations: 8 kB / 0.6265 GB, free: 2.629 MB / 0.5294 GB
Notification: Performance of postOpt simplifyAllExpressions (simulation): time 0.0002313/0.1163, allocations: 19.98 kB / 0.6265 GB, free: 2.609 MB / 0.5294 GB
Notification: Performance of postOpt findZeroCrossings (simulation): time 8.369e-05/0.1164, allocations: 27.95 kB / 0.6265 GB, free: 2.582 MB / 0.5294 GB
Notification: Performance of postOpt collapseArrayExpressions (simulation): time 3.494e-05/0.1164, allocations: 15.98 kB / 0.6266 GB, free: 2.566 MB / 0.5294 GB
Notification: Performance of sorting global known variables: time 0.000749/0.1172, allocations: 455 kB / 0.627 GB, free: 2.129 MB / 0.5294 GB
Notification: Performance of sort global known variables: time 1.81e-07/0.1172, allocations: 0 / 0.627 GB, free: 2.129 MB / 0.5294 GB
Notification: Performance of remove unused functions: time 0.001368/0.1185, allocations: 370.8 kB / 0.6273 GB, free: 1.766 MB / 0.5294 GB
Notification: Model statistics after passing the back-end for simulation:
 * Number of independent subsystems: 1
 * Number of states: 0 ()
 * Number of discrete variables: 0 ()
 * Number of discrete states: 0 ()
 * Number of clocked states: 0 ()
 * Top-level inputs: 0
Notification: Strong component statistics for simulation (38):
 * Single equations (assignments): 37
 * Array equations: 0
 * Algorithm blocks: 0
 * Record equations: 1
 * When equations: 0
 * If-equations: 0
 * Equation systems (not torn): 0
 * Torn equation systems: 0
 * Mixed (continuous/discrete) equation systems: 0
Notification: Performance of Backend phase and start with SimCode phase: time 0.001333/0.1199, allocations: 0.5022 MB / 0.6278 GB, free: 1.258 MB / 0.5294 GB
Notification: Performance of simCode: created initialization part: time 0.00118/0.1211, allocations: 307.7 kB / 0.6281 GB, free: 0.957 MB / 0.5294 GB
Notification: Performance of simCode: created event and clocks part: time 3.156e-06/0.1211, allocations: 3.938 kB / 0.6281 GB, free: 0.9531 MB / 0.5294 GB
Notification: Performance of simCode: created simulation system equations: time 0.0005281/0.1216, allocations: 152.4 kB / 0.6283 GB, free: 0.8047 MB / 0.5294 GB
Notification: Performance of simCode: created of all other equations (e.g. parameter, nominal, assert, etc): time 0.001999/0.1236, allocations: 298.9 kB / 0.6286 GB, free: 0.5273 MB / 0.5294 GB
Notification: Performance of simCode: created linear, non-linear and system jacobian parts: time 0.003203/0.1268, allocations: 1.268 MB / 0.6298 GB, free: 15.23 MB / 0.545 GB
Notification: Performance of simCode: some other stuff during SimCode phase: time 0.0005579/0.1274, allocations: 379.8 kB / 0.6302 GB, free: 14.82 MB / 0.545 GB
Notification: Performance of simCode: alias equations: time 0.0007696/0.1281, allocations: 215.8 kB / 0.6304 GB, free: 14.62 MB / 0.545 GB
Notification: Performance of simCode: all other stuff during SimCode phase: time 0.0002592/0.1284, allocations: 72.47 kB / 0.6304 GB, free: 14.55 MB / 0.545 GB
Notification: Performance of SimCode: time 8.42e-07/0.1284, allocations: 0 / 0.6304 GB, free: 14.55 MB / 0.545 GB
Notification: Performance of Templates: time 0.04089/0.1693, allocations: 14.37 MB / 0.6445 GB, free: 0.4961 MB / 0.545 GB
"
[Timeout remaining time 660]
make -j1 -f ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased.makefile [Timeout 660]
(rm -f ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased.pipe ; mkfifo ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased.pipe ; head -c 1048576 < ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased.pipe >> ../files/ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased.sim & ./ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased  -abortSlowSimulation -alarm=1200  -emit_protected -lv LOG_STATS > ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased.pipe 2>&1) [Timeout 1200]
diffSimulationResults("ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat","/mnt/ReferenceFiles/ThermofluidStream-main-regression/ReferenceData/ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_ref.mat","/var/lib/jenkins/ws/OpenModelicaLibraryTestingWork/OpenModelicaLibraryTesting/files/ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased.diff",relTol=0.003,relTolDiffMinMax=0.003,rangeDelta=0.001) [Timeout 660]
"Error: Could not read variable CPUtime in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat.
Warning: Get data of variable CPUtime from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat failed!
Error: Could not read variable EventCounter in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat.
Warning: Get data of variable EventCounter from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat failed!
Error: Could not read variable _derdummy in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat.
Warning: Get data of variable _derdummy from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat failed!
Error: Could not read variable _dummy in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat.
Warning: Get data of variable _dummy from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat failed!
Error: Could not read variable dropOfCommons.instanceNameColor[1] in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat.
Warning: Get data of variable dropOfCommons.instanceNameColor[1] from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat failed!
Error: Could not read variable dropOfCommons.instanceNameColor[2] in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat.
Warning: Get data of variable dropOfCommons.instanceNameColor[2] from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat failed!
Error: Could not read variable dropOfCommons.instanceNameColor[3] in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat.
Warning: Get data of variable dropOfCommons.instanceNameColor[3] from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat failed!
Error: Could not read variable fullMedium.P_nom in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat.
Warning: Get data of variable fullMedium.P_nom from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat failed!
Error: Could not read variable fullMedium.TC in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat.
Warning: Get data of variable fullMedium.TC from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat failed!
Error: Could not read variable fullMedium.assertionLevel in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat.
Warning: Get data of variable fullMedium.assertionLevel from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat failed!
Error: Could not read variable fullMedium.dp_fixed in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat.
Warning: Get data of variable fullMedium.dp_fixed from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat failed!
Error: Could not read variable fullMedium.dp_nom in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat.
Warning: Get data of variable fullMedium.dp_nom from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat failed!
Error: Could not read variable fullMedium.dp_start in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat.
Warning: Get data of variable fullMedium.dp_start from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat failed!
Error: Could not read variable fullMedium.inlet.der(m_flow) in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat.
Warning: Get data of variable fullMedium.inlet.der(m_flow) from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat failed!
Error: Could not read variable fullMedium.pRatio_fixed in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat.
Warning: Get data of variable fullMedium.pRatio_fixed from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat failed!
Error: Could not read variable fullMedium.p_out_fixed in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat.
Warning: Get data of variable fullMedium.p_out_fixed from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat failed!
Error: Could not read variable incompressibleFluid.P_nom in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat.
Warning: Get data of variable incompressibleFluid.P_nom from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat failed!
Error: Could not read variable incompressibleFluid.TC in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat.
Warning: Get data of variable incompressibleFluid.TC from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat failed!
Error: Could not read variable incompressibleFluid.assertionLevel in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat.
Warning: Get data of variable incompressibleFluid.assertionLevel from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat failed!
Error: Could not read variable incompressibleFluid.dp_fixed in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat.
Warning: Get data of variable incompressibleFluid.dp_fixed from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat failed!
Error: Could not read variable incompressibleFluid.dp_nom in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat.
Warning: Get data of variable incompressibleFluid.dp_nom from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat failed!
Error: Could not read variable incompressibleFluid.dp_start in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat.
Warning: Get data of variable incompressibleFluid.dp_start from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat failed!
Error: Could not read variable incompressibleFluid.inlet.der(m_flow) in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat.
Warning: Get data of variable incompressibleFluid.inlet.der(m_flow) from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat failed!
Error: Could not read variable incompressibleFluid.pRatio_fixed in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat.
Warning: Get data of variable incompressibleFluid.pRatio_fixed from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat failed!
Error: Could not read variable incompressibleFluid.p_out_fixed in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat.
Warning: Get data of variable incompressibleFluid.p_out_fixed from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat failed!
Error: Could not read variable isothermalReference.P_nom in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat.
Warning: Get data of variable isothermalReference.P_nom from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat failed!
Error: Could not read variable isothermalReference.TC in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat.
Warning: Get data of variable isothermalReference.TC from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat failed!
Error: Could not read variable isothermalReference.assertionLevel in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat.
Warning: Get data of variable isothermalReference.assertionLevel from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat failed!
Error: Could not read variable isothermalReference.dp_fixed in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat.
Warning: Get data of variable isothermalReference.dp_fixed from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat failed!
Error: Could not read variable isothermalReference.dp_nom in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat.
Warning: Get data of variable isothermalReference.dp_nom from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat failed!
Error: Could not read variable isothermalReference.dp_start in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat.
Warning: Get data of variable isothermalReference.dp_start from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat failed!
Error: Could not read variable isothermalReference.inlet.der(m_flow) in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat.
Warning: Get data of variable isothermalReference.inlet.der(m_flow) from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat failed!
Error: Could not read variable isothermalReference.pRatio_fixed in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat.
Warning: Get data of variable isothermalReference.pRatio_fixed from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat failed!
Error: Could not read variable isothermalReference.p_out_fixed in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat.
Warning: Get data of variable isothermalReference.p_out_fixed from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat failed!
Error: Could not read variable sink.inlet.der(m_flow) in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat.
Warning: Get data of variable sink.inlet.der(m_flow) from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat failed!
Error: Could not read variable sink1.inlet.der(m_flow) in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat.
Warning: Get data of variable sink1.inlet.der(m_flow) from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat failed!
Error: Could not read variable sink2.inlet.der(m_flow) in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat.
Warning: Get data of variable sink2.inlet.der(m_flow) from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat failed!
Error: Could not read variable source.outlet.der(m_flow) in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat.
Warning: Get data of variable source.outlet.der(m_flow) from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat failed!
Error: Could not read variable source1.outlet.der(m_flow) in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat.
Warning: Get data of variable source1.outlet.der(m_flow) from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat failed!
Error: Could not read variable source2.outlet.der(m_flow) in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat.
Warning: Get data of variable source2.outlet.der(m_flow) from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat failed!
"
[Timeout remaining time 660]
""

Variables in the reference:CPUtime,EventCounter,Time,_derdummy,_dummy,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,eta,fullMedium.L,fullMedium.P,fullMedium.P_nom,fullMedium.TC,fullMedium.adiabaticModel.eta_is,fullMedium.adiabaticModel.h_in,fullMedium.adiabaticModel.h_out,fullMedium.adiabaticModel.h_out_is,fullMedium.adiabaticModel.p_out,fullMedium.adiabaticModel.s_in,fullMedium.adiabaticModel.state_in.T,fullMedium.adiabaticModel.state_in.p,fullMedium.adiabaticModel.w_t,fullMedium.adiabaticModel.w_t_is,fullMedium.assertionLevel,fullMedium.clip_p_out,fullMedium.dh,fullMedium.dp,fullMedium.dp_fixed,fullMedium.dp_nom,fullMedium.dp_start,fullMedium.dr_corr,fullMedium.etaSpec,fullMedium.eta_actual,fullMedium.eta_fixed,fullMedium.eta_is,fullMedium.h_in,fullMedium.h_out,fullMedium.initM_flow,der(fullMedium.inlet.m_flow),fullMedium.inlet.m_flow,fullMedium.inlet.r,fullMedium.inlet.state.T,fullMedium.inlet.state.p,fullMedium.m_acceleration_0,fullMedium.m_flow,fullMedium.m_flowStateSelect,fullMedium.m_flow_0,fullMedium.outlet.m_flow,fullMedium.outlet.r,fullMedium.outlet.state.T,fullMedium.outlet.state.p,fullMedium.outletSpec,fullMedium.outletSpec_actual,fullMedium.outletSpec_prescribed,fullMedium.outletValueSpec,fullMedium.pRatio,fullMedium.pRatio_fixed,fullMedium.p_in,fullMedium.p_min,fullMedium.p_out,fullMedium.p_out_fixed,fullMedium.singularityRegime,incompressibleFluid.L,incompressibleFluid.P,incompressibleFluid.P_nom,incompressibleFluid.TC,incompressibleFluid.adiabaticModel.T_in,incompressibleFluid.adiabaticModel.T_out_is,incompressibleFluid.adiabaticModel.assertionLevel,incompressibleFluid.adiabaticModel.deltaDensityRel,incompressibleFluid.adiabaticModel.eta_is,incompressibleFluid.adiabaticModel.h_in,incompressibleFluid.adiabaticModel.h_out,incompressibleFluid.adiabaticModel.isDensityWithinTol,incompressibleFluid.adiabaticModel.p_out,incompressibleFluid.adiabaticModel.relTolDensity,incompressibleFluid.adiabaticModel.rho_in,incompressibleFluid.adiabaticModel.rho_out,incompressibleFluid.adiabaticModel.state_in.T,incompressibleFluid.adiabaticModel.state_in.p,incompressibleFluid.adiabaticModel.w_t,incompressibleFluid.adiabaticModel.w_t_is,incompressibleFluid.assertionLevel,incompressibleFluid.clip_p_out,incompressibleFluid.dh,incompressibleFluid.dp,incompressibleFluid.dp_fixed,incompressibleFluid.dp_nom,incompressibleFluid.dp_start,incompressibleFluid.dr_corr,incompressibleFluid.etaSpec,incompressibleFluid.eta_actual,incompressibleFluid.eta_fixed,incompressibleFluid.eta_is,incompressibleFluid.h_in,incompressibleFluid.h_out,incompressibleFluid.initM_flow,der(incompressibleFluid.inlet.m_flow),incompressibleFluid.inlet.m_flow,incompressibleFluid.inlet.r,incompressibleFluid.inlet.state.T,incompressibleFluid.inlet.state.p,incompressibleFluid.m_acceleration_0,incompressibleFluid.m_flow,incompressibleFluid.m_flowStateSelect,incompressibleFluid.m_flow_0,incompressibleFluid.outlet.m_flow,incompressibleFluid.outlet.r,incompressibleFluid.outlet.state.T,incompressibleFluid.outlet.state.p,incompressibleFluid.outletSpec,incompressibleFluid.outletSpec_actual,incompressibleFluid.outletSpec_prescribed,incompressibleFluid.outletValueSpec,incompressibleFluid.pRatio,incompressibleFluid.pRatio_fixed,incompressibleFluid.p_in,incompressibleFluid.p_min,incompressibleFluid.p_out,incompressibleFluid.p_out_fixed,incompressibleFluid.singularityRegime,isothermalReference.L,isothermalReference.P,isothermalReference.P_nom,isothermalReference.TC,isothermalReference.adiabaticModel.T_in,isothermalReference.adiabaticModel.T_out_is,isothermalReference.adiabaticModel.assertionLevel,isothermalReference.adiabaticModel.deltaDensityRel,isothermalReference.adiabaticModel.eta_is,isothermalReference.adiabaticModel.h_in,isothermalReference.adiabaticModel.h_out,isothermalReference.adiabaticModel.h_out_is,isothermalReference.adiabaticModel.isDensityWithinTol,isothermalReference.adiabaticModel.p_out,isothermalReference.adiabaticModel.relTolDensity,isothermalReference.adiabaticModel.rho_in,isothermalReference.adiabaticModel.rho_out,isothermalReference.adiabaticModel.state_in.T,isothermalReference.adiabaticModel.state_in.p,isothermalReference.adiabaticModel.w_t,isothermalReference.adiabaticModel.w_t_is,isothermalReference.assertionLevel,isothermalReference.clip_p_out,isothermalReference.dh,isothermalReference.dp,isothermalReference.dp_fixed,isothermalReference.dp_nom,isothermalReference.dp_start,isothermalReference.dr_corr,isothermalReference.etaSpec,isothermalReference.eta_actual,isothermalReference.eta_fixed,isothermalReference.eta_is,isothermalReference.h_in,isothermalReference.h_out,isothermalReference.initM_flow,der(isothermalReference.inlet.m_flow),isothermalReference.inlet.m_flow,isothermalReference.inlet.r,isothermalReference.inlet.state.T,isothermalReference.inlet.state.p,isothermalReference.m_acceleration_0,isothermalReference.m_flow,isothermalReference.m_flowStateSelect,isothermalReference.m_flow_0,isothermalReference.outlet.m_flow,isothermalReference.outlet.r,isothermalReference.outlet.state.T,isothermalReference.outlet.state.p,isothermalReference.outletSpec,isothermalReference.outletSpec_actual,isothermalReference.outletSpec_prescribed,isothermalReference.outletValueSpec,isothermalReference.pRatio,isothermalReference.pRatio_fixed,isothermalReference.p_in,isothermalReference.p_min,isothermalReference.p_out,isothermalReference.p_out_fixed,isothermalReference.singularityRegime,pressureDifference.duration,pressureDifference.height,pressureDifference.offset,pressureDifference.startTime,pressureDifference.y,sink.L,der(sink.inlet.m_flow),sink.inlet.m_flow,sink.inlet.r,sink.inlet.state.T,sink.inlet.state.p,sink.m_flow,sink.m_flowSpec,sink.m_flow_fixed,sink1.L,der(sink1.inlet.m_flow),sink1.inlet.m_flow,sink1.inlet.r,sink1.inlet.state.T,sink1.inlet.state.p,sink1.m_flow,sink1.m_flowSpec,sink1.m_flow_fixed,sink2.L,der(sink2.inlet.m_flow),sink2.inlet.m_flow,sink2.inlet.r,sink2.inlet.state.T,sink2.inlet.state.p,sink2.m_flow,sink2.m_flowSpec,sink2.m_flow_fixed,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

Variables in the result:dropOfCommons.L,dropOfCommons.assertionLevel,dropOfCommons.g,dropOfCommons.k_volume_damping,dropOfCommons.m_flow_reg,dropOfCommons.omega_reg,dropOfCommons.p_min,dropOfCommons.rho_min,eta,fullMedium.L,fullMedium.P,fullMedium.P_in_internal,fullMedium.adiabaticModel.eta_is,fullMedium.adiabaticModel.h_in,fullMedium.adiabaticModel.h_out,fullMedium.adiabaticModel.h_out_is,fullMedium.adiabaticModel.p_out,fullMedium.adiabaticModel.s_in,fullMedium.adiabaticModel.state_in.T,fullMedium.adiabaticModel.state_in.p,fullMedium.adiabaticModel.w_t,fullMedium.adiabaticModel.w_t_is,fullMedium.clip_p_out,fullMedium.dh,fullMedium.dp,fullMedium.dr_corr,fullMedium.etaSpec,fullMedium.eta_actual,fullMedium.eta_fixed,fullMedium.eta_is,fullMedium.h_in,fullMedium.h_out,fullMedium.initM_flow,fullMedium.inlet.m_flow,fullMedium.inlet.r,fullMedium.inlet.state.T,fullMedium.inlet.state.p,fullMedium.m_acceleration_0,fullMedium.m_flow,fullMedium.m_flowStateSelect,fullMedium.m_flow_0,fullMedium.outlet.m_flow,fullMedium.outlet.r,fullMedium.outlet.state.T,fullMedium.outlet.state.p,fullMedium.outletSpec,fullMedium.outletSpec_actual,fullMedium.outletSpec_prescribed,fullMedium.outletValueSpec,fullMedium.pRatio,fullMedium.p_in,fullMedium.p_min,fullMedium.p_out,fullMedium.singularityRegime,incompressibleFluid.L,incompressibleFluid.P,incompressibleFluid.P_in_internal,incompressibleFluid.adiabaticModel.T_in,incompressibleFluid.adiabaticModel.T_out_is,incompressibleFluid.adiabaticModel.assertionLevel,incompressibleFluid.adiabaticModel.deltaDensityRel,incompressibleFluid.adiabaticModel.eta_is,incompressibleFluid.adiabaticModel.h_in,incompressibleFluid.adiabaticModel.h_out,incompressibleFluid.adiabaticModel.isDensityWithinTol,incompressibleFluid.adiabaticModel.p_out,incompressibleFluid.adiabaticModel.relTolDensity,incompressibleFluid.adiabaticModel.rho_in,incompressibleFluid.adiabaticModel.rho_out,incompressibleFluid.adiabaticModel.state_in.T,incompressibleFluid.adiabaticModel.state_in.p,incompressibleFluid.adiabaticModel.w_t,incompressibleFluid.adiabaticModel.w_t_is,incompressibleFluid.clip_p_out,incompressibleFluid.dh,incompressibleFluid.dp,incompressibleFluid.dr_corr,incompressibleFluid.etaSpec,incompressibleFluid.eta_actual,incompressibleFluid.eta_fixed,incompressibleFluid.eta_is,incompressibleFluid.h_in,incompressibleFluid.h_out,incompressibleFluid.initM_flow,incompressibleFluid.inlet.m_flow,incompressibleFluid.inlet.r,incompressibleFluid.inlet.state.T,incompressibleFluid.inlet.state.p,incompressibleFluid.m_acceleration_0,incompressibleFluid.m_flow,incompressibleFluid.m_flowStateSelect,incompressibleFluid.m_flow_0,incompressibleFluid.outlet.m_flow,incompressibleFluid.outlet.r,incompressibleFluid.outlet.state.T,incompressibleFluid.outlet.state.p,incompressibleFluid.outletSpec,incompressibleFluid.outletSpec_actual,incompressibleFluid.outletSpec_prescribed,incompressibleFluid.outletValueSpec,incompressibleFluid.pRatio,incompressibleFluid.p_in,incompressibleFluid.p_min,incompressibleFluid.p_out,incompressibleFluid.singularityRegime,isothermalReference.L,isothermalReference.P,isothermalReference.P_in_internal,isothermalReference.adiabaticModel.T_in,isothermalReference.adiabaticModel.T_out_is,isothermalReference.adiabaticModel.assertionLevel,isothermalReference.adiabaticModel.deltaDensityRel,isothermalReference.adiabaticModel.eta_is,isothermalReference.adiabaticModel.h_in,isothermalReference.adiabaticModel.h_out,isothermalReference.adiabaticModel.h_out_is,isothermalReference.adiabaticModel.isDensityWithinTol,isothermalReference.adiabaticModel.p_out,isothermalReference.adiabaticModel.relTolDensity,isothermalReference.adiabaticModel.rho_in,isothermalReference.adiabaticModel.rho_out,isothermalReference.adiabaticModel.state_in.T,isothermalReference.adiabaticModel.state_in.p,isothermalReference.adiabaticModel.w_t,isothermalReference.adiabaticModel.w_t_is,isothermalReference.clip_p_out,isothermalReference.dh,isothermalReference.dp,isothermalReference.dr_corr,isothermalReference.etaSpec,isothermalReference.eta_actual,isothermalReference.eta_fixed,isothermalReference.eta_is,isothermalReference.h_in,isothermalReference.h_out,isothermalReference.initM_flow,isothermalReference.inlet.m_flow,isothermalReference.inlet.r,isothermalReference.inlet.state.T,isothermalReference.inlet.state.p,isothermalReference.m_acceleration_0,isothermalReference.m_flow,isothermalReference.m_flowStateSelect,isothermalReference.m_flow_0,isothermalReference.outlet.m_flow,isothermalReference.outlet.r,isothermalReference.outlet.state.T,isothermalReference.outlet.state.p,isothermalReference.outletSpec,isothermalReference.outletSpec_actual,isothermalReference.outletSpec_prescribed,isothermalReference.outletValueSpec,isothermalReference.pRatio,isothermalReference.p_in,isothermalReference.p_min,isothermalReference.p_out,isothermalReference.singularityRegime,pressureDifference.duration,pressureDifference.height,pressureDifference.offset,pressureDifference.startTime,pressureDifference.y,sink.L,sink.inlet.m_flow,sink.inlet.r,sink.inlet.state.T,sink.inlet.state.p,sink.m_flow,sink.m_flowSpec,sink.m_flow_fixed,sink1.L,sink1.inlet.m_flow,sink1.inlet.r,sink1.inlet.state.T,sink1.inlet.state.p,sink1.m_flow,sink1.m_flowSpec,sink1.m_flow_fixed,sink2.L,sink2.inlet.m_flow,sink2.inlet.r,sink2.inlet.state.T,sink2.inlet.state.p,sink2.m_flow,sink2.m_flowSpec,sink2.m_flow_fixed,source.L,source.T0,source.T0_par,source.h0,source.h0_par,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,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,source2.outlet.m_flow,source2.outlet.r,source2.outlet.state.T,source2.outlet.state.p,source2.p0,source2.p0_par,time
[Calling sys.exit(0), Time elapsed: 6.15439610555768]