Running: ./testmodel.py --libraries=/home/hudson/saved_omc/libraries/.openmodelica/libraries --ompython_omhome=/usr ThermofluidStream_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 0.001444/0.001444, allocations: 101.5 kB / 18.95 MB, free: 1.184 MB / 13.93 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 0.001566/0.001566, allocations: 218.3 kB / 22.25 MB, free: 3.57 MB / 13.93 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 1.559/1.559, allocations: 230.6 MB / 256 MB, free: 9.613 MB / 202.7 MB
"
[Timeout remaining time 178]
loadFile("/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermofluidStream 1.4.0/package.mo", uses=false) [Timeout 180]
"Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermofluidStream 1.4.0/package.mo): time 1.073/1.073, allocations: 154.1 MB / 466.6 MB, free: 3.305 MB / 362.7 MB
"
[Timeout remaining time 179]
Using package ThermofluidStream with version 1.4.0 (/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermofluidStream 1.4.0/package.mo)
Using package Modelica with version 4.1.0 (/home/hudson/saved_omc/libraries/.openmodelica/libraries/Modelica 4.1.0+maint.om/package.mo)
Using package Complex with version 4.1.0 (/home/hudson/saved_omc/libraries/.openmodelica/libraries/Complex 4.1.0+maint.om/package.mo)
Using package ModelicaServices with version 4.1.0 (/home/hudson/saved_omc/libraries/.openmodelica/libraries/ModelicaServices 4.1.0+maint.om/package.mo)
Running command: translateModel(ThermofluidStream.Idealized.Examples.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_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_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased") [Timeout 660]
"Notification: Performance of FrontEnd - loaded program: time 0.002767/0.002767, allocations: 88.16 kB / 0.6443 GB, free: 27.7 MB / 490.7 MB
Notification: Performance of FrontEnd - Absyn->SCode: time 0.1561/0.1589, allocations: 88.77 MB / 0.731 GB, free: 2.738 MB / 0.5417 GB
Notification: Performance of NFInst.instantiate(ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased): time 0.06452/0.2234, allocations: 43.92 MB / 0.7738 GB, free: 6.66 MB / 0.5886 GB
Notification: Performance of NFInst.instExpressions: time 0.005213/0.2286, allocations: 2.53 MB / 0.7763 GB, free: 4.125 MB / 0.5886 GB
Notification: Performance of NFInst.updateImplicitVariability: time 0.0006706/0.2293, allocations: 71.31 kB / 0.7764 GB, free: 4.055 MB / 0.5886 GB
Notification: Performance of NFTyping.typeComponents: time 0.00112/0.2304, allocations: 381.2 kB / 0.7768 GB, free: 3.68 MB / 0.5886 GB
Notification: Performance of NFTyping.typeBindings: time 0.00646/0.2369, allocations: 2.399 MB / 0.7791 GB, free: 1.273 MB / 0.5886 GB
Notification: Performance of NFTyping.typeClassSections: time 0.003677/0.2405, allocations: 1.274 MB / 0.7803 GB, free: 15.99 MB / 0.6042 GB
Notification: Performance of NFFlatten.flatten: time 0.002448/0.243, allocations: 1.491 MB / 0.7818 GB, free: 14.5 MB / 0.6042 GB
Notification: Performance of NFFlatten.resolveConnections: time 0.0003409/0.2433, allocations: 127.8 kB / 0.7819 GB, free: 14.35 MB / 0.6042 GB
Notification: Performance of NFEvalConstants.evaluate: time 0.005377/0.2487, allocations: 2.669 MB / 0.7845 GB, free: 11.68 MB / 0.6042 GB
Notification: Performance of NFSimplifyModel.simplify: time 0.0007584/0.2495, allocations: 441.5 kB / 0.7849 GB, free: 11.24 MB / 0.6042 GB
Notification: Performance of NFPackage.collectConstants: time 0.0001092/0.2496, allocations: 56 kB / 0.785 GB, free: 11.19 MB / 0.6042 GB
Notification: Performance of NFFlatten.collectFunctions: time 0.009299/0.2589, allocations: 4.513 MB / 0.7894 GB, free: 6.668 MB / 0.6042 GB
Notification: Performance of NFScalarize.scalarize: time 0.0002455/0.2591, allocations: 171 kB / 0.7896 GB, free: 6.5 MB / 0.6042 GB
Notification: Performance of NFVerifyModel.verify: time 0.0005259/0.2596, allocations: 377.8 kB / 0.7899 GB, free: 6.129 MB / 0.6042 GB
Notification: Performance of NFConvertDAE.convert: time 0.003942/0.2636, allocations: 2.063 MB / 0.7919 GB, free: 4.059 MB / 0.6042 GB
Notification: Performance of FrontEnd - DAE generated: time 3.867e-06/0.2636, allocations: 0 / 0.7919 GB, free: 4.059 MB / 0.6042 GB
Notification: Performance of FrontEnd: time 1.433e-06/0.2636, allocations: 0 / 0.7919 GB, free: 4.059 MB / 0.6042 GB
Notification: Performance of Transformations before backend: time 1.277e-05/0.2636, allocations: 0 / 0.7919 GB, free: 4.059 MB / 0.6042 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 0.002599/0.2662, allocations: 1.464 MB / 0.7934 GB, free: 2.559 MB / 0.6042 GB
Notification: Performance of prepare preOptimizeDAE: time 4.046e-05/0.2662, allocations: 8.031 kB / 0.7934 GB, free: 2.551 MB / 0.6042 GB
Notification: Performance of preOpt normalInlineFunction (simulation): time 0.001181/0.2674, allocations: 208 kB / 0.7936 GB, free: 2.348 MB / 0.6042 GB
Notification: Performance of preOpt evaluateParameters (simulation): time 0.001786/0.2692, allocations: 0.7337 MB / 0.7943 GB, free: 1.582 MB / 0.6042 GB
Notification: Performance of preOpt simplifyIfEquations (simulation): time 0.0002435/0.2694, allocations: 207.8 kB / 0.7945 GB, free: 1.344 MB / 0.6042 GB
Notification: Performance of preOpt expandDerOperator (simulation): time 0.0001195/0.2696, allocations: 63.95 kB / 0.7946 GB, free: 1.281 MB / 0.6042 GB
Notification: Performance of preOpt clockPartitioning (simulation): time 0.001537/0.2711, allocations: 0.6937 MB / 0.7952 GB, free: 0.5469 MB / 0.6042 GB
Notification: Performance of preOpt findStateOrder (simulation): time 1.987e-05/0.2711, allocations: 0 / 0.7952 GB, free: 0.5469 MB / 0.6042 GB
Notification: Performance of preOpt replaceEdgeChange (simulation): time 6.006e-05/0.2712, allocations: 28 kB / 0.7953 GB, free: 0.5195 MB / 0.6042 GB
Notification: Performance of preOpt inlineArrayEqn (simulation): time 2.213e-05/0.2712, allocations: 20 kB / 0.7953 GB, free: 0.5 MB / 0.6042 GB
Notification: Performance of preOpt removeEqualRHS (simulation): time 0.001268/0.2725, allocations: 480.9 kB / 0.7957 GB, free: 32 kB / 0.6042 GB
Notification: Performance of preOpt removeSimpleEquations (simulation): time 0.003581/0.2761, allocations: 2.095 MB / 0.7978 GB, free: 13.84 MB / 0.6198 GB
Notification: Performance of preOpt comSubExp (simulation): time 0.001446/0.2775, allocations: 399.9 kB / 0.7982 GB, free: 13.45 MB / 0.6198 GB
Notification: Performance of preOpt resolveLoops (simulation): time 0.0004265/0.2779, allocations: 149.3 kB / 0.7983 GB, free: 13.3 MB / 0.6198 GB
Notification: Performance of preOpt evalFunc (simulation): time 0.0004427/0.2784, allocations: 120.2 kB / 0.7984 GB, free: 13.18 MB / 0.6198 GB
Notification: Performance of preOpt encapsulateWhenConditions (simulation): time 3.777e-05/0.2784, allocations: 34.84 kB / 0.7985 GB, free: 13.14 MB / 0.6198 GB
Notification: Performance of pre-optimization done (n=34): time 2.014e-06/0.2784, allocations: 0 / 0.7985 GB, free: 13.14 MB / 0.6198 GB
Notification: Performance of matching and sorting (n=34): time 0.001573/0.28, allocations: 494.2 kB / 0.7989 GB, free: 12.65 MB / 0.6198 GB
Notification: Performance of inlineWhenForInitialization (initialization): time 5.153e-05/0.28, allocations: 55.41 kB / 0.799 GB, free: 12.58 MB / 0.6198 GB
Notification: Performance of selectInitializationVariablesDAE (initialization): time 0.000972/0.281, allocations: 0.685 MB / 0.7996 GB, free: 11.89 MB / 0.6198 GB
Notification: Performance of collectPreVariables (initialization): time 3.978e-05/0.281, allocations: 29.7 kB / 0.7997 GB, free: 11.85 MB / 0.6198 GB
Notification: Performance of collectInitialEqns (initialization): time 0.0004597/0.2815, allocations: 492.2 kB / 0.8001 GB, free: 11.37 MB / 0.6198 GB
Notification: Performance of collectInitialBindings (initialization): time 0.0001277/0.2816, allocations: 123.1 kB / 0.8003 GB, free: 11.25 MB / 0.6198 GB
Notification: Performance of simplifyInitialFunctions (initialization): time 0.0001561/0.2818, allocations: 86.08 kB / 0.8003 GB, free: 11.16 MB / 0.6198 GB
Notification: Performance of setup shared object (initialization): time 0.0004089/0.2822, allocations: 329.9 kB / 0.8007 GB, free: 10.83 MB / 0.6198 GB
Notification: Performance of preBalanceInitialSystem (initialization): time 0.0003385/0.2825, allocations: 120.8 kB / 0.8008 GB, free: 10.71 MB / 0.6198 GB
Notification: Performance of partitionIndependentBlocks (initialization): time 0.0004186/0.283, allocations: 200.9 kB / 0.801 GB, free: 10.48 MB / 0.6198 GB
Notification: Performance of analyzeInitialSystem (initialization): time 0.0007797/0.2837, allocations: 339.9 kB / 0.8013 GB, free: 10.12 MB / 0.6198 GB
Notification: Performance of solveInitialSystemEqSystem (initialization): time 2.594e-06/0.2837, allocations: 0 / 0.8013 GB, free: 10.12 MB / 0.6198 GB
Notification: Performance of matching and sorting (n=51) (initialization): time 0.001068/0.2848, allocations: 476.5 kB / 0.8017 GB, free: 9.648 MB / 0.6198 GB
Notification: Performance of prepare postOptimizeDAE: time 1.98e-05/0.2848, allocations: 8.938 kB / 0.8018 GB, free: 9.641 MB / 0.6198 GB
Notification: Performance of postOpt simplifyComplexFunction (initialization): time 6.552e-06/0.2848, allocations: 3.938 kB / 0.8018 GB, free: 9.637 MB / 0.6198 GB
Notification: Performance of postOpt tearingSystem (initialization): time 1.947e-05/0.2848, allocations: 4 kB / 0.8018 GB, free: 9.633 MB / 0.6198 GB
Notification: Performance of postOpt solveSimpleEquations (initialization): time 0.0004364/0.2853, allocations: 99.88 kB / 0.8019 GB, free: 9.535 MB / 0.6198 GB
Notification: Performance of postOpt calculateStrongComponentJacobians (initialization): time 1.213e-05/0.2853, allocations: 8 kB / 0.8019 GB, free: 9.527 MB / 0.6198 GB
Notification: Performance of postOpt simplifyAllExpressions (initialization): time 0.0003009/0.2856, allocations: 47.66 kB / 0.8019 GB, free: 9.48 MB / 0.6198 GB
Notification: Performance of postOpt collapseArrayExpressions (initialization): time 5.618e-05/0.2857, allocations: 23.98 kB / 0.8019 GB, free: 9.457 MB / 0.6198 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 0.0003088/0.286, allocations: 201.8 kB / 0.8021 GB, free: 9.25 MB / 0.6198 GB
Notification: Performance of postOpt lateInlineFunction (simulation): time 0.000149/0.2861, allocations: 83.44 kB / 0.8022 GB, free: 9.168 MB / 0.6198 GB
Notification: Performance of postOpt wrapFunctionCalls (simulation): time 0.001451/0.2876, allocations: 0.6029 MB / 0.8028 GB, free: 8.559 MB / 0.6198 GB
Notification: Performance of postOpt inlineArrayEqn (simulation): time 9.478e-06/0.2876, allocations: 4 kB / 0.8028 GB, free: 8.555 MB / 0.6198 GB
Notification: Performance of postOpt constantLinearSystem (simulation): time 4.057e-06/0.2876, allocations: 0 / 0.8028 GB, free: 8.555 MB / 0.6198 GB
Notification: Performance of postOpt simplifysemiLinear (simulation): time 7.294e-06/0.2876, allocations: 3.984 kB / 0.8028 GB, free: 8.551 MB / 0.6198 GB
Notification: Performance of postOpt removeSimpleEquations (simulation): time 0.0007225/0.2883, allocations: 480.8 kB / 0.8033 GB, free: 8.051 MB / 0.6198 GB
Notification: Performance of postOpt simplifyComplexFunction (simulation): time 5.931e-06/0.2883, allocations: 4 kB / 0.8033 GB, free: 8.047 MB / 0.6198 GB
Notification: Performance of postOpt solveSimpleEquations (simulation): time 0.0003408/0.2887, allocations: 79.89 kB / 0.8033 GB, free: 7.969 MB / 0.6198 GB
Notification: Performance of postOpt tearingSystem (simulation): time 8.205e-06/0.2887, allocations: 4 kB / 0.8033 GB, free: 7.965 MB / 0.6198 GB
Notification: Performance of postOpt inputDerivativesUsed (simulation): time 3.074e-05/0.2887, allocations: 11.98 kB / 0.8034 GB, free: 7.953 MB / 0.6198 GB
Notification: Performance of postOpt calculateStrongComponentJacobians (simulation): time 2.415e-06/0.2887, allocations: 0 / 0.8034 GB, free: 7.953 MB / 0.6198 GB
Notification: Performance of postOpt calculateStateSetsJacobians (simulation): time 1.402e-06/0.2887, allocations: 3.938 kB / 0.8034 GB, free: 7.949 MB / 0.6198 GB
Notification: Performance of postOpt symbolicJacobian (simulation): time 0.0009253/0.2896, allocations: 437 kB / 0.8038 GB, free: 7.504 MB / 0.6198 GB
Notification: Performance of postOpt removeConstants (simulation): time 0.0002296/0.2898, allocations: 111.3 kB / 0.8039 GB, free: 7.395 MB / 0.6198 GB
Notification: Performance of postOpt simplifyTimeIndepFuncCalls (simulation): time 7.839e-05/0.2899, allocations: 4 kB / 0.8039 GB, free: 7.391 MB / 0.6198 GB
Notification: Performance of postOpt simplifyAllExpressions (simulation): time 0.0002491/0.2902, allocations: 23.98 kB / 0.8039 GB, free: 7.367 MB / 0.6198 GB
Notification: Performance of postOpt findZeroCrossings (simulation): time 9.027e-05/0.2903, allocations: 31.7 kB / 0.8039 GB, free: 7.336 MB / 0.6198 GB
Notification: Performance of postOpt collapseArrayExpressions (simulation): time 4.085e-05/0.2903, allocations: 15.98 kB / 0.804 GB, free: 7.32 MB / 0.6198 GB
Notification: Performance of sorting global known variables: time 0.0006579/0.291, allocations: 467 kB / 0.8044 GB, free: 6.871 MB / 0.6198 GB
Notification: Performance of sort global known variables: time 1.21e-07/0.291, allocations: 4 kB / 0.8044 GB, free: 6.867 MB / 0.6198 GB
Notification: Performance of remove unused functions: time 0.001013/0.292, allocations: 362.9 kB / 0.8047 GB, free: 6.512 MB / 0.6198 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 0.0009876/0.293, allocations: 495.1 kB / 0.8052 GB, free: 6.023 MB / 0.6198 GB
Notification: Performance of simCode: created initialization part: time 0.0008708/0.2938, allocations: 307.8 kB / 0.8055 GB, free: 5.723 MB / 0.6198 GB
Notification: Performance of simCode: created event and clocks part: time 2.865e-06/0.2938, allocations: 0 / 0.8055 GB, free: 5.723 MB / 0.6198 GB
Notification: Performance of simCode: created simulation system equations: time 0.0003833/0.2942, allocations: 151.8 kB / 0.8057 GB, free: 5.574 MB / 0.6198 GB
Notification: Performance of simCode: created of all other equations (e.g. parameter, nominal, assert, etc): time 0.001475/0.2957, allocations: 325.6 kB / 0.806 GB, free: 5.281 MB / 0.6198 GB
Notification: Performance of simCode: created linear, non-linear and system jacobian parts: time 0.00257/0.2983, allocations: 1.334 MB / 0.8073 GB, free: 3.91 MB / 0.6198 GB
Notification: Performance of simCode: some other stuff during SimCode phase: time 0.0006878/0.299, allocations: 388.1 kB / 0.8076 GB, free: 3.5 MB / 0.6198 GB
Notification: Performance of simCode: alias equations: time 0.0005935/0.2995, allocations: 220.4 kB / 0.8079 GB, free: 3.293 MB / 0.6198 GB
Notification: Performance of simCode: all other stuff during SimCode phase: time 0.0001832/0.2997, allocations: 75.39 kB / 0.8079 GB, free: 3.219 MB / 0.6198 GB
Notification: Performance of SimCode: time 5.81e-07/0.2997, allocations: 0 / 0.8079 GB, free: 3.219 MB / 0.6198 GB
Notification: Performance of Templates: time 0.03106/0.3308, allocations: 15.96 MB / 0.8235 GB, free: 3.555 MB / 0.6355 GB
"
[Timeout remaining time 660]
make -j1 -f ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased.makefile [Timeout 660]
(rm -f ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased.pipe ; mkfifo ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased.pipe ; head -c 1048576 < ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased.pipe >> ../files/ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased.sim & ./ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased  -abortSlowSimulation -alarm=1200  -emit_protected -lv LOG_STATS > ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased.pipe 2>&1) [Timeout 1200]
diffSimulationResults("ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat","/mnt/ReferenceFiles/ThermofluidStream-main-regression/ReferenceData/ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_ref.mat","/var/lib/jenkins1/ws/OpenModelicaLibraryTestingWork/OpenModelicaLibraryTesting/files/ThermofluidStream_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_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat.
Warning: Get data of variable CPUtime from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat failed!
Error: Could not read variable EventCounter in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat.
Warning: Get data of variable EventCounter from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat failed!
Error: Could not read variable _derdummy in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat.
Warning: Get data of variable _derdummy from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat failed!
Error: Could not read variable _dummy in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat.
Warning: Get data of variable _dummy from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat failed!
Error: Could not read variable dropOfCommons.instanceNameColor[1] in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat.
Warning: Get data of variable dropOfCommons.instanceNameColor[1] from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat failed!
Error: Could not read variable dropOfCommons.instanceNameColor[2] in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat.
Warning: Get data of variable dropOfCommons.instanceNameColor[2] from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat failed!
Error: Could not read variable dropOfCommons.instanceNameColor[3] in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat.
Warning: Get data of variable dropOfCommons.instanceNameColor[3] from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat failed!
Error: Could not read variable fullMedium.P_nom in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat.
Warning: Get data of variable fullMedium.P_nom from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat failed!
Error: Could not read variable fullMedium.TC in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat.
Warning: Get data of variable fullMedium.TC from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat failed!
Error: Could not read variable fullMedium.assertionLevel in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat.
Warning: Get data of variable fullMedium.assertionLevel from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat failed!
Error: Could not read variable fullMedium.dp_fixed in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat.
Warning: Get data of variable fullMedium.dp_fixed from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat failed!
Error: Could not read variable fullMedium.dp_nom in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat.
Warning: Get data of variable fullMedium.dp_nom from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat failed!
Error: Could not read variable fullMedium.dp_start in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat.
Warning: Get data of variable fullMedium.dp_start from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat failed!
Error: Could not read variable fullMedium.inlet.der(m_flow) in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat.
Warning: Get data of variable fullMedium.inlet.der(m_flow) from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat failed!
Error: Could not read variable fullMedium.pRatio_fixed in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat.
Warning: Get data of variable fullMedium.pRatio_fixed from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat failed!
Error: Could not read variable fullMedium.p_out_fixed in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat.
Warning: Get data of variable fullMedium.p_out_fixed from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat failed!
Error: Could not read variable incompressibleFluid.P_nom in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat.
Warning: Get data of variable incompressibleFluid.P_nom from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat failed!
Error: Could not read variable incompressibleFluid.TC in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat.
Warning: Get data of variable incompressibleFluid.TC from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat failed!
Error: Could not read variable incompressibleFluid.assertionLevel in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat.
Warning: Get data of variable incompressibleFluid.assertionLevel from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat failed!
Error: Could not read variable incompressibleFluid.dp_fixed in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat.
Warning: Get data of variable incompressibleFluid.dp_fixed from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat failed!
Error: Could not read variable incompressibleFluid.dp_nom in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat.
Warning: Get data of variable incompressibleFluid.dp_nom from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat failed!
Error: Could not read variable incompressibleFluid.dp_start in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat.
Warning: Get data of variable incompressibleFluid.dp_start from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat failed!
Error: Could not read variable incompressibleFluid.inlet.der(m_flow) in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat.
Warning: Get data of variable incompressibleFluid.inlet.der(m_flow) from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat failed!
Error: Could not read variable incompressibleFluid.pRatio_fixed in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat.
Warning: Get data of variable incompressibleFluid.pRatio_fixed from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat failed!
Error: Could not read variable incompressibleFluid.p_out_fixed in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat.
Warning: Get data of variable incompressibleFluid.p_out_fixed from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat failed!
Error: Could not read variable isothermalReference.P_nom in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat.
Warning: Get data of variable isothermalReference.P_nom from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat failed!
Error: Could not read variable isothermalReference.TC in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat.
Warning: Get data of variable isothermalReference.TC from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat failed!
Error: Could not read variable isothermalReference.assertionLevel in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat.
Warning: Get data of variable isothermalReference.assertionLevel from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat failed!
Error: Could not read variable isothermalReference.dp_fixed in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat.
Warning: Get data of variable isothermalReference.dp_fixed from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat failed!
Error: Could not read variable isothermalReference.dp_nom in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat.
Warning: Get data of variable isothermalReference.dp_nom from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat failed!
Error: Could not read variable isothermalReference.dp_start in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat.
Warning: Get data of variable isothermalReference.dp_start from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat failed!
Error: Could not read variable isothermalReference.inlet.der(m_flow) in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat.
Warning: Get data of variable isothermalReference.inlet.der(m_flow) from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat failed!
Error: Could not read variable isothermalReference.pRatio_fixed in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat.
Warning: Get data of variable isothermalReference.pRatio_fixed from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat failed!
Error: Could not read variable isothermalReference.p_out_fixed in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat.
Warning: Get data of variable isothermalReference.p_out_fixed from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat failed!
Error: Could not read variable sink.inlet.der(m_flow) in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat.
Warning: Get data of variable sink.inlet.der(m_flow) from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat failed!
Error: Could not read variable sink1.inlet.der(m_flow) in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat.
Warning: Get data of variable sink1.inlet.der(m_flow) from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat failed!
Error: Could not read variable sink2.inlet.der(m_flow) in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat.
Warning: Get data of variable sink2.inlet.der(m_flow) from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat failed!
Error: Could not read variable source.outlet.der(m_flow) in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat.
Warning: Get data of variable source.outlet.der(m_flow) from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat failed!
Error: Could not read variable source1.outlet.der(m_flow) in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat.
Warning: Get data of variable source1.outlet.der(m_flow) from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat failed!
Error: Could not read variable source2.outlet.der(m_flow) in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat.
Warning: Get data of variable source2.outlet.der(m_flow) from file ThermofluidStream_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.iconIsCompression,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.iconIsCompression,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.iconIsCompression,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: 7.102283586980775]