Running: ./testmodel.py --libraries=/home/hudson/saved_omc/libraries/.openmodelica/libraries --ompython_omhome=/usr ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater.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 0.001005/0.001005, allocations: 91.56 kB / 20.22 MB, free: 4.211 MB / 18.57 MB
"
[Timeout remaining time 180]
loadFile("/home/hudson/saved_omc/libraries/.openmodelica/libraries/Complex 4.1.0+maint.om/package.mo", uses=false) [Timeout 180]
"Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/Complex 4.1.0+maint.om/package.mo): time 0.000949/0.000949, allocations: 157.3 kB / 23.52 MB, free: 0.9062 MB / 18.57 MB
"
[Timeout remaining time 180]
loadFile("/home/hudson/saved_omc/libraries/.openmodelica/libraries/Modelica 4.1.0+maint.om/package.mo", uses=false) [Timeout 180]
"Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/Modelica 4.1.0+maint.om/package.mo): time 0.9063/0.9063, allocations: 177.2 MB / 203.9 MB, free: 5.598 MB / 186.7 MB
"
[Timeout remaining time 179]
loadFile("/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermofluidStream 1.4.0/package.mo", uses=false) [Timeout 180]
"Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermofluidStream 1.4.0/package.mo): time 0.6366/0.6366, allocations: 118.6 MB / 379 MB, free: 1.48 MB / 346.7 MB
"
[Timeout remaining time 179]
Using package ThermofluidStream with version 1.4.0 (/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermofluidStream 1.4.0/package.mo)
Using package Modelica with version 4.1.0 (/home/hudson/saved_omc/libraries/.openmodelica/libraries/Modelica 4.1.0+maint.om/package.mo)
Using package Complex with version 4.1.0 (/home/hudson/saved_omc/libraries/.openmodelica/libraries/Complex 4.1.0+maint.om/package.mo)
Using package ModelicaServices with version 4.1.0 (/home/hudson/saved_omc/libraries/.openmodelica/libraries/ModelicaServices 4.1.0+maint.om/package.mo)
Running command: translateModel(ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater,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.ConstantPropertyLiquidWater")
translateModel(ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater,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.ConstantPropertyLiquidWater") [Timeout 660]
"Notification: Performance of FrontEnd - loaded program: time 1.753e-06/1.753e-06, allocations: 0 / 482.9 MB, free: 8.75 MB / 410.7 MB
Notification: Performance of FrontEnd - Absyn->SCode: time 1.337e-05/1.512e-05, allocations: 2.312 kB / 482.9 MB, free: 8.746 MB / 410.7 MB
Notification: Performance of NFInst.instantiate(ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater): time 0.01881/0.01882, allocations: 26.69 MB / 0.4976 GB, free: 6.32 MB / 426.7 MB
Notification: Performance of NFInst.instExpressions: time 0.005669/0.02449, allocations: 6.368 MB / 0.5039 GB, free: 0.6641 MB / 426.7 MB
Notification: Performance of NFInst.updateImplicitVariability: time 0.000504/0.02499, allocations: 67.31 kB / 0.5039 GB, free: 0.5977 MB / 426.7 MB
Notification: Performance of NFTyping.typeComponents: time 0.0007836/0.02578, allocations: 433.4 kB / 0.5043 GB, free: 208 kB / 426.7 MB
Notification: Performance of NFTyping.typeBindings: time 0.001813/0.02759, allocations: 1.156 MB / 0.5055 GB, free: 15.04 MB / 442.7 MB
Notification: Performance of NFTyping.typeClassSections: time 0.001027/0.02862, allocations: 0.6772 MB / 0.5061 GB, free: 14.36 MB / 442.7 MB
Notification: Performance of NFFlatten.flatten: time 0.001434/0.03005, allocations: 1.576 MB / 0.5077 GB, free: 12.77 MB / 442.7 MB
Notification: Performance of NFFlatten.resolveConnections: time 0.0002422/0.03029, allocations: 127.8 kB / 0.5078 GB, free: 12.64 MB / 442.7 MB
Notification: Performance of NFEvalConstants.evaluate: time 0.001018/0.03131, allocations: 0.8723 MB / 0.5086 GB, free: 11.76 MB / 442.7 MB
Notification: Performance of NFSimplifyModel.simplify: time 0.0004042/0.03172, allocations: 382.6 kB / 0.509 GB, free: 11.39 MB / 442.7 MB
Notification: Performance of NFPackage.collectConstants: time 7.646e-05/0.03179, allocations: 56 kB / 0.5091 GB, free: 11.33 MB / 442.7 MB
Notification: Performance of NFFlatten.collectFunctions: time 0.001046/0.03284, allocations: 0.5963 MB / 0.5096 GB, free: 10.73 MB / 442.7 MB
Notification: Performance of NFScalarize.scalarize: time 0.0001148/0.03295, allocations: 163.1 kB / 0.5098 GB, free: 10.57 MB / 442.7 MB
Notification: Performance of NFVerifyModel.verify: time 0.0001986/0.03315, allocations: 303.1 kB / 0.5101 GB, free: 10.28 MB / 442.7 MB
Notification: Performance of NFConvertDAE.convert: time 0.00138/0.03453, allocations: 1.616 MB / 0.5117 GB, free: 8.656 MB / 442.7 MB
Notification: Performance of FrontEnd - DAE generated: time 2.505e-06/0.03453, allocations: 0 / 0.5117 GB, free: 8.656 MB / 442.7 MB
Notification: Performance of FrontEnd: time 1.233e-06/0.03454, allocations: 0 / 0.5117 GB, free: 8.656 MB / 442.7 MB
Notification: Performance of Transformations before backend: time 1.296e-05/0.03455, allocations: 8 kB / 0.5117 GB, free: 8.648 MB / 442.7 MB
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 0.001384/0.03593, allocations: 1.483 MB / 0.5131 GB, free: 7.125 MB / 442.7 MB
Notification: Performance of prepare preOptimizeDAE: time 3.345e-05/0.03597, allocations: 8.031 kB / 0.5131 GB, free: 7.117 MB / 442.7 MB
Notification: Performance of preOpt normalInlineFunction (simulation): time 0.000175/0.03614, allocations: 180.1 kB / 0.5133 GB, free: 6.941 MB / 442.7 MB
Notification: Performance of preOpt evaluateParameters (simulation): time 0.0008411/0.03698, allocations: 0.8137 MB / 0.5141 GB, free: 6.09 MB / 442.7 MB
Notification: Performance of preOpt simplifyIfEquations (simulation): time 0.0001193/0.0371, allocations: 208.1 kB / 0.5143 GB, free: 5.852 MB / 442.7 MB
Notification: Performance of preOpt expandDerOperator (simulation): time 6.935e-05/0.03717, allocations: 64.38 kB / 0.5144 GB, free: 5.789 MB / 442.7 MB
Notification: Performance of preOpt clockPartitioning (simulation): time 0.0009328/0.0381, allocations: 0.7019 MB / 0.515 GB, free: 5.039 MB / 442.7 MB
Notification: Performance of preOpt findStateOrder (simulation): time 1.187e-05/0.03812, allocations: 192 / 0.515 GB, free: 5.039 MB / 442.7 MB
Notification: Performance of preOpt replaceEdgeChange (simulation): time 3.311e-05/0.03815, allocations: 31.94 kB / 0.5151 GB, free: 5.008 MB / 442.7 MB
Notification: Performance of preOpt inlineArrayEqn (simulation): time 1.052e-05/0.03816, allocations: 20 kB / 0.5151 GB, free: 4.988 MB / 442.7 MB
Notification: Performance of preOpt removeEqualRHS (simulation): time 0.0005484/0.03871, allocations: 455.4 kB / 0.5155 GB, free: 4.543 MB / 442.7 MB
Notification: Performance of preOpt removeSimpleEquations (simulation): time 0.00195/0.04066, allocations: 2.62 MB / 0.5181 GB, free: 1.82 MB / 442.7 MB
Notification: Performance of preOpt comSubExp (simulation): time 0.0004351/0.04109, allocations: 392.8 kB / 0.5185 GB, free: 1.426 MB / 442.7 MB
Notification: Performance of preOpt resolveLoops (simulation): time 0.0002321/0.04133, allocations: 206.8 kB / 0.5187 GB, free: 1.223 MB / 442.7 MB
Notification: Performance of preOpt evalFunc (simulation): time 0.001195/0.04252, allocations: 1.068 MB / 0.5197 GB, free: 132 kB / 442.7 MB
Notification: Performance of preOpt encapsulateWhenConditions (simulation): time 1.995e-05/0.04254, allocations: 41.77 kB / 0.5197 GB, free: 80 kB / 442.7 MB
Notification: Performance of pre-optimization done (n=45): time 1.222e-06/0.04254, allocations: 0 / 0.5197 GB, free: 80 kB / 442.7 MB
Notification: Performance of matching and sorting (n=45): time 0.0006919/0.04323, allocations: 0.5315 MB / 0.5203 GB, free: 15.54 MB / 458.7 MB
Notification: Performance of inlineWhenForInitialization (initialization): time 3.141e-05/0.04327, allocations: 63.28 kB / 0.5203 GB, free: 15.47 MB / 458.7 MB
Notification: Performance of selectInitializationVariablesDAE (initialization): time 0.0005753/0.04384, allocations: 0.8392 MB / 0.5211 GB, free: 14.61 MB / 458.7 MB
Notification: Performance of collectPreVariables (initialization): time 1.981e-05/0.04386, allocations: 33.7 kB / 0.5212 GB, free: 14.57 MB / 458.7 MB
Notification: Performance of collectInitialEqns (initialization): time 0.0005083/0.04437, allocations: 0.5383 MB / 0.5217 GB, free: 14.03 MB / 458.7 MB
Notification: Performance of collectInitialBindings (initialization): time 8.316e-05/0.04445, allocations: 178.5 kB / 0.5219 GB, free: 13.86 MB / 458.7 MB
Notification: Performance of simplifyInitialFunctions (initialization): time 9.424e-05/0.04455, allocations: 115.8 kB / 0.522 GB, free: 13.73 MB / 458.7 MB
Notification: Performance of setup shared object (initialization): time 0.0001087/0.04465, allocations: 0.5004 MB / 0.5225 GB, free: 13.23 MB / 458.7 MB
Notification: Performance of preBalanceInitialSystem (initialization): time 0.0001674/0.04482, allocations: 128.9 kB / 0.5226 GB, free: 13.1 MB / 458.7 MB
Notification: Performance of partitionIndependentBlocks (initialization): time 0.0002457/0.04507, allocations: 323 kB / 0.5229 GB, free: 12.71 MB / 458.7 MB
Notification: Performance of analyzeInitialSystem (initialization): time 0.0004425/0.04551, allocations: 490.4 kB / 0.5234 GB, free: 12.15 MB / 458.7 MB
Notification: Performance of solveInitialSystemEqSystem (initialization): time 2.524e-06/0.04551, allocations: 0 / 0.5234 GB, free: 12.15 MB / 458.7 MB
Notification: Performance of matching and sorting (n=62) (initialization): time 0.0005659/0.04608, allocations: 0.5347 MB / 0.5239 GB, free: 11.61 MB / 458.7 MB
Notification: Performance of prepare postOptimizeDAE: time 1.378e-05/0.04609, allocations: 4 kB / 0.5239 GB, free: 11.61 MB / 458.7 MB
Notification: Performance of postOpt simplifyComplexFunction (initialization): time 6.853e-06/0.0461, allocations: 4 kB / 0.5239 GB, free: 11.61 MB / 458.7 MB
Notification: Performance of postOpt tearingSystem (initialization): time 1.504e-05/0.04611, allocations: 8 kB / 0.5239 GB, free: 11.6 MB / 458.7 MB
Notification: Performance of postOpt solveSimpleEquations (initialization): time 0.000206/0.04632, allocations: 119.8 kB / 0.524 GB, free: 11.48 MB / 458.7 MB
Notification: Performance of postOpt calculateStrongComponentJacobians (initialization): time 9.878e-06/0.04633, allocations: 15.88 kB / 0.524 GB, free: 11.46 MB / 458.7 MB
Notification: Performance of postOpt simplifyAllExpressions (initialization): time 0.0001379/0.04647, allocations: 52.05 kB / 0.5241 GB, free: 11.41 MB / 458.7 MB
Notification: Performance of postOpt collapseArrayExpressions (initialization): time 3.107e-05/0.0465, allocations: 28 kB / 0.5241 GB, free: 11.39 MB / 458.7 MB
Notification: Model statistics after passing the back-end for initialization:
 * Number of independent subsystems: 19
 * 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 (62):
 * Single equations (assignments): 62
 * 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 0.0001784/0.04668, allocations: 244.4 kB / 0.5243 GB, free: 11.14 MB / 458.7 MB
Notification: Performance of postOpt lateInlineFunction (simulation): time 8.106e-05/0.04676, allocations: 103.4 kB / 0.5244 GB, free: 11.04 MB / 458.7 MB
Notification: Performance of postOpt wrapFunctionCalls (simulation): time 0.0007985/0.04756, allocations: 0.8564 MB / 0.5253 GB, free: 10.14 MB / 458.7 MB
Notification: Performance of postOpt inlineArrayEqn (simulation): time 6.282e-06/0.04756, allocations: 4 kB / 0.5253 GB, free: 10.14 MB / 458.7 MB
Notification: Performance of postOpt constantLinearSystem (simulation): time 4.729e-06/0.04757, allocations: 7.875 kB / 0.5253 GB, free: 10.13 MB / 458.7 MB
Notification: Performance of postOpt simplifysemiLinear (simulation): time 4.639e-06/0.04757, allocations: 3.984 kB / 0.5253 GB, free: 10.12 MB / 458.7 MB
Notification: Performance of postOpt removeSimpleEquations (simulation): time 0.0004307/0.048, allocations: 0.5861 MB / 0.5259 GB, free: 9.504 MB / 458.7 MB
Notification: Performance of postOpt simplifyComplexFunction (simulation): time 2.726e-06/0.04801, allocations: 0 / 0.5259 GB, free: 9.504 MB / 458.7 MB
Notification: Performance of postOpt solveSimpleEquations (simulation): time 0.0001157/0.04812, allocations: 55.97 kB / 0.5259 GB, free: 9.449 MB / 458.7 MB
Notification: Performance of postOpt tearingSystem (simulation): time 2.655e-06/0.04812, allocations: 0 / 0.5259 GB, free: 9.449 MB / 458.7 MB
Notification: Performance of postOpt inputDerivativesUsed (simulation): time 1.113e-05/0.04814, allocations: 4 kB / 0.5259 GB, free: 9.445 MB / 458.7 MB
Notification: Performance of postOpt calculateStrongComponentJacobians (simulation): time 2.465e-06/0.04814, allocations: 7.938 kB / 0.5259 GB, free: 9.438 MB / 458.7 MB
Notification: Performance of postOpt calculateStateSetsJacobians (simulation): time 2.224e-06/0.04814, allocations: 4 kB / 0.5259 GB, free: 9.434 MB / 458.7 MB
Notification: Performance of postOpt symbolicJacobian (simulation): time 0.0003748/0.04852, allocations: 397.3 kB / 0.5263 GB, free: 9.023 MB / 458.7 MB
Notification: Performance of postOpt removeConstants (simulation): time 0.0001037/0.04862, allocations: 99.33 kB / 0.5264 GB, free: 8.926 MB / 458.7 MB
Notification: Performance of postOpt simplifyTimeIndepFuncCalls (simulation): time 3.978e-05/0.04866, allocations: 15.94 kB / 0.5264 GB, free: 8.91 MB / 458.7 MB
Notification: Performance of postOpt simplifyAllExpressions (simulation): time 8.476e-05/0.04874, allocations: 12 kB / 0.5264 GB, free: 8.898 MB / 458.7 MB
Notification: Performance of postOpt findZeroCrossings (simulation): time 6.041e-05/0.0488, allocations: 23.95 kB / 0.5265 GB, free: 8.875 MB / 458.7 MB
Notification: Performance of postOpt collapseArrayExpressions (simulation): time 1.248e-05/0.04882, allocations: 11.94 kB / 0.5265 GB, free: 8.863 MB / 458.7 MB
Notification: Performance of sorting global known variables: time 0.0004126/0.04923, allocations: 0.5659 MB / 0.527 GB, free: 8.285 MB / 458.7 MB
Notification: Performance of sort global known variables: time 6e-08/0.04923, allocations: 0 / 0.527 GB, free: 8.285 MB / 458.7 MB
Notification: Performance of remove unused functions: time 0.00043/0.04966, allocations: 279.3 kB / 0.5273 GB, free: 8.012 MB / 458.7 MB
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 (31):
 * Single equations (assignments): 30
 * 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 0.0003844/0.05004, allocations: 391.5 kB / 0.5277 GB, free: 7.629 MB / 458.7 MB
Notification: Performance of simCode: created initialization part: time 0.0004279/0.05047, allocations: 356.2 kB / 0.528 GB, free: 7.277 MB / 458.7 MB
Notification: Performance of simCode: created event and clocks part: time 1.483e-06/0.05047, allocations: 0 / 0.528 GB, free: 7.277 MB / 458.7 MB
Notification: Performance of simCode: created simulation system equations: time 0.0001561/0.05063, allocations: 140.6 kB / 0.5281 GB, free: 7.137 MB / 458.7 MB
Notification: Performance of simCode: created of all other equations (e.g. parameter, nominal, assert, etc): time 0.001078/0.05171, allocations: 389.9 kB / 0.5285 GB, free: 6.789 MB / 458.7 MB
Notification: Performance of simCode: created linear, non-linear and system jacobian parts: time 0.001324/0.05303, allocations: 1.351 MB / 0.5298 GB, free: 5.391 MB / 458.7 MB
Notification: Performance of simCode: some other stuff during SimCode phase: time 0.0002115/0.05324, allocations: 378.8 kB / 0.5302 GB, free: 4.988 MB / 458.7 MB
Notification: Performance of simCode: all other stuff during SimCode phase: time 0.000113/0.05336, allocations: 80.47 kB / 0.5303 GB, free: 4.91 MB / 458.7 MB
Notification: Performance of SimCode: time 6.51e-07/0.05336, allocations: 4 kB / 0.5303 GB, free: 4.906 MB / 458.7 MB
Notification: Performance of Templates: time 0.01189/0.06525, allocations: 15.09 MB / 0.545 GB, free: 5.945 MB / 474.7 MB
"
[Timeout remaining time 660]
make -j1 -f ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater.makefile [Timeout 660]
(rm -f ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater.pipe ; mkfifo ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater.pipe ; head -c 1048576 < ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater.pipe >> ../files/ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater.sim & ./ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater -emit_protected > ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater.pipe 2>&1) [Timeout 240]
diffSimulationResults("ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat","/mnt/ReferenceFiles/ThermofluidStream-main-regression/ReferenceData/ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_ref.mat","/var/lib/jenkins/ws/OpenModelicaLibraryTestingWork/OpenModelicaLibraryTesting/files/ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater.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.ConstantPropertyLiquidWater_res.mat.
Warning: Get data of variable CPUtime from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat failed!
Error: Could not read variable EventCounter in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat.
Warning: Get data of variable EventCounter from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat failed!
Error: Could not read variable _derdummy in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat.
Warning: Get data of variable _derdummy from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat failed!
Error: Could not read variable _dummy in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat.
Warning: Get data of variable _dummy from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat failed!
Error: Could not read variable dropOfCommons.instanceNameColor[1] in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat.
Warning: Get data of variable dropOfCommons.instanceNameColor[1] from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat failed!
Error: Could not read variable dropOfCommons.instanceNameColor[2] in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat.
Warning: Get data of variable dropOfCommons.instanceNameColor[2] from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat failed!
Error: Could not read variable dropOfCommons.instanceNameColor[3] in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat.
Warning: Get data of variable dropOfCommons.instanceNameColor[3] from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat failed!
Error: Could not read variable fullMedium.P_nom in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat.
Warning: Get data of variable fullMedium.P_nom from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat failed!
Error: Could not read variable fullMedium.TC in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat.
Warning: Get data of variable fullMedium.TC from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat failed!
Error: Could not read variable fullMedium.assertionLevel in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat.
Warning: Get data of variable fullMedium.assertionLevel from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat failed!
Error: Could not read variable fullMedium.dp_fixed in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat.
Warning: Get data of variable fullMedium.dp_fixed from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat failed!
Error: Could not read variable fullMedium.dp_nom in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat.
Warning: Get data of variable fullMedium.dp_nom from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat failed!
Error: Could not read variable fullMedium.dp_start in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat.
Warning: Get data of variable fullMedium.dp_start from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat failed!
Error: Could not read variable fullMedium.inlet.der(m_flow) in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat.
Warning: Get data of variable fullMedium.inlet.der(m_flow) from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat failed!
Error: Could not read variable fullMedium.pRatio_fixed in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat.
Warning: Get data of variable fullMedium.pRatio_fixed from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat failed!
Error: Could not read variable fullMedium.p_out_fixed in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat.
Warning: Get data of variable fullMedium.p_out_fixed from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat failed!
Error: Could not read variable incompressibleFluid.P_nom in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat.
Warning: Get data of variable incompressibleFluid.P_nom from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat failed!
Error: Could not read variable incompressibleFluid.TC in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat.
Warning: Get data of variable incompressibleFluid.TC from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat failed!
Error: Could not read variable incompressibleFluid.assertionLevel in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat.
Warning: Get data of variable incompressibleFluid.assertionLevel from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat failed!
Error: Could not read variable incompressibleFluid.dp_fixed in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat.
Warning: Get data of variable incompressibleFluid.dp_fixed from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat failed!
Error: Could not read variable incompressibleFluid.dp_nom in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat.
Warning: Get data of variable incompressibleFluid.dp_nom from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat failed!
Error: Could not read variable incompressibleFluid.dp_start in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat.
Warning: Get data of variable incompressibleFluid.dp_start from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat failed!
Error: Could not read variable incompressibleFluid.inlet.der(m_flow) in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat.
Warning: Get data of variable incompressibleFluid.inlet.der(m_flow) from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat failed!
Error: Could not read variable incompressibleFluid.pRatio_fixed in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat.
Warning: Get data of variable incompressibleFluid.pRatio_fixed from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat failed!
Error: Could not read variable incompressibleFluid.p_out_fixed in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat.
Warning: Get data of variable incompressibleFluid.p_out_fixed from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat failed!
Error: Could not read variable isothermalReference.P_nom in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat.
Warning: Get data of variable isothermalReference.P_nom from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat failed!
Error: Could not read variable isothermalReference.TC in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat.
Warning: Get data of variable isothermalReference.TC from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat failed!
Error: Could not read variable isothermalReference.assertionLevel in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat.
Warning: Get data of variable isothermalReference.assertionLevel from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat failed!
Error: Could not read variable isothermalReference.dp_fixed in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat.
Warning: Get data of variable isothermalReference.dp_fixed from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat failed!
Error: Could not read variable isothermalReference.dp_nom in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat.
Warning: Get data of variable isothermalReference.dp_nom from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat failed!
Error: Could not read variable isothermalReference.dp_start in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat.
Warning: Get data of variable isothermalReference.dp_start from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat failed!
Error: Could not read variable isothermalReference.inlet.der(m_flow) in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat.
Warning: Get data of variable isothermalReference.inlet.der(m_flow) from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat failed!
Error: Could not read variable isothermalReference.pRatio_fixed in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat.
Warning: Get data of variable isothermalReference.pRatio_fixed from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat failed!
Error: Could not read variable isothermalReference.p_out_fixed in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat.
Warning: Get data of variable isothermalReference.p_out_fixed from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat failed!
Error: Could not read variable sink.inlet.der(m_flow) in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat.
Warning: Get data of variable sink.inlet.der(m_flow) from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat failed!
Error: Could not read variable sink1.inlet.der(m_flow) in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat.
Warning: Get data of variable sink1.inlet.der(m_flow) from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat failed!
Error: Could not read variable sink2.inlet.der(m_flow) in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat.
Warning: Get data of variable sink2.inlet.der(m_flow) from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat failed!
Error: Could not read variable source.outlet.der(m_flow) in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat.
Warning: Get data of variable source.outlet.der(m_flow) from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat failed!
Error: Could not read variable source1.outlet.der(m_flow) in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat.
Warning: Get data of variable source1.outlet.der(m_flow) from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat failed!
Error: Could not read variable source2.outlet.der(m_flow) in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat.
Warning: Get data of variable source2.outlet.der(m_flow) from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat failed!
"
[Timeout remaining time 660]
Reference file matches
[Calling sys.exit(0), Time elapsed: 6.497423549881205]