Running: ./testmodel.py --libraries=/home/hudson/saved_omc/libraries/.openmodelica/libraries --ompython_omhome=/usr ThermofluidStream_ThermofluidStream.Idealized.Tests.Processes.Adiabatic.PumpConstant.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 0.00143/0.00143, allocations: 88.88 kB / 20.22 MB, free: 4.184 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 0.001526/0.001526, allocations: 173.6 kB / 23.53 MB, free: 0.8672 MB / 18.57 MB
"
[Timeout remaining time 180]
loadFile("/home/hudson/saved_omc/libraries/.openmodelica/libraries/Modelica 4.1.0+maint.om/package.mo", uses=false) [Timeout 180]
"Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/Modelica 4.1.0+maint.om/package.mo): time 1.533/1.533, allocations: 177.2 MB / 203.9 MB, free: 5.59 MB / 186.7 MB
"
[Timeout remaining time 178]
loadFile("/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermofluidStream 1.4.0/package.mo", uses=false) [Timeout 180]
"Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermofluidStream 1.4.0/package.mo): time 1.032/1.032, allocations: 118.6 MB / 379 MB, free: 1.488 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.Tests.Processes.Adiabatic.PumpConstant,tolerance=1e-06,outputFormat="mat",numberOfIntervals=100,variableFilter="CPUtime|EventCounter|NonlinearSystems.initialization.1..Calls|NonlinearSystems.initialization.1..Iterations|NonlinearSystems.initialization.1..Jacobians|NonlinearSystems.initialization.1..Residues|NonlinearSystems.initialization.2..Calls|NonlinearSystems.initialization.2..Iterations|NonlinearSystems.initialization.2..Jacobians|NonlinearSystems.initialization.2..Residues|NonlinearSystems.initialization.3..Calls|NonlinearSystems.initialization.3..Iterations|NonlinearSystems.initialization.3..Jacobians|NonlinearSystems.initialization.3..Residues|Time|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.P_out|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.d|fullMedium.adiabaticModel.state_in.h|fullMedium.adiabaticModel.state_in.p|fullMedium.adiabaticModel.state_in.phase|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.d|fullMedium.inlet.state.h|fullMedium.inlet.state.p|fullMedium.inlet.state.phase|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.d|fullMedium.outlet.state.h|fullMedium.outlet.state.p|fullMedium.outlet.state.phase|fullMedium.outletSpec|fullMedium.outletSpec_actual|fullMedium.outletValueSpec|fullMedium.pRatio|fullMedium.pRatio_fixed|fullMedium.p_in|fullMedium.p_min|fullMedium.p_out|fullMedium.p_out_fixed|fullMedium.singularityRegime|fullMedium1.L|fullMedium1.P|fullMedium1.P_in|fullMedium1.P_nom|fullMedium1.TC|fullMedium1.adiabaticModel.eta_is|fullMedium1.adiabaticModel.h_in|fullMedium1.adiabaticModel.h_out|fullMedium1.adiabaticModel.h_out_is|fullMedium1.adiabaticModel.p_out|fullMedium1.adiabaticModel.s_in|fullMedium1.adiabaticModel.state_in.T|fullMedium1.adiabaticModel.state_in.d|fullMedium1.adiabaticModel.state_in.h|fullMedium1.adiabaticModel.state_in.p|fullMedium1.adiabaticModel.state_in.phase|fullMedium1.adiabaticModel.w_t|fullMedium1.adiabaticModel.w_t_is|fullMedium1.assertionLevel|fullMedium1.clip_p_out|der.fullMedium1.dp.|fullMedium1.dh|fullMedium1.dp|fullMedium1.dp_fixed|fullMedium1.dp_nom|fullMedium1.dp_start|fullMedium1.dr_corr|fullMedium1.etaSpec|fullMedium1.eta_actual|fullMedium1.eta_fixed|fullMedium1.eta_is|fullMedium1.h_in|fullMedium1.h_out|fullMedium1.initM_flow|der.fullMedium1.inlet.m_flow.|fullMedium1.inlet.m_flow|fullMedium1.inlet.r|fullMedium1.inlet.state.T|fullMedium1.inlet.state.d|fullMedium1.inlet.state.h|fullMedium1.inlet.state.p|fullMedium1.inlet.state.phase|fullMedium1.m_acceleration_0|fullMedium1.m_flow|fullMedium1.m_flowStateSelect|fullMedium1.m_flow_0|fullMedium1.outlet.m_flow|fullMedium1.outlet.r|fullMedium1.outlet.state.T|fullMedium1.outlet.state.d|fullMedium1.outlet.state.h|fullMedium1.outlet.state.p|fullMedium1.outlet.state.phase|fullMedium1.outletSpec_actual|fullMedium1.pRatio|fullMedium1.pRatio_fixed|fullMedium1.p_in|fullMedium1.p_min|fullMedium1.p_out|fullMedium1.p_out_fixed|fullMedium1.singularityRegime|fullMedium2.L|fullMedium2.P|fullMedium2.P_in|fullMedium2.P_nom|fullMedium2.TC|fullMedium2.adiabaticModel.eta_is|fullMedium2.adiabaticModel.h_in|fullMedium2.adiabaticModel.h_out|fullMedium2.adiabaticModel.h_out_is|fullMedium2.adiabaticModel.p_out|fullMedium2.adiabaticModel.s_in|fullMedium2.adiabaticModel.state_in.T|fullMedium2.adiabaticModel.state_in.d|fullMedium2.adiabaticModel.state_in.h|fullMedium2.adiabaticModel.state_in.p|fullMedium2.adiabaticModel.state_in.phase|fullMedium2.adiabaticModel.w_t|fullMedium2.adiabaticModel.w_t_is|fullMedium2.assertionLevel|fullMedium2.clip_p_out|fullMedium2.dh|fullMedium2.dp|fullMedium2.dp_fixed|fullMedium2.dp_nom|fullMedium2.dp_start|fullMedium2.dr_corr|fullMedium2.etaSpec|fullMedium2.eta_actual|fullMedium2.eta_fixed|fullMedium2.eta_is|fullMedium2.h_in|fullMedium2.h_out|fullMedium2.initM_flow|der.fullMedium2.inlet.m_flow.|fullMedium2.inlet.m_flow|fullMedium2.inlet.r|fullMedium2.inlet.state.T|fullMedium2.inlet.state.d|fullMedium2.inlet.state.h|fullMedium2.inlet.state.p|fullMedium2.inlet.state.phase|fullMedium2.m_acceleration_0|fullMedium2.m_flow|fullMedium2.m_flowStateSelect|fullMedium2.m_flow_0|fullMedium2.outlet.m_flow|fullMedium2.outlet.r|fullMedium2.outlet.state.T|fullMedium2.outlet.state.d|fullMedium2.outlet.state.h|fullMedium2.outlet.state.p|fullMedium2.outlet.state.phase|fullMedium2.outletSpec|fullMedium2.outletSpec_actual|fullMedium2.outletValueSpec|fullMedium2.pRatio|fullMedium2.pRatio_fixed|fullMedium2.p_in|fullMedium2.p_min|fullMedium2.p_out|fullMedium2.p_out_fixed|fullMedium2.singularityRegime|fullMedium3.L|fullMedium3.P|fullMedium3.P_in|fullMedium3.P_nom|fullMedium3.TC|fullMedium3.adiabaticModel.eta_is|fullMedium3.adiabaticModel.h_in|fullMedium3.adiabaticModel.h_out|fullMedium3.adiabaticModel.h_out_is|fullMedium3.adiabaticModel.p_out|fullMedium3.adiabaticModel.s_in|fullMedium3.adiabaticModel.state_in.T|fullMedium3.adiabaticModel.state_in.d|fullMedium3.adiabaticModel.state_in.h|fullMedium3.adiabaticModel.state_in.p|fullMedium3.adiabaticModel.state_in.phase|fullMedium3.adiabaticModel.w_t|fullMedium3.adiabaticModel.w_t_is|fullMedium3.assertionLevel|fullMedium3.clip_p_out|fullMedium3.dh|fullMedium3.dp|fullMedium3.dp_fixed|fullMedium3.dp_nom|fullMedium3.dp_start|fullMedium3.dr_corr|fullMedium3.etaSpec|fullMedium3.eta_actual|fullMedium3.eta_fixed|fullMedium3.eta_is|fullMedium3.h_in|fullMedium3.h_out|fullMedium3.initM_flow|der.fullMedium3.inlet.m_flow.|fullMedium3.inlet.m_flow|fullMedium3.inlet.r|fullMedium3.inlet.state.T|fullMedium3.inlet.state.d|fullMedium3.inlet.state.h|fullMedium3.inlet.state.p|fullMedium3.inlet.state.phase|fullMedium3.m_acceleration_0|fullMedium3.m_flow|fullMedium3.m_flowStateSelect|fullMedium3.m_flow_0|fullMedium3.outlet.m_flow|fullMedium3.outlet.r|fullMedium3.outlet.state.T|fullMedium3.outlet.state.d|fullMedium3.outlet.state.h|fullMedium3.outlet.state.p|fullMedium3.outlet.state.phase|fullMedium3.outletSpec_actual|fullMedium3.pRatio|fullMedium3.pRatio_fixed|fullMedium3.p_in|fullMedium3.p_min|fullMedium3.p_out|fullMedium3.p_out_fixed|fullMedium3.singularityRegime|gain.k|gain.u|gain.y|gain1.k|gain1.u|gain1.y|gain2.k|gain2.u|gain2.y|incompressibleFluid.L|incompressibleFluid.P|incompressibleFluid.P_nom|incompressibleFluid.P_out|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.d|incompressibleFluid.adiabaticModel.state_in.h|incompressibleFluid.adiabaticModel.state_in.p|incompressibleFluid.adiabaticModel.state_in.phase|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.d|incompressibleFluid.inlet.state.h|incompressibleFluid.inlet.state.p|incompressibleFluid.inlet.state.phase|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.d|incompressibleFluid.outlet.state.h|incompressibleFluid.outlet.state.p|incompressibleFluid.outlet.state.phase|incompressibleFluid.outletSpec|incompressibleFluid.outletSpec_actual|incompressibleFluid.outletValueSpec|incompressibleFluid.pRatio|incompressibleFluid.pRatio_fixed|incompressibleFluid.p_in|incompressibleFluid.p_min|incompressibleFluid.p_out|incompressibleFluid.p_out_fixed|incompressibleFluid.singularityRegime|incompressibleFluid1.L|incompressibleFluid1.P|incompressibleFluid1.P_in|incompressibleFluid1.P_nom|incompressibleFluid1.TC|incompressibleFluid1.adiabaticModel.T_in|incompressibleFluid1.adiabaticModel.T_out_is|incompressibleFluid1.adiabaticModel.assertionLevel|incompressibleFluid1.adiabaticModel.deltaDensityRel|incompressibleFluid1.adiabaticModel.eta_is|incompressibleFluid1.adiabaticModel.h_in|incompressibleFluid1.adiabaticModel.h_out|incompressibleFluid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cModel.w_t_is|isothermalReference3.assertionLevel|isothermalReference3.clip_p_out|isothermalReference3.dh|isothermalReference3.dp|isothermalReference3.dp_fixed|isothermalReference3.dp_nom|isothermalReference3.dp_start|isothermalReference3.dr_corr|isothermalReference3.etaSpec|isothermalReference3.eta_actual|isothermalReference3.eta_fixed|isothermalReference3.eta_is|isothermalReference3.h_in|isothermalReference3.h_out|isothermalReference3.initM_flow|der.isothermalReference3.inlet.m_flow.|isothermalReference3.inlet.m_flow|isothermalReference3.inlet.r|isothermalReference3.inlet.state.T|isothermalReference3.inlet.state.d|isothermalReference3.inlet.state.h|isothermalReference3.inlet.state.p|isothermalReference3.inlet.state.phase|isothermalReference3.m_acceleration_0|isothermalReference3.m_flow|isothermalReference3.m_flowStateSelect|isothermalReference3.m_flow_0|isothermalReference3.outlet.m_flow|isothermalReference3.outlet.r|isothermalReference3.outlet.state.T|isothermalReference3.outlet.state.d|isothermalReference3.outlet.state.h|isothermalReference3.outlet.state.p|isothermalReference3.outlet.state.phase|isothermalReference3.outletSpec_actual|isothermalReference3.pRatio|isothermalReference3.pRatio_fixed|isothermalReference3.p_in|isothermalReference3.p_min|isothermalReference3.p_out|isothermalReference3.p_out_fixed|isothermalReference3.singularityRegime|pRatio|sink.L|der.sink.inlet.m_flow.|sink.inlet.m_flow|sink.inlet.r|sink.inlet.state.T|sink.inlet.state.d|sink.inlet.state.h|sink.inlet.state.p|sink.inlet.state.phase|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.d|sink1.inlet.state.h|sink1.inlet.state.p|sink1.inlet.state.phase|sink1.m_flow|sink1.m_flowSpec|sink1.m_flow_fixed|sink10.L|der.sink10.inlet.m_flow.|sink10.inlet.m_flow|sink10.inlet.r|sink10.inlet.state.T|sink10.inlet.state.d|sink10.inlet.state.h|sink10.inlet.state.p|sink10.inlet.state.phase|sink10.m_flow|sink10.m_flowSpec|sink10.m_flow_fixed|sink11.L|der.sink11.inlet.m_flow.|sink11.inlet.m_flow|sink11.inlet.r|sink11.inlet.state.T|sink11.inlet.state.d|sink11.inlet.state.h|sink11.inlet.state.p|sink11.inlet.state.phase|sink11.m_flow|sink11.m_flowSpec|sink11.m_flow_fixed|sink2.L|der.sink2.inlet.m_flow.|sink2.inlet.m_flow|sink2.inlet.r|sink2.inlet.state.T|sink2.inlet.state.d|sink2.inlet.state.h|sink2.inlet.state.p|sink2.inlet.state.phase|sink2.m_flow|sink2.m_flowSpec|sink2.m_flow_fixed|sink3.L|der.sink3.inlet.m_flow.|sink3.inlet.m_flow|sink3.inlet.r|sink3.inlet.state.T|sink3.inlet.state.d|sink3.inlet.state.h|sink3.inlet.state.p|sink3.inlet.state.phase|sink3.m_flow|sink3.m_flowSpec|sink3.m_flow_fixed|sink4.L|der.sink4.inlet.m_flow.|sink4.inlet.m_flow|sink4.inlet.r|sink4.inlet.state.T|sink4.inlet.state.d|sink4.inlet.state.h|sink4.inlet.state.p|sink4.inlet.state.phase|sink5.L|der.sink5.inlet.m_flow.|sink5.inlet.m_flow|sink5.inlet.r|sink5.inlet.state.T|sink5.inlet.state.d|sink5.inlet.state.h|sink5.inlet.state.p|sink5.inlet.state.phase|sink5.m_flow|sink5.m_flowSpec|sink5.m_flow_fixed|sink6.L|der.sink6.inlet.m_flow.|sink6.inlet.m_flow|sink6.inlet.r|sink6.inlet.state.T|sink6.inlet.state.d|sink6.inlet.state.h|sink6.inlet.state.p|sink6.inlet.state.phase|sink7.L|der.sink7.inlet.m_flow.|sink7.inlet.m_flow|sink7.inlet.r|sink7.inlet.state.T|sink7.inlet.state.d|sink7.inlet.state.h|sink7.inlet.state.p|sink7.inlet.state.phase|sink7.m_flow|sink7.m_flowSpec|sink7.m_flow_fixed|sink8.L|der.sink8.inlet.m_flow.|sink8.inlet.m_flow|sink8.inlet.r|sink8.inlet.state.T|sink8.inlet.state.d|sink8.inlet.state.h|sink8.inlet.state.p|sink8.inlet.state.phase|sink9.L|der.sink9.inlet.m_flow.|sink9.inlet.m_flow|sink9.inlet.r|sink9.inlet.state.T|sink9.inlet.state.d|sink9.inlet.state.h|sink9.inlet.state.p|sink9.inlet.state.phase|sink9.m_flow|sink9.m_flowSpec|sink9.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.d|source.outlet.state.h|source.outlet.state.p|source.outlet.state.phase|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.d|source1.outlet.state.h|source1.outlet.state.p|source1.outlet.state.phase|source1.p0|source1.p0_par|source10.L|source10.T0|source10.T0_par|source10.h0|source10.h0_par|der.source10.outlet.m_flow.|source10.outlet.m_flow|source10.outlet.r|source10.outlet.state.T|source10.outlet.state.d|source10.outlet.state.h|source10.outlet.state.p|source10.outlet.state.phase|source10.p0|source10.p0_par|source11.L|source11.T0|source11.T0_par|source11.h0|source11.h0_par|der.source11.outlet.m_flow.|source11.outlet.m_flow|source11.outlet.r|source11.outlet.state.T|source11.outlet.state.d|source11.outlet.state.h|source11.outlet.state.p|source11.outlet.state.phase|source11.p0|source11.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.d|source2.outlet.state.h|source2.outlet.state.p|source2.outlet.state.phase|source2.p0|source2.p0_par|source3.L|source3.T0|source3.T0_par|source3.h0|source3.h0_par|der.source3.outlet.m_flow.|source3.outlet.m_flow|source3.outlet.r|source3.outlet.state.T|source3.outlet.state.d|source3.outlet.state.h|source3.outlet.state.p|source3.outlet.state.phase|source3.p0|source3.p0_par|source4.L|source4.T0|source4.T0_par|source4.h0|source4.h0_par|der.source4.outlet.m_flow.|source4.outlet.m_flow|source4.outlet.r|source4.outlet.state.T|source4.outlet.state.d|source4.outlet.state.h|source4.outlet.state.p|source4.outlet.state.phase|source4.p0|source4.p0_par|source5.L|source5.T0|source5.T0_par|source5.h0|source5.h0_par|der.source5.outlet.m_flow.|source5.outlet.m_flow|source5.outlet.r|source5.outlet.state.T|source5.outlet.state.d|source5.outlet.state.h|source5.outlet.state.p|source5.outlet.state.phase|source5.p0|source5.p0_par|source6.L|source6.T0|source6.T0_par|source6.h0|source6.h0_par|der.source6.outlet.m_flow.|source6.outlet.m_flow|source6.outlet.r|source6.outlet.state.T|source6.outlet.state.d|source6.outlet.state.h|source6.outlet.state.p|source6.outlet.state.phase|source6.p0|source6.p0_par|source7.L|source7.T0|source7.T0_par|source7.h0|source7.h0_par|der.source7.outlet.m_flow.|source7.outlet.m_flow|source7.outlet.r|source7.outlet.state.T|source7.outlet.state.d|source7.outlet.state.h|source7.outlet.state.p|source7.outlet.state.phase|source7.p0|source7.p0_par|source8.L|source8.T0|source8.T0_par|source8.h0|source8.h0_par|der.source8.outlet.m_flow.|source8.outlet.m_flow|source8.outlet.r|source8.outlet.state.T|source8.outlet.state.d|source8.outlet.state.h|source8.outlet.state.p|source8.outlet.state.phase|source8.p0|source8.p0_par|source9.L|source9.T0|source9.T0_par|source9.h0|source9.h0_par|der.source9.outlet.m_flow.|source9.outlet.m_flow|source9.outlet.r|source9.outlet.state.T|source9.outlet.state.d|source9.outlet.state.h|source9.outlet.state.p|source9.outlet.state.phase|source9.p0|source9.p0_par",fileNamePrefix="ThermofluidStream_ThermofluidStream.Idealized.Tests.Processes.Adiabatic.PumpConstant") [Timeout 660]
"Notification: Performance of FrontEnd - Absyn->SCode: time 1.517e-05/1.517e-05, allocations: 2.312 kB / 483.8 MB, free: 24.17 MB / 426.7 MB
Notification: Performance of NFInst.instantiate(ThermofluidStream.Idealized.Tests.Processes.Adiabatic.PumpConstant): time 0.4728/0.4728, allocations: 219.3 MB / 0.6867 GB, free: 9.469 MB / 0.5573 GB
Notification: Performance of NFInst.instExpressions: time 0.04206/0.5149, allocations: 42.22 MB / 0.7279 GB, free: 8.465 MB / 0.5573 GB
Notification: Performance of NFInst.updateImplicitVariability: time 0.004289/0.5191, allocations: 270.6 kB / 0.7282 GB, free: 8.465 MB / 0.5573 GB
Notification: Performance of NFTyping.typeComponents: time 0.006073/0.5252, allocations: 2.362 MB / 0.7305 GB, free: 8.129 MB / 0.5573 GB
Notification: Performance of NFTyping.typeBindings: time 0.02877/0.554, allocations: 12.17 MB / 0.7424 GB, free: 4.355 MB / 0.5573 GB
Notification: Performance of NFTyping.typeClassSections: time 0.01129/0.5653, allocations: 4.94 MB / 0.7472 GB, free: 2.441 MB / 0.5573 GB
Notification: Performance of NFFlatten.flatten: time 0.008707/0.574, allocations: 8.394 MB / 0.7554 GB, free: 15.35 MB / 0.573 GB
Notification: Performance of NFFlatten.resolveConnections: time 0.002189/0.5762, allocations: 0.5885 MB / 0.756 GB, free: 15.14 MB / 0.573 GB
Notification: Performance of NFEvalConstants.evaluate: time 0.0598/0.636, allocations: 23.73 MB / 0.7792 GB, free: 15.18 MB / 0.5886 GB
Notification: Performance of NFSimplifyModel.simplify: time 0.004573/0.6405, allocations: 1.6 MB / 0.7807 GB, free: 13.71 MB / 0.5886 GB
Notification: Performance of NFPackage.collectConstants: time 0.0008989/0.6414, allocations: 272 kB / 0.781 GB, free: 13.45 MB / 0.5886 GB
Notification: Performance of NFFlatten.collectFunctions: time 0.03164/0.6731, allocations: 12.89 MB / 0.7936 GB, free: 0.8828 MB / 0.5886 GB
Notification: Performance of combineBinaries: time 0.01069/0.6838, allocations: 7.608 MB / 0.801 GB, free: 9.348 MB / 0.6042 GB
Notification: Performance of replaceArrayConstructors: time 0.006372/0.6901, allocations: 5.244 MB / 0.8061 GB, free: 4.062 MB / 0.6042 GB
Notification: Performance of NFVerifyModel.verify: time 0.001249/0.6914, allocations: 428 kB / 0.8065 GB, free: 3.645 MB / 0.6042 GB
Notification: Performance of FrontEnd: time 0.002977/0.6944, allocations: 1.118 MB / 0.8076 GB, free: 2.676 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: 804 (660)
 * Number of variables: 804 (804)
Notification: Performance of [SIM] Bindings: time 0.04011/0.7345, allocations: 20.09 MB / 0.8272 GB, free: 14.71 MB / 0.6355 GB
Notification: Performance of [SIM] FunctionAlias: time 0.008894/0.7434, allocations: 3.832 MB / 0.831 GB, free: 11.18 MB / 0.6355 GB
Notification: Performance of [SIM] Early Inline: time 0.05543/0.7988, allocations: 22.51 MB / 0.853 GB, free: 5.406 MB / 0.6511 GB
Notification: Performance of [SIM] Simplify 1: time 0.004463/0.8033, allocations: 1.096 MB / 0.854 GB, free: 4.273 MB / 0.6511 GB
Warning: NBAlias.setStartFixed: Alias set with conflicting unfixed start values detected. Use -d=dumprepl for more information.
Notification: Performance of [SIM] Alias: time 0.0522/0.8555, allocations: 17.69 MB / 0.8713 GB, free: 484 kB / 0.6667 GB
Notification: Performance of [SIM] Simplify 2: time 0.003434/0.8589, allocations: 0.8193 MB / 0.8721 GB, free: 15.59 MB / 0.6823 GB
Notification: Performance of [SIM] Remove Stream: time 0.002743/0.8616, allocations: 0.8426 MB / 0.8729 GB, free: 14.68 MB / 0.6823 GB
Notification: Performance of [SIM] Detect States: time 0.006275/0.8679, allocations: 2.556 MB / 0.8754 GB, free: 12.11 MB / 0.6823 GB
Notification: Performance of [SIM] Events: time 0.003086/0.871, allocations: 1.161 MB / 0.8765 GB, free: 10.96 MB / 0.6823 GB
Notification: Performance of [SIM] Partitioning: time 0.01418/0.8852, allocations: 4.808 MB / 0.8812 GB, free: 5.605 MB / 0.6823 GB
Error: Internal error NBResolveSingularities.indexReduction failed because there was not enough state candidates to balance out the constraint equations.
Constraint Equations (33/33)
******************************
(1)       [SCAL] (1) source.outlet.state.p = fullMedium.adiabaticModel.state_in.p; ($RES_SIM_518)
(2)       [SCAL] (1) fullMedium2.adiabaticModel.h_out_is = ThermofluidStream.Media.myMedia.Water.IF97_Utilities.h_props_ps(fullMedium2.p_out, fullMedium2.adiabaticModel.s_in, ThermofluidStream.Media.myMedia.Water.IF97_Utilities.waterBaseProp_ps(fullMedium2.p_out, fullMedium2.adiabaticModel.s_in, 0, 0)); ($RES_AUX_731)
(3)       [SCAL] (1) fullMedium2.pRatio_fixed = fullMedium2.p_out / fullMedium2.p_in; ($RES_BND_567)
(4)       [SCAL] (1) source4.outlet.state.p = fullMedium2.adiabaticModel.state_in.p; ($RES_SIM_488)
(5)       [SCAL] (1) fullMedium2.adiabaticModel.h_in = fullMedium2.adiabaticModel.state_in.h; ($RES_AUX_730)
(6)       [SCAL] (1) fullMedium2.dh = fullMedium2.h_out - fullMedium2.h_in; ($RES_SIM_245)
(7)       [SCAL] (1) fullMedium2.m_flow = (fullMedium2.dh * fullMedium1.P_in_internal) / (4.930380657631324e-32 + fullMedium2.dh ^ 2.0); ($RES_SIM_243)
(8)       [SCAL] (1) fullMedium2.adiabaticModel.s_in = ThermofluidStream.Media.myMedia.Water.IF97_Utilities.s_props_ph(fullMedium2.adiabaticModel.state_in.p, fullMedium2.adiabaticModel.state_in.h, ThermofluidStream.Media.myMedia.Water.IF97_Utilities.waterBaseProp_ph(fullMedium2.adiabaticModel.state_in.p, fullMedium2.adiabaticModel.state_in.h, fullMedium2.adiabaticModel.state_in.phase, 0)); ($RES_AUX_729)
(9)       [SCAL] (1) fullMedium2.h_in = fullMedium2.adiabaticModel.state_in.h; ($RES_AUX_727)
(10)      [SCAL] (1) fullMedium.dh = fullMedium.h_out - fullMedium.h_in; ($RES_SIM_325)
(11)      [SCAL] (1) fullMedium2.p_in = fullMedium2.adiabaticModel.state_in.p; ($RES_AUX_726)
(12)      [SCAL] (1) fullMedium.P_in_internal = sink.m_flow_fixed * fullMedium.dh; ($RES_SIM_323)
(13)      [SCAL] (1) fullMedium.adiabaticModel.h_out_is = ThermofluidStream.Media.myMedia.Water.IF97_Utilities.h_props_ps(fullMedium.p_out, fullMedium.adiabaticModel.s_in, ThermofluidStream.Media.myMedia.Water.IF97_Utilities.waterBaseProp_ps(fullMedium.p_out, fullMedium.adiabaticModel.s_in, 0, 0)); ($RES_AUX_707)
(14)      [SCAL] (1) fullMedium.adiabaticModel.h_in = fullMedium.adiabaticModel.state_in.h; ($RES_AUX_706)
(15)      [SCAL] (1) fullMedium.adiabaticModel.s_in = ThermofluidStream.Media.myMedia.Water.IF97_Utilities.s_props_ph(fullMedium.adiabaticModel.state_in.p, fullMedium.adiabaticModel.state_in.h, ThermofluidStream.Media.myMedia.Water.IF97_Utilities.waterBaseProp_ph(fullMedium.adiabaticModel.state_in.p, fullMedium.adiabaticModel.state_in.h, fullMedium.adiabaticModel.state_in.phase, 0)); ($RES_AUX_705)
(16)      [SCAL] (1) fullMedium.h_in = fullMedium.adiabaticModel.state_in.h; ($RES_AUX_703)
(17)      [SCAL] (1) fullMedium.p_in = fullMedium.adiabaticModel.state_in.p; ($RES_AUX_702)
(18)      [SCAL] (1) fullMedium1.P_in_internal = -gain.k * fullMedium.P_in_internal; ($RES_SIM_179)
(19)      [SCAL] (1) fullMedium2.adiabaticModel.w_t_is = fullMedium2.adiabaticModel.h_out_is - fullMedium2.adiabaticModel.h_in; ($RES_SIM_255)
(20)      [SCAL] (1) fullMedium2.adiabaticModel.w_t = fullMedium2.h_out - fullMedium2.adiabaticModel.h_in; ($RES_SIM_254)
(21)      [SCAL] (1) fullMedium2.adiabaticModel.w_t = if $SEV_3 then fullMedium2.adiabaticModel.w_t_is / fullMedium2.eta_fixed else fullMedium2.adiabaticModel.w_t_is * fullMedium2.eta_fixed; ($RES_SIM_251)
(22)      [SCAL] (1) fullMedium.adiabaticModel.w_t_is = fullMedium.adiabaticModel.h_out_is - fullMedium.adiabaticModel.h_in; ($RES_SIM_335)
(23)      [SCAL] (1) fullMedium.adiabaticModel.w_t = fullMedium.h_out - fullMedium.adiabaticModel.h_in; ($RES_SIM_334)
(24)      [SCAL] (1) fullMedium.pRatio_fixed = fullMedium.p_out / fullMedium.p_in; ($RES_BND_529)
(25)      [SCAL] (1) source4.outlet.state.h = fullMedium2.adiabaticModel.state_in.h; ($RES_SIM_491)
(26)      [SCAL] (1) fullMedium.adiabaticModel.w_t = if $SEV_0 then fullMedium.adiabaticModel.w_t_is / fullMedium.eta_fixed else fullMedium.adiabaticModel.w_t_is * fullMedium.eta_fixed; ($RES_SIM_331)
(27)      [SCAL] (1) source4.outlet.state.p = source4.p0_par; ($RES_SIM_898)
(28)      [SCAL] (1) source.outlet.state.p = source.p0_par; ($RES_SIM_868)
(29)      [SCAL] (1) source4.outlet.state.h = ThermofluidStream.Media.myMedia.Water.IF97_Utilities.h_props_pT(source4.p0_par, source4.T0_par, ThermofluidStream.Media.myMedia.Water.IF97_Utilities.waterBaseProp_pT(source4.p0_par, source4.T0_par, 0)); ($RES_SIM_895)
(30)      [SCAL] (1) source.outlet.state.h = fullMedium.adiabaticModel.state_in.h; ($RES_SIM_521)
(31)      [SCAL] (1) source.outlet.state.h = ThermofluidStream.Media.myMedia.Water.IF97_Utilities.h_props_pT(source.p0_par, source.T0_par, ThermofluidStream.Media.myMedia.Water.IF97_Utilities.waterBaseProp_pT(source.p0_par, source.T0_par, 0)); ($RES_SIM_865)
(32)      [SCAL] (1) source4.outlet.state.phase = 1; ($RES_SIM_894)
(33)      [SCAL] (1) source.outlet.state.phase = 1; ($RES_SIM_864)


State Candidate Variables (31/31)
***********************************
(1)       [ALGB] (1) output Real source4.outlet.state.h (start = 1e5, min = -1e10, max = 1e10, nominal = 5e5)
(2)       [ALGB] (1) Real fullMedium2.p_out (start = 5e6, min = 611.657, max = 1e8, nominal = 1e6)
(3)       [ALGB] (1) Real fullMedium2.h_in = ThermofluidStream.Idealized.Tests.Processes.Adiabatic.PumpConstant.fullMedium2.Medium.specificEnthalpy(fullMedium2.adiabaticModel.state_in) (start = 1e5, min = -1e10, max = 1e10, nominal = 5e5)
(4)       [ALGB] (1) Real fullMedium.p_in = ThermofluidStream.Idealized.Tests.Processes.Adiabatic.PumpConstant.fullMedium.Medium.pressure(fullMedium.adiabaticModel.state_in) (start = 5e6, min = 611.657, max = 1e8, nominal = 1e6)
(5)       [ALGB] (1) Real fullMedium2.h_out (start = 1e5, min = -1e10, max = 1e10, nominal = 5e5)
(6)       [ALGB] (1) Real fullMedium.p_out (start = 5e6, min = 611.657, max = 1e8, nominal = 1e6)
(7)       [ALGB] (1) final Real fullMedium.adiabaticModel.w_t_is
(8)       [ALGB] (1) Real fullMedium.dh
(9)       [ALGB] (1) final input Real fullMedium2.adiabaticModel.state_in.h = fullMedium2.inlet.state.h (start = 1e5, min = -1e10, max = 1e10, nominal = 5e5)
(10)      [ALGB] (1) Real fullMedium1.P_in_internal
(11)      [ALGB] (1) final Real fullMedium2.adiabaticModel.h_in = ThermofluidStream.Idealized.Tests.Processes.Adiabatic.PumpConstant.fullMedium2.adiabaticModel.Medium.specificEnthalpy(fullMedium2.adiabaticModel.state_in) (start = 1e5, min = -1e10, max = 1e10, nominal = 5e5)
(12)      [ALGB] (1) final Real fullMedium.adiabaticModel.h_in = ThermofluidStream.Idealized.Tests.Processes.Adiabatic.PumpConstant.fullMedium.adiabaticModel.Medium.specificEnthalpy(fullMedium.adiabaticModel.state_in) (start = 1e5, min = -1e10, max = 1e10, nominal = 5e5)
(13)      [ALGB] (1) Real fullMedium.h_out (start = 1e5, min = -1e10, max = 1e10, nominal = 5e5)
(14)      [ALGB] (1) output Real source.outlet.state.h (start = 1e5, min = -1e10, max = 1e10, nominal = 5e5)
(15)      [ALGB] (1) final Real fullMedium.adiabaticModel.s_in = ThermofluidStream.Idealized.Tests.Processes.Adiabatic.PumpConstant.fullMedium.adiabaticModel.Medium.specificEntropy(fullMedium.adiabaticModel.state_in) (min = -1e7, max = 1e7, nominal = 1000.0)
(16)      [ALGB] (1) Real fullMedium2.dh
(17)      [ALGB] (1) final Real fullMedium2.adiabaticModel.s_in = ThermofluidStream.Idealized.Tests.Processes.Adiabatic.PumpConstant.fullMedium2.adiabaticModel.Medium.specificEntropy(fullMedium2.adiabaticModel.state_in) (min = -1e7, max = 1e7, nominal = 1000.0)
(18)      [ALGB] (1) output Real source.outlet.state.p (start = 5e6, min = 611.657, max = 1e8, nominal = 1e6)
(19)      [ALGB] (1) final input Real fullMedium2.adiabaticModel.state_in.p = fullMedium2.inlet.state.p (start = 5e6, min = 611.657, max = 1e8, nominal = 1e6)
(20)      [ALGB] (1) output Real source4.outlet.state.p (start = 5e6, min = 611.657, max = 1e8, nominal = 1e6)
(21)      [ALGB] (1) final Real fullMedium2.adiabaticModel.w_t_is
(22)      [ALGB] (1) final Real fullMedium2.adiabaticModel.w_t
(23)      [ALGB] (1) final Real fullMedium2.adiabaticModel.h_out_is = ThermofluidStream.Idealized.Tests.Processes.Adiabatic.PumpConstant.fullMedium2.adiabaticModel.Medium.specificEnthalpy_psX(fullMedium2.p_out, fullMedium2.adiabaticModel.s_in, {}, 0) (start = 1e5, min = -1e10, max = 1e10, nominal = 5e5)
(24)      [STAT] (1) Real fullMedium2.m_flow = fullMedium2.m_flow (StateSelect = default)
(25)      [ALGB] (1) Real fullMedium2.p_in = ThermofluidStream.Idealized.Tests.Processes.Adiabatic.PumpConstant.fullMedium2.Medium.pressure(fullMedium2.adiabaticModel.state_in) (start = 5e6, min = 611.657, max = 1e8, nominal = 1e6)
(26)      [ALGB] (1) Real fullMedium.h_in = ThermofluidStream.Idealized.Tests.Processes.Adiabatic.PumpConstant.fullMedium.Medium.specificEnthalpy(fullMedium.adiabaticModel.state_in) (start = 1e5, min = -1e10, max = 1e10, nominal = 5e5)
(27)      [ALGB] (1) final input Real fullMedium.adiabaticModel.state_in.p = fullMedium.inlet.state.p (start = 5e6, min = 611.657, max = 1e8, nominal = 1e6)
(28)      [ALGB] (1) final input Real fullMedium.adiabaticModel.state_in.h = fullMedium.inlet.state.h (start = 1e5, min = -1e10, max = 1e10, nominal = 5e5)
(29)      [ALGB] (1) final Real fullMedium.adiabaticModel.h_out_is = ThermofluidStream.Idealized.Tests.Processes.Adiabatic.PumpConstant.fullMedium.adiabaticModel.Medium.specificEnthalpy_psX(fullMedium.p_out, fullMedium.adiabaticModel.s_in, {}, 0) (start = 1e5, min = -1e10, max = 1e10, nominal = 5e5)
(30)      [ALGB] (1) final Real fullMedium.adiabaticModel.w_t
(31)      [ALGB] (1) Real fullMedium.P_in_internal
"
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[Calling sys.exit(0), Time elapsed: 4.39458226300485]