Running: ./testmodel.py --libraries=/home/hudson/saved_omc/libraries/.openmodelica/libraries --ompython_omhome=/usr ClaRa_dev_ClaRa.Components.VolumesValvesFittings.Fittings.Check.Test_SprayInjector.conf.json
loadFile("/home/hudson/saved_omc/libraries/.openmodelica/libraries/SMArtIInt 0.2.2-main/package.mo", uses=false)
loadFile("/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.8.1-main/package.mo", uses=false)
loadFile("/home/hudson/saved_omc/libraries/.openmodelica/libraries/ModelicaServices 4.0.0+maint.om/package.mo", uses=false)
loadFile("/home/hudson/saved_omc/libraries/.openmodelica/libraries/Complex 4.0.0+maint.om/package.mo", uses=false)
loadFile("/home/hudson/saved_omc/libraries/.openmodelica/libraries/Modelica 4.0.0+maint.om/package.mo", uses=false)
loadFile("/home/hudson/saved_omc/libraries/.openmodelica/libraries/ClaRa 1.8.2-main/package.mo", uses=false)
Using package ClaRa with version 1.8.2 (/home/hudson/saved_omc/libraries/.openmodelica/libraries/ClaRa 1.8.2-main/package.mo)
Using package Modelica with version 4.0.0 (/home/hudson/saved_omc/libraries/.openmodelica/libraries/Modelica 4.0.0+maint.om/package.mo)
Using package Complex with version 4.0.0 (/home/hudson/saved_omc/libraries/.openmodelica/libraries/Complex 4.0.0+maint.om/package.mo)
Using package ModelicaServices with version 4.0.0 (/home/hudson/saved_omc/libraries/.openmodelica/libraries/ModelicaServices 4.0.0+maint.om/package.mo)
Using package TILMedia with version 1.8.1 ClaRa (/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.8.1-main/package.mo)
Using package SMArtIInt with version 0.2.2 (/home/hudson/saved_omc/libraries/.openmodelica/libraries/SMArtIInt 0.2.2-main/package.mo)
Running command: translateModel(ClaRa.Components.VolumesValvesFittings.Fittings.Check.Test_SprayInjector,tolerance=1e-06,outputFormat="mat",numberOfIntervals=5000,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|NonlinearSystems.initialization.4..Calls|NonlinearSystems.initialization.4..Iterations|NonlinearSystems.initialization.4..Jacobians|NonlinearSystems.initialization.4..Residues|NonlinearSystems.initialization.5..Calls|NonlinearSystems.initialization.5..Iterations|NonlinearSystems.initialization.5..Jacobians|NonlinearSystems.initialization.5..Residues|NonlinearSystems.initialization.6..Calls|NonlinearSystems.initialization.6..Iterations|NonlinearSystems.initialization.6..Jacobians|NonlinearSystems.initialization.6..Residues|NonlinearSystems.simplified_homotopy_initialization.1..Calls|NonlinearSystems.simplified_homotopy_initialization.1..Iterations|NonlinearSystems.simplified_homotopy_initialization.1..Jacobians|NonlinearSystems.simplified_homotopy_initialization.1..Residues|NonlinearSystems.simplified_homotopy_initialization.2..Calls|NonlinearSystems.simplified_homotopy_initialization.2..Iterations|NonlinearSystems.simplified_homotopy_initialization.2..Jacobians|NonlinearSystems.simplified_homotopy_initialization.2..Residues|NonlinearSystems.simulation.1..Calls|NonlinearSystems.simulation.1..Iterations|NonlinearSystems.simulation.1..Jacobians|NonlinearSystems.simulation.1..Residues|NonlinearSystems.simulation.2..Calls|NonlinearSystems.simulation.2..Iterations|NonlinearSystems.simulation.2..Jacobians|NonlinearSystems.simulation.2..Residues|NonlinearSystems.simulation.3..Calls|NonlinearSystems.simulation.3..Iterations|NonlinearSystems.simulation.3..Jacobians|NonlinearSystems.simulation.3..Residues|NonlinearSystems.simulation.4..Calls|NonlinearSystems.simulation.4..Iterations|NonlinearSystems.simulation.4..Jacobians|NonlinearSystems.simulation.4..Residues|NonlinearSystems.simulation.5..Calls|NonlinearSystems.simulation.5..Iterations|NonlinearSystems.simulation.5..Jacobians|NonlinearSystems.simulation.5..Residues|Time|chk|chk1|injector.Delta_p_nom|injector.N|injector.N_wall|injector.Tau|injector.checkValve|injector.diameter_i|injector.diameter_o|injector.eye.T|injector.eye.h|injector.eye.m_flow|injector.eye.p|injector.eye.s|injector.eye_int.1..T|injector.eye_int.1..h|injector.eye_int.1..m_flow|injector.eye_int.1..p|injector.eye_int.1..s|injector.h_nom_Main|injector.h_nom_Spray|injector.h_start_Main|injector.h_start_Spray|injector.initOption|injector.inlet1.h_outflow|injector.inlet1.m_flow|injector.inlet1.p|injector.inlet2.h_outflow|injector.inlet2.m_flow|injector.inlet2.p|injector.length|injector.m_flow_nom_main|injector.m_flow_nom_spray|injector.mixingZone.H_flow_in.1.|injector.mixingZone.H_flow_in.2.|injector.mixingZone.H_flow_out|der.injector.mixingZone.h.|der.injector.mixingZone.p.|injector.mixingZone.drhodt|injector.mixingZone.eye_int.1..T|injector.mixingZone.eye_int.1..h|injector.mixingZone.eye_int.1..m_flow|injector.mixingZone.eye_int.1..p|injector.mixingZone.eye_int.1..s|injector.mixingZone.h|injector.mixingZone.h_nom|injector.mixingZone.h_start|injector.mixingZone.initOption|injector.mixingZone.inlet1.h_outflow|injector.mixingZone.inlet1.m_flow|injector.mixingZone.inlet1.p|injector.mixingZone.inlet2.h_outflow|injector.mixingZone.inlet2.m_flow|injector.mixingZone.inlet2.p|injector.mixingZone.m_flow_in_nom.1.|injector.mixingZone.m_flow_in_nom.2.|injector.mixingZone.mass|injector.mixingZone.outlet.h_outflow|injector.mixingZone.outlet.m_flow|injector.mixingZone.outlet.p|injector.mixingZone.p|injector.mixingZone.p_nom|injector.mixingZone.p_start|injector.mixingZone.preciseTwoPhase|injector.mixingZone.pressureLossIn1.dp|injector.mixingZone.pressureLossIn1.hasPressureLoss|injector.mixingZone.pressureLossIn1.m_flow|injector.mixingZone.pressureLossIn2.dp|injector.mixingZone.pressureLossIn2.hasPressureLoss|injector.mixingZone.pressureLossIn2.m_flow|injector.mixingZone.pressureLossOut.dp|injector.mixingZone.pressureLossOut.hasPressureLoss|injector.mixingZone.pressureLossOut.m_flow|injector.mixingZone.showData|injector.mixingZone.showExpertSummary|injector.mixingZone.summary.fluid.H|injector.mixingZone.summary.fluid.T|injector.mixingZone.summary.fluid.T_sat|injector.mixingZone.summary.fluid.h|injector.mixingZone.summary.fluid.h_bub|injector.mixingZone.summary.fluid.h_dew|injector.mixingZone.summary.fluid.mass|injector.mixingZone.summary.fluid.p|injector.mixingZone.summary.fluid.rho|injector.mixingZone.summary.fluid.s|injector.mixingZone.summary.fluid.showExpertSummary|injector.mixingZone.summary.fluid.steamQuality|injector.mixingZone.summary.inlet1.H_flow|injector.mixingZone.summary.inlet1.T|injector.mixingZone.summary.inlet1.h|injector.mixingZone.summary.inlet1.m_flow|injector.mixingZone.summary.inlet1.p|injector.mixingZone.summary.inlet1.rho|injector.mixingZone.summary.inlet1.s|injector.mixingZone.summary.inlet1.showExpertSummary|injector.mixingZone.summary.inlet1.steamQuality|injector.mixingZone.summary.inlet2.H_flow|injector.mixingZone.summary.inlet2.T|injector.mixingZone.summary.inlet2.h|injector.mixingZone.summary.inlet2.m_flow|injector.mixingZone.summary.inlet2.p|injector.mixingZone.summary.inlet2.rho|injector.mixingZone.summary.inlet2.s|injector.mixingZone.summary.inlet2.showExpertSummary|injector.mixingZone.summary.inlet2.steamQuality|injector.mixingZone.summary.outlet.H_flow|injector.mixingZone.summary.outlet.T|injector.mixingZone.summary.outlet.h|injector.mixingZone.summary.outlet.m_flow|injector.mixingZone.summary.outlet.p|injector.mixingZone.summary.outlet.rho|injector.mixingZone.summary.outlet.s|injector.mixingZone.summary.outlet.showExpertSummary|injector.mixingZone.summary.outlet.steamQuality|injector.mixingZone.summary.outline.volume_tot|injector.mixingZone.useHomotopy|injector.mixingZone.volume|injector.opening|injector.opening_leak_|der.injector.outflowZone.p.|injector.outflowZone.fluidIn.M|injector.outflowZone.fluidIn.M_i.1.|injector.outflowZone.fluidIn.T|injector.outflowZone.fluidIn.VLE.T_l|injector.outflowZone.fluidIn.VLE.T_v|injector.outflowZone.fluidIn.VLE.d_l|injector.outflowZone.fluidIn.VLE.d_v|injector.outflowZone.fluidIn.VLE.h_l|injector.outflowZone.fluidIn.VLE.h_v|injector.outflowZone.fluidIn.VLE.nc|injector.outflowZone.fluidIn.VLE.p_l|injector.outflowZone.fluidIn.VLE.p_v|injector.outflowZone.fluidIn.VLE.s_l|injector.outflowZone.fluidIn.VLE.s_v|injector.outflowZone.fluidIn.VLEAdditional.beta_l|injector.outflowZone.fluidIn.VLEAdditional.beta_v|injector.outflowZone.fluidIn.VLEAdditional.cp_l|injector.outflowZone.fluidIn.VLEAdditional.cp_v|injector.outflowZone.fluidIn.VLEAdditional.kappa_l|injector.outflowZone.fluidIn.VLEAdditional.kappa_v|injector.outflowZone.fluidIn.VLETransp.Pr_l|injector.outflowZone.fluidIn.VLETransp.Pr_v|injector.outflowZone.fluidIn.VLETransp.eta_l|injector.outflowZone.fluidIn.VLETransp.eta_v|injector.outflowZone.fluidIn.VLETransp.lambda_l|injector.outflowZone.fluidIn.VLETransp.lambda_v|injector.outflowZone.fluidIn.beta|injector.outflowZone.fluidIn.computeSurfaceTension|injector.outflowZone.fluidIn.computeTransportProperties|injector.outflowZone.fluidIn.computeVLEAdditionalProperties|injector.outflowZone.fluidIn.computeVLETransportProperties|injector.outflowZone.fluidIn.cp|injector.outflowZone.fluidIn.crit.T|injector.outflowZone.fluidIn.crit.d|injector.outflowZone.fluidIn.crit.h|injector.outflowZone.fluidIn.crit.p|injector.outflowZone.fluidIn.crit.s|injector.outflowZone.fluidIn.cv|injector.outflowZone.fluidIn.d|injector.outflowZone.fluidIn.deactivateDensityDerivatives|injector.outflowZone.fluidIn.deactivateTwoPhaseRegion|injector.outflowZone.fluidIn.drhodh_pxi|injector.outflowZone.fluidIn.drhodp_hxi|injector.outflowZone.fluidIn.gamma|injector.outflowZone.fluidIn.h|injector.outflowZone.fluidIn.interpolateTransportProperties|injector.outflowZone.fluidIn.kappa|injector.outflowZone.fluidIn.p|injector.outflowZone.fluidIn.q|injector.outflowZone.fluidIn.s|injector.outflowZone.fluidIn.stateSelectPreferForInputs|injector.outflowZone.fluidIn.transp.Pr|injector.outflowZone.fluidIn.transp.eta|injector.outflowZone.fluidIn.transp.lambda|injector.outflowZone.fluidIn.transp.sigma|injector.outflowZone.fluidIn.vleFluidPointer.id|injector.outflowZone.fluidIn.w|injector.outflowZone.fluidOut.M|injector.outflowZone.fluidOut.M_i.1.|injector.outflowZone.fluidOut.T|injector.outflowZone.fluidOut.VLE.T_l|injector.outflowZone.fluidOut.VLE.T_v|injector.outflowZone.fluidOut.VLE.d_l|injector.outflowZone.fluidOut.VLE.d_v|injector.outflowZone.fluidOut.VLE.h_l|injector.outflowZone.fluidOut.VLE.h_v|injector.outflowZone.fluidOut.VLE.nc|injector.outflowZone.fluidOut.VLE.p_l|injector.outflowZone.fluidOut.VLE.p_v|injector.outflowZone.fluidOut.VLE.s_l|injector.outflowZone.fluidOut.VLE.s_v|injector.outflowZone.fluidOut.VLEAdditional.beta_l|injector.outflowZone.fluidOut.VLEAdditional.beta_v|injector.outflowZone.fluidOut.VLEAdditional.cp_l|injector.outflowZone.fluidOut.VLEAdditional.cp_v|injector.outflowZone.fluidOut.VLEAdditional.kappa_l|injector.outflowZone.fluidOut.VLEAdditional.kappa_v|injector.outflowZone.fluidOut.VLETransp.Pr_l|injector.outflowZone.fluidOut.VLETransp.Pr_v|injector.outflowZone.fluidOut.VLETransp.eta_l|injector.outflowZone.fluidOut.VLETransp.eta_v|injector.outflowZone.fluidOut.VLETransp.lambda_l|injector.outflowZone.fluidOut.VLETransp.lambda_v|injector.outflowZone.fluidOut.beta|injector.outflowZone.fluidOut.computeSurfaceTension|injector.outflowZone.fluidOut.computeTransportProperties|injector.outflowZone.fluidOut.computeVLEAdditionalProperties|injector.outflowZone.fluidOut.computeVLETransportProperties|injector.outflowZone.fluidOut.cp|injector.outflowZone.fluidOut.crit.T|injector.outflowZone.fluidOut.crit.d|injector.outflowZone.fluidOut.crit.h|injector.outflowZone.fluidOut.crit.p|injector.outflowZone.fluidOut.crit.s|injector.outflowZone.fluidOut.cv|injector.outflowZone.fluidOut.d|injector.outflowZone.fluidOut.deactivateDensityDerivatives|injector.outflowZone.fluidOut.deactivateTwoPhaseRegion|injector.outflowZone.fluidOut.drhodh_pxi|injector.outflowZone.fluidOut.drhodp_hxi|injector.outflowZone.fluidOut.gamma|injector.outflowZone.fluidOut.h|injector.outflowZone.fluidOut.interpolateTransportProperties|injector.outflowZone.fluidOut.kappa|injector.outflowZone.fluidOut.p|injector.outflowZone.fluidOut.q|injector.outflowZone.fluidOut.s|injector.outflowZone.fluidOut.stateSelectPreferForInputs|injector.outflowZone.fluidOut.transp.Pr|injector.outflowZone.fluidOut.transp.eta|injector.outflowZone.fluidOut.transp.lambda|injector.outflowZone.fluidOut.transp.sigma|injector.outflowZone.fluidOut.vleFluidPointer.id|injector.outflowZone.fluidOut.w|injector.outflowZone.geo.A_cross|injector.outflowZone.geo.A_front|injector.outflowZone.geo.A_heat.1.|injector.outflowZone.geo.A_heat_CF.1.|injector.outflowZone.geo.A_hor|injector.outflowZone.geo.CF_geo.1.|injector.outflowZone.geo.N_heat|injector.outflowZone.geo.N_inlet|injector.outflowZone.geo.N_outlet|injector.outflowZone.geo.N_passes|injector.outflowZone.geo.N_tubes|injector.outflowZone.geo.diameter|injector.outflowZone.geo.diameter_hyd|injector.outflowZone.geo.height_fill|injector.outflowZone.geo.length|injector.outflowZone.geo.orientation|injector.outflowZone.geo.shape.1,1.|injector.outflowZone.geo.shape.1,2.|injector.outflowZone.geo.shape.2,1.|injector.outflowZone.geo.shape.2,2.|injector.outflowZone.geo.volume|injector.outflowZone.geo.z_in.1.|injector.outflowZone.geo.z_out.1.|injector.outflowZone.h_nom|injector.outflowZone.h_start|injector.outflowZone.heat.Q_flow|injector.outflowZone.heat.T|injector.outflowZone.heatSurfaceAlloc|injector.outflowZone.heattransfer.HR|injector.outflowZone.heattransfer.HR_nom|injector.outflowZone.heattransfer.HT_type|injector.outflowZone.heattransfer.alpha|injector.outflowZone.heattransfer.alpha_nom|injector.outflowZone.heattransfer.heat.Q_flow|injector.outflowZone.heattransfer.heat.T|injector.outflowZone.heattransfer.heatSurfaceAlloc|injector.outflowZone.initOption|injector.outflowZone.inlet.h_outflow|injector.outflowZone.inlet.m_flow|injector.outflowZone.inlet.p|injector.outflowZone.m_flow_nom|injector.outflowZone.mass|injector.outflowZone.outlet.h_outflow|injector.outflowZone.outlet.m_flow|injector.outflowZone.outlet.p|injector.outflowZone.p|injector.outflowZone.p_nom|injector.outflowZone.p_start|injector.outflowZone.phaseBorder.Delta_p_geo_in|injector.outflowZone.phaseBorder.Delta_p_geo_out|injector.outflowZone.phaseBorder.h_inflow|injector.outflowZone.phaseBorder.h_outflow|injector.outflowZone.phaseBorder.level_abs|injector.outflowZone.phaseBorder.level_rel|injector.outflowZone.phaseBorder.level_rel_start|injector.outflowZone.phaseBorder.provideDensityDerivative|injector.outflowZone.pressureLoss.Delta_p|injector.outflowZone.pressureLoss.Delta_p_nom|injector.outflowZone.showExpertSummary|injector.outflowZone.summary.fluid.H|injector.outflowZone.summary.fluid.T|injector.outflowZone.summary.fluid.T_sat|injector.outflowZone.summary.fluid.h|injector.outflowZone.summary.fluid.h_bub|injector.outflowZone.summary.fluid.h_dew|injector.outflowZone.summary.fluid.mass|injector.outflowZone.summary.fluid.p|injector.outflowZone.summary.fluid.rho|injector.outflowZone.summary.fluid.s|injector.outflowZone.summary.fluid.showExpertSummary|injector.outflowZone.summary.fluid.steamQuality|injector.outflowZone.summary.inlet.H_flow|injector.outflowZone.summary.inlet.T|injector.outflowZone.summary.inlet.h|injector.outflowZone.summary.inlet.m_flow|injector.outflowZone.summary.inlet.p|injector.outflowZone.summary.inlet.rho|injector.outflowZone.summary.inlet.s|injector.outflowZone.summary.inlet.showExpertSummary|injector.outflowZone.summary.inlet.steamQuality|injector.outflowZone.summary.outlet.H_flow|injector.outflowZone.summary.outlet.T|injector.outflowZone.summary.outlet.h|injector.outflowZone.summary.outlet.m_flow|injector.outflowZone.summary.outlet.p|injector.outflowZone.summary.outlet.rho|injector.outflowZone.summary.outlet.s|injector.outflowZone.summary.outlet.showExpertSummary|injector.outflowZone.summary.outlet.steamQuality|injector.outflowZone.summary.outline.A_heat|injector.outflowZone.summary.outline.Delta_p|injector.outflowZone.summary.outline.Q_flow_tot|injector.outflowZone.summary.outline.showExpertSummary|injector.outflowZone.summary.outline.volume_tot|injector.outflowZone.useHomotopy|injector.outlet.h_outflow|injector.outlet.m_flow|injector.outlet.p|injector.p_nom|injector.p_start|injector.preciseTwoPhase|injector.showData|injector.showExpertSumm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ctor1.mixingZone.fluidOut.1..VLEAdditional.cp_l|injector1.mixingZone.fluidOut.1..VLEAdditional.cp_v|injector1.mixingZone.fluidOut.1..VLEAdditional.kappa_l|injector1.mixingZone.fluidOut.1..VLEAdditional.kappa_v|injector1.mixingZone.fluidOut.1..VLETransp.Pr_l|injector1.mixingZone.fluidOut.1..VLETransp.Pr_v|injector1.mixingZone.fluidOut.1..VLETransp.eta_l|injector1.mixingZone.fluidOut.1..VLETransp.eta_v|injector1.mixingZone.fluidOut.1..VLETransp.lambda_l|injector1.mixingZone.fluidOut.1..VLETransp.lambda_v|injector1.mixingZone.fluidOut.1..beta|injector1.mixingZone.fluidOut.1..computeSurfaceTension|injector1.mixingZone.fluidOut.1..computeTransportProperties|injector1.mixingZone.fluidOut.1..computeVLEAdditionalProperties|injector1.mixingZone.fluidOut.1..computeVLETransportProperties|injector1.mixingZone.fluidOut.1..cp|injector1.mixingZone.fluidOut.1..crit.T|injector1.mixingZone.fluidOut.1..crit.d|injector1.mixingZone.fluidOut.1..crit.h|injector1.mixingZone.fluidOut.1..crit.p|injector1.mixingZone.fluidOut.1..crit.s|injector1.mixingZone.fluidOut.1..cv|injector1.mixingZone.fluidOut.1..d|injector1.mixingZone.fluidOut.1..deactivateDensityDerivatives|injector1.mixingZone.fluidOut.1..deactivateTwoPhaseRegion|injector1.mixingZone.fluidOut.1..drhodh_pxi|injector1.mixingZone.fluidOut.1..drhodp_hxi|injector1.mixingZone.fluidOut.1..gamma|injector1.mixingZone.fluidOut.1..h|injector1.mixingZone.fluidOut.1..interpolateTransportProperties|injector1.mixingZone.fluidOut.1..kappa|injector1.mixingZone.fluidOut.1..p|injector1.mixingZone.fluidOut.1..q|injector1.mixingZone.fluidOut.1..s|injector1.mixingZone.fluidOut.1..stateSelectPreferForInputs|injector1.mixingZone.fluidOut.1..transp.Pr|injector1.mixingZone.fluidOut.1..transp.eta|injector1.mixingZone.fluidOut.1..transp.lambda|injector1.mixingZone.fluidOut.1..transp.sigma|injector1.mixingZone.fluidOut.1..vleFluidPointer.id|injector1.mixingZone.fluidOut.1..w|injector1.mixingZone.geo.A_cross|injector1.mixingZone.geo.A_front|injector1.mixingZone.geo.A_heat.1.|injector1.mixingZone.geo.A_heat_CF.1.|injector1.mixingZone.geo.A_hor|injector1.mixingZone.geo.CF_geo.1.|injector1.mixingZone.geo.N_heat|injector1.mixingZone.geo.N_inlet|injector1.mixingZone.geo.N_outlet|injector1.mixingZone.geo.height_fill|injector1.mixingZone.geo.shape.1,1.|injector1.mixingZone.geo.shape.1,2.|injector1.mixingZone.geo.shape.2,1.|injector1.mixingZone.geo.shape.2,2.|injector1.mixingZone.geo.volume|injector1.mixingZone.geo.z_in.1.|injector1.mixingZone.geo.z_in.2.|injector1.mixingZone.geo.z_out.1.|injector1.mixingZone.h_liq|injector1.mixingZone.h_liq_start|injector1.mixingZone.h_vap|injector1.mixingZone.h_vap_start|injector1.mixingZone.heatSurfaceAlloc|injector1.mixingZone.heat.1..Q_flow|injector1.mixingZone.heat.1..T|injector1.mixingZone.heat.2..Q_flow|injector1.mixingZone.heat.2..T|injector1.mixingZone.heattransfer.Delta_T_mean.1.|injector1.mixingZone.heattransfer.Delta_T_mean.2.|injector1.mixingZone.heattransfer.HR.1.|injector1.mixingZone.heattransfer.HR.2.|injector1.mixingZone.heattransfer.HR_nom.1.|injector1.mixingZone.heattransfer.HR_nom.2.|injector1.mixingZone.heattransfer.Q_flow_tot|injector1.mixingZone.heattransfer.alpha.1.|injector1.mixingZone.heattransfer.alpha.2.|injector1.mixingZone.heattransfer.alpha_nom.1.|injector1.mixingZone.heattransfer.alpha_nom.2.|injector1.mixingZone.heattransfer.heatSurfaceAlloc|injector1.mixingZone.heattransfer.heat.1..Q_flow|injector1.mixingZone.heattransfer.heat.1..T|injector1.mixingZone.heattransfer.heat.2..Q_flow|injector1.mixingZone.heattransfer.heat.2..T|injector1.mixingZone.initOption|injector1.mixingZone.inlet.1..h_outflow|injector1.mixingZone.inlet.1..m_flow|injector1.mixingZone.inlet.1..p|injector1.mixingZone.inlet.2..h_outflow|injector1.mixingZone.inlet.2..m_flow|injector1.mixingZone.inlet.2..p|injector1.mixingZone.level_rel_start|injector1.mixingZone.m_flow_cond|injector1.mixingZone.m_flow_evap|injector1.mixingZone.m_flow_nom|injector1.mixingZone.mass_liq|injector1.mixingZone.mass_vap|injector1.mixingZone.outlet.1..h_outflow|injector1.mixingZone.outlet.1..m_flow|injector1.mixingZone.outlet.1..p|injector1.mixingZone.p_liq|injector1.mixingZone.p_nom|injector1.mixingZone.p_start|injector1.mixingZone.p_vap|injector1.mixingZone.phaseBorder.Delta_p_geo_in.1.|injector1.mixingZone.phaseBorder.Delta_p_geo_in.2.|injector1.mixingZone.phaseBorder.Delta_p_geo_out.1.|injector1.mixingZone.phaseBorder.H_flow_inliq.1.|injector1.mixingZone.phaseBorder.H_flow_inliq.2.|injector1.mixingZone.phaseBorder.H_flow_invap.1.|injector1.mixingZone.phaseBorder.H_flow_invap.2.|injector1.mixingZone.phaseBorder.H_flow_outliq.1.|injector1.mixingZone.phaseBorder.H_flow_outvap.1.|injector1.mixingZone.phaseBorder.eps_mix.1.|injector1.mixingZone.phaseBorder.eps_mix.2.|injector1.mixingZone.phaseBorder.level_abs|injector1.mixingZone.phaseBorder.level_rel|injector1.mixingZone.phaseBorder.level_rel_start|injector1.mixingZone.phaseBorder.m_flow_inliq.1.|injector1.mixingZone.phaseBorder.m_flow_inliq.2.|injector1.m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ctor1.mixingZone.fluidOut.1..VLEAdditional.cp_l|injector1.mixingZone.fluidOut.1..VLEAdditional.cp_v|injector1.mixingZone.fluidOut.1..VLEAdditional.kappa_l|injector1.mixingZone.fluidOut.1..VLEAdditional.kappa_v|injector1.mixingZone.fluidOut.1..VLETransp.Pr_l|injector1.mixingZone.fluidOut.1..VLETransp.Pr_v|injector1.mixingZone.fluidOut.1..VLETransp.eta_l|injector1.mixingZone.fluidOut.1..VLETransp.eta_v|injector1.mixingZone.fluidOut.1..VLETransp.lambda_l|injector1.mixingZone.fluidOut.1..VLETransp.lambda_v|injector1.mixingZone.fluidOut.1..beta|injector1.mixingZone.fluidOut.1..computeSurfaceTension|injector1.mixingZone.fluidOut.1..computeTransportProperties|injector1.mixingZone.fluidOut.1..computeVLEAdditionalProperties|injector1.mixingZone.fluidOut.1..computeVLETransportProperties|injector1.mixingZone.fluidOut.1..cp|injector1.mixingZone.fluidOut.1..crit.T|injector1.mixingZone.fluidOut.1..crit.d|injector1.mixingZone.fluidOut.1..crit.h|injector1.mixingZone.fluidOut.1..crit.p|injector1.mixingZone.fluidOut.1..crit.s|injector1.mixingZone.fluidOut.1..cv|injector1.mixingZone.fluidOut.1..d|injector1.mixingZone.fluidOut.1..deactivateDensityDerivatives|injector1.mixingZone.fluidOut.1..deactivateTwoPhaseRegion|injector1.mixingZone.fluidOut.1..drhodh_pxi|injector1.mixingZone.fluidOut.1..drhodp_hxi|injector1.mixingZone.fluidOut.1..gamma|injector1.mixingZone.fluidOut.1..h|injector1.mixingZone.fluidOut.1..interpolateTransportProperties|injector1.mixingZone.fluidOut.1..kappa|injector1.mixingZone.fluidOut.1..p|injector1.mixingZone.fluidOut.1..q|injector1.mixingZone.fluidOut.1..s|injector1.mixingZone.fluidOut.1..stateSelectPreferForInputs|injector1.mixingZone.fluidOut.1..transp.Pr|injector1.mixingZone.fluidOut.1..transp.eta|injector1.mixingZone.fluidOut.1..transp.lambda|injector1.mixingZone.fluidOut.1..transp.sigma|injector1.mixingZone.fluidOut.1..vleFluidPointer.id|injector1.mixingZone.fluidOut.1..w|injector1.mixingZone.geo.A_cross|injector1.mixingZone.geo.A_front|injector1.mixingZone.geo.A_heat.1.|injector1.mixingZone.geo.A_heat_CF.1.|injector1.mixingZone.geo.A_hor|injector1.mixingZone.geo.CF_geo.1.|injector1.mixingZone.geo.N_heat|injector1.mixingZone.geo.N_inlet|injector1.mixingZone.geo.N_outlet|injector1.mixingZone.geo.height_fill|injector1.mixingZone.geo.shape.1,1.|injector1.mixingZone.geo.shape.1,2.|injector1.mixingZone.geo.shape.2,1.|injector1.mixingZone.geo.shape.2,2.|injector1.mixingZone.geo.volume|injector1.mixingZone.geo.z_in.1.|injector1.mixingZone.geo.z_in.2.|injector1.mixingZone.geo.z_out.1.|injector1.mixingZone.h_liq|injector1.mixingZone.h_liq_start|injector1.mixingZone.h_vap|injector1.mixingZone.h_vap_start|injector1.mixingZone.heatSurfaceAlloc|injector1.mixingZone.heat.1..Q_flow|injector1.mixingZone.heat.1..T|injector1.mixingZone.heat.2..Q_flow|injector1.mixingZone.heat.2..T|injector1.mixingZone.heattransfer.Delta_T_mean.1.|injector1.mixingZone.heattransfer.Delta_T_mean.2.|injector1.mixingZone.heattransfer.HR.1.|injector1.mixingZone.heattransfer.HR.2.|injector1.mixingZone.heattransfer.HR_nom.1.|injector1.mixingZone.heattransfer.HR_nom.2.|injector1.mixingZone.heattransfer.Q_flow_tot|injector1.mixingZone.heattransfer.alpha.1.|injector1.mixingZone.heattransfer.alpha.2.|injector1.mixingZone.heattransfer.alpha_nom.1.|injector1.mixingZone.heattransfer.alpha_nom.2.|injector1.mixingZone.heattransfer.heatSurfaceAlloc|injector1.mixingZone.heattransfer.heat.1..Q_flow|injector1.mixingZone.heattransfer.heat.1..T|injector1.mixingZone.heattransfer.heat.2..Q_flow|injector1.mixingZone.heattransfer.heat.2..T|injector1.mixingZone.initOption|injector1.mixingZone.inlet.1..h_outflow|injector1.mixingZone.inlet.1..m_flow|injector1.mixingZone.inlet.1..p|injector1.mixingZone.inlet.2..h_outflow|injector1.mixingZone.inlet.2..m_flow|injector1.mixingZone.inlet.2..p|injector1.mixingZone.level_rel_start|injector1.mixingZone.m_flow_cond|injector1.mixingZone.m_flow_evap|injector1.mixingZone.m_flow_nom|injector1.mixingZone.mass_liq|injector1.mixingZone.mass_vap|injector1.mixingZone.outlet.1..h_outflow|injector1.mixingZone.outlet.1..m_flow|injector1.mixingZone.outlet.1..p|injector1.mixingZone.p_liq|injector1.mixingZone.p_nom|injector1.mixingZone.p_start|injector1.mixingZone.p_vap|injector1.mixingZone.phaseBorder.Delta_p_geo_in.1.|injector1.mixingZone.phaseBorder.Delta_p_geo_in.2.|injector1.mixingZone.phaseBorder.Delta_p_geo_out.1.|injector1.mixingZone.phaseBorder.H_flow_inliq.1.|injector1.mixingZone.phaseBorder.H_flow_inliq.2.|injector1.mixingZone.phaseBorder.H_flow_invap.1.|injector1.mixingZone.phaseBorder.H_flow_invap.2.|injector1.mixingZone.phaseBorder.H_flow_outliq.1.|injector1.mixingZone.phaseBorder.H_flow_outvap.1.|injector1.mixingZone.phaseBorder.eps_mix.1.|injector1.mixingZone.phaseBorder.eps_mix.2.|injector1.mixingZone.phaseBorder.level_abs|injector1.mixingZone.phaseBorder.level_rel|injector1.mixingZone.phaseBorder.level_rel_start|injector1.mixingZone.phaseBorder.m_flow_inliq.1.|injector1.mixingZone.phaseBorder.m_flow_inliq.2.|injector1.m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Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/SMArtIInt 0.2.2-main/package.mo): time 0.009074/0.009074, allocations: 1.437 MB / 17.75 MB, free: 4.891 MB / 14.72 MB
Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.8.1-main/package.mo): time 0.113/0.113, allocations: 22.38 MB / 41.17 MB, free: 7.762 MB / 34.91 MB
Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/ModelicaServices 4.0.0+maint.om/package.mo): time 0.001161/0.001161, allocations: 108 kB / 48.65 MB, free: 256 kB / 34.91 MB
Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/Complex 4.0.0+maint.om/package.mo): time 0.001308/0.001308, allocations: 194.1 kB / 56.26 MB, free: 9.469 MB / 46.55 MB
Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/Modelica 4.0.0+maint.om/package.mo): time 1.342/1.342, allocations: 222.9 MB / 286.6 MB, free: 13.95 MB / 222.1 MB
Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/ClaRa 1.8.2-main/package.mo): time 0.9063/0.9063, allocations: 127.8 MB / 471.3 MB, free: 0.5508 MB / 366.1 MB
Notification: Performance of FrontEnd - loaded program: time 0.002336/0.002336, allocations: 131.8 kB / 0.6362 GB, free: 12.98 MB / 478.1 MB
Notification: Performance of FrontEnd - Absyn->SCode: time 0.3913/0.3936, allocations: 82.34 MB / 0.7166 GB, free: 9.547 MB / 0.5138 GB
Notification: Performance of NFInst.instantiate(ClaRa.Components.VolumesValvesFittings.Fittings.Check.Test_SprayInjector): time 0.0367/0.4304, allocations: 36.39 MB / 0.7521 GB, free: 11.41 MB / 0.545 GB
Notification: Performance of NFInst.instExpressions: time 0.04301/0.4734, allocations: 24.03 MB / 0.7756 GB, free: 3.316 MB / 0.5607 GB
Notification: Performance of NFInst.updateImplicitVariability: time 0.008987/0.4825, allocations: 159.2 kB / 0.7757 GB, free: 3.16 MB / 0.5607 GB
Notification: Performance of NFTyping.typeComponents: time 0.009791/0.4923, allocations: 3.789 MB / 0.7794 GB, free: 15.36 MB / 0.5763 GB
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/ClaRa 1.8.2-main/Components/VolumesValvesFittings/Fittings/Check/Test_SprayInjector.mo:19:1-19:147:writable] Warning: Conditional component 'H_flow' is used in a non-connect context.
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/ClaRa 1.8.2-main/Components/VolumesValvesFittings/Fittings/Check/Test_SprayInjector.mo:20:1-20:151:writable] Warning: Conditional component 'H_flow' is used in a non-connect context.
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/ClaRa 1.8.2-main/Components/VolumesValvesFittings/Fittings/SprayInjectorVLE_L3.mo:106:7-106:36:writable] Warning: Conditional component 's' is used in a non-connect context.
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/ClaRa 1.8.2-main/Components/VolumesValvesFittings/Fittings/SprayInjectorVLE_L3.mo:107:7-107:58:writable] Warning: Conditional component 'steamQuality' is used in a non-connect context.
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/ClaRa 1.8.2-main/Components/VolumesValvesFittings/Fittings/SprayInjectorVLE_L3.mo:109:7-109:40:writable] Warning: Conditional component 'rho' is used in a non-connect context.
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/ClaRa 1.8.2-main/Components/VolumesValvesFittings/Fittings/SprayInjectorVLE_L3.mo:116:7-116:30:writable] Warning: Conditional component 's' is used in a non-connect context.
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/ClaRa 1.8.2-main/Components/VolumesValvesFittings/Fittings/SprayInjectorVLE_L3.mo:117:7-117:52:writable] Warning: Conditional component 'steamQuality' is used in a non-connect context.
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/ClaRa 1.8.2-main/Components/VolumesValvesFittings/Fittings/SprayInjectorVLE_L3.mo:119:7-119:34:writable] Warning: Conditional component 'rho' is used in a non-connect context.
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.8.1-main/VLEFluidFunctions.mo:187:13-191:23:writable] Warning: Pure function 'TILMedia.Internals.VLEFluidConfigurations.FullyMixtureCompatible.VLEFluidFunctions.temperature_phxi' contains a call to impure function 'TILMedia.Internals.VLEFluidFunctions.temperature_phxi'.
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.8.1-main/VLEFluidFunctions.mo:177:13-181:19:writable] Warning: Pure function 'TILMedia.Internals.VLEFluidConfigurations.FullyMixtureCompatible.VLEFluidFunctions.density_phxi' contains a call to impure function 'TILMedia.Internals.VLEFluidFunctions.density_phxi'.
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/ClaRa 1.8.2-main/Components/VolumesValvesFittings/Fittings/SprayInjectorVLE_L3_advanced.mo:149:7-149:30:writable] Warning: Conditional component 's' is used in a non-connect context.
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/ClaRa 1.8.2-main/Components/VolumesValvesFittings/Fittings/SprayInjectorVLE_L3_advanced.mo:150:7-150:52:writable] Warning: Conditional component 'steamQuality' is used in a non-connect context.
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/ClaRa 1.8.2-main/Components/VolumesValvesFittings/Fittings/SprayInjectorVLE_L3_advanced.mo:152:7-152:34:writable] Warning: Conditional component 'rho' is used in a non-connect context.
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.8.1-main/VLEFluidFunctions.mo:777:13-781:24:writable] Warning: Pure function 'TILMedia.Internals.VLEFluidConfigurations.FullyMixtureCompatible.VLEFluidFunctions.bubbleDensity_pxi' contains a call to impure function 'TILMedia.Internals.VLEFluidFunctions.bubbleDensity_pxi'.
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.8.1-main/VLEFluidFunctions.mo:772:13-776:21:writable] Warning: Pure function 'TILMedia.Internals.VLEFluidConfigurations.FullyMixtureCompatible.VLEFluidFunctions.dewDensity_pxi' contains a call to impure function 'TILMedia.Internals.VLEFluidFunctions.dewDensity_pxi'.
Notification: Performance of NFTyping.typeBindings: time 0.01712/0.5095, allocations: 6.078 MB / 0.7854 GB, free: 9.246 MB / 0.5763 GB
Notification: Performance of NFTyping.typeClassSections: time 0.01246/0.5219, allocations: 5.494 MB / 0.7907 GB, free: 3.754 MB / 0.5763 GB
Notification: Performance of NFFlatten.flatten: time 0.02349/0.5455, allocations: 17.48 MB / 0.8078 GB, free: 2.223 MB / 0.5919 GB
Notification: Performance of NFFlatten.resolveConnections: time 0.01023/0.5557, allocations: 6.14 MB / 0.8138 GB, free: 11.99 MB / 0.6075 GB
Notification: Performance of NFEvalConstants.evaluate: time 0.01184/0.5676, allocations: 6.825 MB / 0.8205 GB, free: 5.145 MB / 0.6075 GB
Notification: Performance of NFSimplifyModel.simplify: time 0.0108/0.5784, allocations: 6.806 MB / 0.8271 GB, free: 14.31 MB / 0.6232 GB
Notification: Performance of NFPackage.collectConstants: time 0.003835/0.5823, allocations: 1.145 MB / 0.8282 GB, free: 13.17 MB / 0.6232 GB
Notification: Performance of NFFlatten.collectFunctions: time 0.007417/0.5897, allocations: 2.731 MB / 0.8309 GB, free: 10.44 MB / 0.6232 GB
Notification: Performance of NFScalarize.scalarize: time 0.005089/0.5948, allocations: 3.365 MB / 0.8342 GB, free: 7.062 MB / 0.6232 GB
Notification: Performance of NFVerifyModel.verify: time 0.01023/0.6051, allocations: 5.866 MB / 0.8399 GB, free: 1.168 MB / 0.6232 GB
Notification: Performance of NFConvertDAE.convert: time 0.02446/0.6296, allocations: 17.55 MB / 0.8571 GB, free: 15.55 MB / 0.6544 GB
Notification: Performance of FrontEnd - DAE generated: time 4.759e-06/0.6296, allocations: 0 / 0.8571 GB, free: 15.55 MB / 0.6544 GB
Notification: Performance of FrontEnd: time 1.213e-06/0.6296, allocations: 0 / 0.8571 GB, free: 15.55 MB / 0.6544 GB
Notification: Performance of Transformations before backend: time 0.0004967/0.6301, allocations: 0 / 0.8571 GB, free: 15.55 MB / 0.6544 GB
Notification: Model statistics after passing the front-end and creating the data structures used by the back-end:
 * Number of equations: 2219
 * Number of variables: 2219
Notification: Performance of Generate backend data structure: time 0.0275/0.6576, allocations: 11.29 MB / 0.8681 GB, free: 4.137 MB / 0.6544 GB
Notification: Performance of prepare preOptimizeDAE: time 3.936e-05/0.6577, allocations: 8.031 kB / 0.8681 GB, free: 4.129 MB / 0.6544 GB
Notification: Performance of preOpt normalInlineFunction (simulation): time 0.005098/0.6628, allocations: 1.36 MB / 0.8694 GB, free: 2.762 MB / 0.6544 GB
Notification: Performance of preOpt evaluateParameters (simulation): time 0.01611/0.6789, allocations: 7.898 MB / 0.8771 GB, free: 10.78 MB / 0.67 GB
Notification: Performance of preOpt simplifyIfEquations (simulation): time 0.0005176/0.6795, allocations: 451.9 kB / 0.8776 GB, free: 10.34 MB / 0.67 GB
Notification: Performance of preOpt expandDerOperator (simulation): time 0.002183/0.6817, allocations: 0.5741 MB / 0.8781 GB, free: 9.762 MB / 0.67 GB
Notification: Performance of preOpt clockPartitioning (simulation): time 0.02331/0.705, allocations: 11.74 MB / 0.8896 GB, free: 12.27 MB / 0.6857 GB
Notification: Performance of preOpt findStateOrder (simulation): time 0.0002637/0.7053, allocations: 75.25 kB / 0.8897 GB, free: 12.2 MB / 0.6857 GB
Notification: Performance of preOpt replaceEdgeChange (simulation): time 0.001749/0.7071, allocations: 300 kB / 0.89 GB, free: 11.91 MB / 0.6857 GB
Notification: Performance of preOpt inlineArrayEqn (simulation): time 0.0006301/0.7077, allocations: 484.6 kB / 0.8904 GB, free: 11.43 MB / 0.6857 GB
Notification: Performance of preOpt removeEqualRHS (simulation): time 0.01918/0.7269, allocations: 8.617 MB / 0.8988 GB, free: 2.789 MB / 0.6857 GB
Warning: The model contains alias variables with redundant start and/or conflicting nominal values. It is recommended to resolve the conflicts, because otherwise the system could be hard to solve. To print the conflicting alias sets and the chosen candidates please use -d=aliasConflicts.
Notification: Performance of preOpt removeSimpleEquations (simulation): time 0.4208/1.148, allocations: 65.51 MB / 0.9628 GB, free: 203 MB / 0.7482 GB
Notification: Performance of preOpt comSubExp (simulation): time 0.01426/1.162, allocations: 6.868 MB / 0.9695 GB, free: 202.2 MB / 0.7482 GB
Notification: Performance of preOpt resolveLoops (simulation): time 0.00751/1.17, allocations: 3.987 MB / 0.9734 GB, free: 200.3 MB / 0.7482 GB
Notification: Performance of preOpt evalFunc (simulation): time 0.001858/1.171, allocations: 0.5344 MB / 0.9739 GB, free: 200.1 MB / 0.7482 GB
Notification: Performance of preOpt encapsulateWhenConditions (simulation): time 9.219e-05/1.172, allocations: 124.9 kB / 0.9741 GB, free: 200 MB / 0.7482 GB
Notification: Performance of pre-optimization done (n=1085): time 9.698e-06/1.172, allocations: 0 / 0.9741 GB, free: 200 MB / 0.7482 GB
Notification: Performance of matching and sorting (n=1086): time 0.09/1.262, allocations: 56.77 MB / 1.029 GB, free: 159.8 MB / 0.7482 GB
Notification: Performance of inlineWhenForInitialization (initialization): time 0.0001858/1.262, allocations: 1.023 MB / 1.03 GB, free: 158.6 MB / 0.7482 GB
Notification: Performance of selectInitializationVariablesDAE (initialization): time 0.01029/1.272, allocations: 7.208 MB / 1.038 GB, free: 151.5 MB / 0.7482 GB
Notification: Performance of collectPreVariables (initialization): time 0.001491/1.274, allocations: 109.7 kB / 1.038 GB, free: 151.4 MB / 0.7482 GB
Notification: Performance of collectInitialEqns (initialization): time 0.002442/1.276, allocations: 3.93 MB / 1.041 GB, free: 147.8 MB / 0.7482 GB
Notification: Performance of collectInitialBindings (initialization): time 0.003707/1.28, allocations: 3.719 MB / 1.045 GB, free: 144.6 MB / 0.7482 GB
Notification: Performance of simplifyInitialFunctions (initialization): time 0.003579/1.283, allocations: 1.999 MB / 1.047 GB, free: 142.6 MB / 0.7482 GB
Notification: Performance of setup shared object (initialization): time 4.963e-05/1.284, allocations: 301.1 kB / 1.047 GB, free: 142.3 MB / 0.7482 GB
Notification: Performance of preBalanceInitialSystem (initialization): time 0.006456/1.29, allocations: 3.612 MB / 1.051 GB, free: 138.7 MB / 0.7482 GB
Notification: Performance of partitionIndependentBlocks (initialization): time 0.009026/1.299, allocations: 6.951 MB / 1.058 GB, free: 130.3 MB / 0.7482 GB
Notification: Performance of analyzeInitialSystem (initialization): time 0.01805/1.317, allocations: 11.7 MB / 1.069 GB, free: 117.3 MB / 0.7482 GB
Notification: Performance of solveInitialSystemEqSystem (initialization): time 0.0001361/1.317, allocations: 32 kB / 1.069 GB, free: 117.3 MB / 0.7482 GB
Notification: Performance of matching and sorting (n=1577) (initialization): time 0.03275/1.35, allocations: 12.89 MB / 1.082 GB, free: 104.4 MB / 0.7482 GB
Notification: Performance of prepare postOptimizeDAE: time 0.0001496/1.35, allocations: 48 kB / 1.082 GB, free: 104.4 MB / 0.7482 GB
Notification: Performance of postOpt simplifyComplexFunction (initialization): time 0.0008792/1.351, allocations: 351.7 kB / 1.082 GB, free: 104 MB / 0.7482 GB
Notification: Performance of postOpt tearingSystem (initialization): time 0.08617/1.437, allocations: 8.783 MB / 1.091 GB, free: 95.23 MB / 0.7482 GB
Notification: Performance of postOpt solveSimpleEquations (initialization): time 0.006581/1.444, allocations: 1.626 MB / 1.092 GB, free: 93.61 MB / 0.7482 GB
Notification: Performance of postOpt calculateStrongComponentJacobians (initialization): time 0.01075/1.455, allocations: 10.42 MB / 1.102 GB, free: 82.77 MB / 0.7482 GB
Notification: Performance of postOpt simplifyAllExpressions (initialization): time 0.00789/1.463, allocations: 468.6 kB / 1.103 GB, free: 82.33 MB / 0.7482 GB
Notification: Performance of postOpt collapseArrayExpressions (initialization): time 0.001858/1.465, allocations: 475.8 kB / 1.103 GB, free: 81.87 MB / 0.7482 GB
Notification: Performance of preBalanceInitialSystem (initialization_lambda0): time 0.01194/1.477, allocations: 5.525 MB / 1.109 GB, free: 76.33 MB / 0.7482 GB
Notification: Performance of partitionIndependentBlocks (initialization_lambda0): time 0.008555/1.485, allocations: 6.873 MB / 1.115 GB, free: 67.98 MB / 0.7482 GB
Notification: Performance of analyzeInitialSystem (initialization_lambda0): time 0.01571/1.501, allocations: 11.55 MB / 1.127 GB, free: 54.96 MB / 0.7482 GB
Notification: Performance of solveInitialSystemEqSystem (initialization_lambda0): time 9.208e-05/1.501, allocations: 32 kB / 1.127 GB, free: 54.93 MB / 0.7482 GB
Notification: Performance of matching and sorting (n=1577) (initialization_lambda0): time 0.02443/1.525, allocations: 12.01 MB / 1.138 GB, free: 42.9 MB / 0.7482 GB
Notification: Performance of prepare postOptimizeDAE: time 8.529e-05/1.526, allocations: 55.94 kB / 1.139 GB, free: 42.84 MB / 0.7482 GB
Notification: Performance of postOpt simplifyComplexFunction (initialization): time 0.0006842/1.526, allocations: 351.7 kB / 1.139 GB, free: 42.5 MB / 0.7482 GB
Notification: Performance of postOpt tearingSystem (initialization): time 0.002218/1.529, allocations: 1.085 MB / 1.14 GB, free: 41.4 MB / 0.7482 GB
Notification: Performance of postOpt solveSimpleEquations (initialization): time 0.006264/1.535, allocations: 1.692 MB / 1.142 GB, free: 39.71 MB / 0.7482 GB
Notification: Performance of postOpt calculateStrongComponentJacobians (initialization): time 0.007808/1.543, allocations: 8.563 MB / 1.15 GB, free: 30.69 MB / 0.7482 GB
Notification: Performance of postOpt simplifyAllExpressions (initialization): time 0.007852/1.551, allocations: 450.2 kB / 1.15 GB, free: 30.27 MB / 0.7482 GB
Notification: Performance of postOpt collapseArrayExpressions (initialization): time 0.001836/1.552, allocations: 467.8 kB / 1.151 GB, free: 29.81 MB / 0.7482 GB
Notification: Model statistics after passing the back-end for initialization:
 * Number of independent subsystems: 475
 * Number of states: 0 ()
 * Number of discrete variables: 2 (valve1.pressureLoss.normIsValid,valve.pressureLoss.normIsValid)
 * Number of discrete states: 0 ()
 * Number of clocked states: 0 ()
 * Top-level inputs: 0
Notification: Strong component statistics for initialization (895):
 * Single equations (assignments): 803
 * Array equations: 0
 * Algorithm blocks: 0
 * Record equations: 84
 * When equations: 0
 * If-equations: 0
 * Equation systems (not torn): 1
 * Torn equation systems: 7
 * Mixed (continuous/discrete) equation systems: 0
Notification: Equation system details (not torn):
 * Constant Jacobian (size): 0 systems
 * Linear Jacobian (size,density): 0 systems
 * Non-linear Jacobian (size): 1 system
   {1}
 * Without analytic Jacobian (size): 0 systems
Notification: Torn system details for strict tearing set:
 * Linear torn systems (#iteration vars, #inner vars, density): 2 systems
   {(4,3,87.5%), (1,6,100.0%)}
 * Non-linear torn systems (#iteration vars, #inner vars): 5 systems
   {(3,39), (3,17), (1,3), (1,3), (1,3)}
Notification: Performance of prepare postOptimizeDAE: time 0.003617/1.556, allocations: 0.7046 MB / 1.151 GB, free: 29.16 MB / 0.7482 GB
Notification: Performance of postOpt lateInlineFunction (simulation): time 0.003706/1.56, allocations: 0.9504 MB / 1.152 GB, free: 28.21 MB / 0.7482 GB
Notification: Performance of postOpt wrapFunctionCalls (simulation): time 0.02482/1.585, allocations: 10.39 MB / 1.163 GB, free: 17.79 MB / 0.7482 GB
Notification: Performance of postOpt simplifysemiLinear (simulation): time 0.000122/1.585, allocations: 35.89 kB / 1.163 GB, free: 17.75 MB / 0.7482 GB
Notification: Performance of postOpt simplifyComplexFunction (simulation): time 0.0006094/1.585, allocations: 259.7 kB / 1.163 GB, free: 17.5 MB / 0.7482 GB
Notification: Performance of postOpt removeConstants (simulation): time 0.00586/1.591, allocations: 2.365 MB / 1.165 GB, free: 15.13 MB / 0.7482 GB
Notification: Performance of postOpt simplifyTimeIndepFuncCalls (simulation): time 0.002942/1.594, allocations: 108 kB / 1.165 GB, free: 15.03 MB / 0.7482 GB
Notification: Performance of postOpt simplifyAllExpressions (simulation): time 0.006744/1.601, allocations: 215.8 kB / 1.165 GB, free: 14.82 MB / 0.7482 GB
Notification: Performance of postOpt findZeroCrossings (simulation): time 0.001707/1.603, allocations: 431.2 kB / 1.166 GB, free: 14.39 MB / 0.7482 GB
[/var/lib/jenkins1/ws/OpenModelicaLibraryTestingWork/OpenModelica/OMCompiler/Compiler/BackEnd/DAEMode.mo:528:7-530:90:writable] Error: Internal error DAEMode.traverserStrongComponents failed on equation:
1/1 (9): (valve1.fluidOut.q, valve1.fluidOut.cp, valve1.fluidOut.cv, valve1.fluidOut.beta, valve1.fluidOut.kappa, valve1.fluidOut.drhodp_hxi, valve1.fluidOut.drhodh_pxi, _, valve1.fluidOut.w, valve1.fluidOut.gamma) = TILMedia.Internals.VLEFluidObjectFunctions.additionalProperties_phxi(massFlowSource_XRG5.p, valve1.summary.outlet.h, {}, valve1.fluidOut.vleFluidPointer)

Variables:
1: valve1.fluidOut.beta:VARIABLE(unit = "1/K" protected = true )  "Isobaric thermal expansion coefficient" type: Real
2: valve1.fluidOut.kappa:VARIABLE(unit = "1/Pa" protected = true )  "Isothermal compressibility" type: Real
3: valve1.fluidOut.drhodp_hxi:VARIABLE(unit = "s2/m2" protected = true )  "1st derivative of density wrt pressure at specific enthalpy and mass fraction" type: Real
4: valve1.fluidOut.w:VARIABLE(unit = "m/s" protected = true )  "Speed of sound" type: Real
5: valve1.fluidOut.gamma:VARIABLE(protected = true )  "Heat capacity ratio aka isentropic expansion factor" type: Real
6: valve1.fluidOut.cv:VARIABLE(unit = "J/(kg.K)" protected = true )  "Specific isochoric heat capacity cv" type: Real
7: valve1.fluidOut.drhodh_pxi:VARIABLE(unit = "kg.s2/m5" protected = true )  "1st derivative of density wrt specific enthalpy at constant pressure and mass fraction" type: Real
8: valve1.fluidOut.cp:VARIABLE(unit = "J/(kg.K)" protected = true )  "Specific isobaric heat capacity cp" type: Real
9: valve1.fluidOut.q:VARIABLE(min = 0.0 max = 1.0 unit = "1" protected = true )  "Steam mass fraction (quality)" type: Real
[/var/lib/jenkins1/ws/OpenModelicaLibraryTestingWork/OpenModelica/OMCompiler/Compiler/BackEnd/DAEMode.mo:528:7-530:90:writable] Error: Internal error DAEMode.traverserStrongComponents failed on equation:
1/1 (1): valve1.pressureLoss.Delta_p_ = min(abs(valve1.pressureLoss.Delta_p) / valve1.pressureLoss.p_in, valve1.pressureLoss.x_TChoked)
2/2 (1): $cse54 = max(0.6666666666666666, 1.0 - valve1.pressureLoss.Delta_p_ / (3.0 * valve1.pressureLoss.x_TChoked))
3/3 (1): valve1.pressureLoss.Y = min(1.0, $cse54)
4/4 (1): quadruple1.m_flow = 2.777777777777778e-5 * valve1.pressureLoss.Kv * valve1.pressureLoss.F_P * valve1.pressureLoss.Y * $cse52 * sqrt(max(1e-15, valve1.iCom.rho_in))
5/5 (1): valve1.iCom.rho_in = if noEvent(valve1.summary.outline.opening_ < 0.0) then valve1.fluidIn.d else ClaRa.Basics.Functions.Stepsmoother(10.0, -10.0, valve1.pressureLoss.Delta_p) * valve1.fluidIn.d + ClaRa.Basics.Functions.Stepsmoother(-10.0, 10.0, valve1.pressureLoss.Delta_p) * valve1.fluidOut.d
6/6 (1): valve1.fluidOut.d = TILMedia.Internals.VLEFluidConfigurations.FullyMixtureCompatible.VLEFluidObjectFunctions.density_phxi(massFlowSource_XRG5.p, valve1.summary.outlet.h, {}, valve1.fluidOut.vleFluidPointer)
7/7 (1): $cse73 = ClaRa.Basics.Functions.Stepsmoother(valve1.fluidOut.VLE.h_v + 1000.0, valve1.fluidOut.VLE.h_v, valve1.summary.outlet.h)
8/8 (1): valve1.iCom.gamma_out = ($cse73 * valve1.fluidOut.cp + $cse74 * TILMedia.Internals.VLEFluidConfigurations.FullyMixtureCompatible.VLEFluidObjectFunctions.specificIsobaricHeatCapacity_phxi(massFlowSource_XRG5.p, valve1.fluidOut.VLE.h_v, {}, valve1.fluidOut.vleFluidPointer)) / ($cse73 * valve1.fluidOut.cv + $cse74 * TILMedia.Internals.VLEFluidConfigurations.FullyMixtureCompatible.VLEFluidObjectFunctions.specificIsochoricHeatCapacity_phxi(massFlowSource_XRG5.p, valve1.fluidOut.VLE.h_v, {}, valve1.fluidOut.vleFluidPointer))
9/9 (1): valve1.pressureLoss.gamma = if valve1.summary.outline.opening_ < 0.0 then valve1.iCom.gamma_in else ClaRa.Basics.Functions.Stepsmoother(1000.0, -1000.0, valve1.pressureLoss.Delta_p) * valve1.iCom.gamma_in + ClaRa.Basics.Functions.Stepsmoother(-1000.0, 1000.0, valve1.pressureLoss.Delta_p) * valve1.iCom.gamma_out
10/10 (1): valve1.pressureLoss.F_gamma = 0.7142857142857143 * valve1.pressureLoss.gamma
11/11 (1): valve1.pressureLoss.x_TChoked = valve1.pressureLoss.F_gamma * valve1.pressureLoss.x_TP
12/12 (1): $cse53 = min(abs(valve1.pressureLoss.Delta_p), abs(valve1.pressureLoss.x_TChoked * valve1.pressureLoss.p_in))
13/13 (1): valve1.pressureLoss.Delta_p_actual = /*Real*/(sign(valve1.pressureLoss.Delta_p)) * $cse53
14/14 (1): $cse52 = ClaRa.Basics.Functions.ThermoRoot(valve1.pressureLoss.Delta_p_actual, valve1.pressureLoss.Delta_p_eps)
15/15 (1): $cse74 = ClaRa.Basics.Functions.Stepsmoother(valve1.fluidOut.VLE.h_v, valve1.fluidOut.VLE.h_v + 1000.0, valve1.summary.outlet.h)
16/16 (1): valve1.summary.outlet.h = if noEvent(valve1.summary.outline.opening_ < 0.0) then valve1.outlet.h_outflow else ClaRa.Basics.Functions.Stepsmoother(10.0, -10.0, valve1.pressureLoss.Delta_p) * valve1.outlet.h_outflow + ClaRa.Basics.Functions.Stepsmoother(-10.0, 10.0, valve1.pressureLoss.Delta_p) * massFlowSource_XRG5.h
17/17 (1): valve1.summary.inlet.h = if noEvent(valve1.summary.outline.opening_ < 0.0) then valve1.outlet.h_outflow else ClaRa.Basics.Functions.Stepsmoother(10.0, -10.0, valve1.pressureLoss.Delta_p) * valve1.outlet.h_outflow + ClaRa.Basics.Functions.Stepsmoother(-10.0, 10.0, valve1.pressureLoss.Delta_p) * massFlowSource_XRG5.h
18/18 (1): $cse71 = ClaRa.Basics.Functions.Stepsmoother(valve1.fluidIn.VLE.h_v + 1000.0, valve1.fluidIn.VLE.h_v, valve1.summary.inlet.h)
19/19 (1): valve1.iCom.gamma_in = ($cse71 * valve1.fluidIn.cp + $cse72 * TILMedia.Internals.VLEFluidConfigurations.FullyMixtureCompatible.VLEFluidObjectFunctions.specificIsobaricHeatCapacity_phxi(injector1.mixingZone.p_vap, valve1.fluidIn.VLE.h_v, {}, valve1.fluidIn.vleFluidPointer)) / ($cse71 * valve1.fluidIn.cv + $cse72 * TILMedia.Internals.VLEFluidConfigurations.FullyMixtureCompatible.VLEFluidObjectFunctions.specificIsochoricHeatCapacity_phxi(injector1.mixingZone.p_vap, valve1.fluidIn.VLE.h_v, {}, valve1.fluidIn.vleFluidPointer))
20/20 (1): $cse72 = ClaRa.Basics.Functions.Stepsmoother(valve1.fluidIn.VLE.h_v, valve1.fluidIn.VLE.h_v + 1000.0, valve1.summary.inlet.h)
21/21 (9): (valve1.fluidIn.q, valve1.fluidIn.cp, valve1.fluidIn.cv, valve1.fluidIn.beta, valve1.fluidIn.kappa, valve1.fluidIn.drhodp_hxi, valve1.fluidIn.drhodh_pxi, _, valve1.fluidIn.w, valve1.fluidIn.gamma) = TILMedia.Internals.VLEFluidObjectFunctions.additionalProperties_phxi(injector1.mixingZone.p_vap, valve1.summary.inlet.h, {}, valve1.fluidIn.vleFluidPointer)
22/30 (1): valve1.fluidIn.d = TILMedia.Internals.VLEFluidConfigurations.FullyMixtureCompatible.VLEFluidObjectFunctions.density_phxi(injector1.mixingZone.p_vap, valve1.summary.inlet.h, {}, valve1.fluidIn.vleFluidPointer)
23/31 (1): injector1.mixingZone.fluidOut[1].h = if noEvent((-quadruple1.m_flow) > 0.0) then massFlowSource_XRG5.h else valve1.outlet.h_outflow
24/32 (1): injector1.mixingZone.phaseBorder.steamQuality_out[1] = TILMedia.Internals.VLEFluidConfigurations.FullyMixtureCompatible.VLEFluidObjectFunctions.steamMassFraction_phxi(injector1.mixingZone.p_vap, injector1.mixingZone.fluidOut[1].h, {}, injector1.mixingZone.iCom.fluidPointer_out[1])
25/33 (1): injector1.mixingZone.phaseBorder.zoneAlloc_out[1] = 1.0 + $cse21 * $cse22 + $cse23 * injector1.mixingZone.phaseBorder.steamQuality_out[1]
26/34 (1): $cse23 = ClaRa.Basics.Functions.Stepsmoother(0.001, 0.0, -quadruple1.m_flow)
27/35 (1): $cse21 = ClaRa.Basics.Functions.Stepsmoother(0.0, 0.001, -quadruple1.m_flow)
28/36 (1): valve1.outlet.h_outflow = (-1.0 + injector1.mixingZone.phaseBorder.zoneAlloc_out[1]) * injector1.mixingZone.h_vap + (2.0 - injector1.mixingZone.phaseBorder.zoneAlloc_out[1]) * injector1.mixingZone.h_liq
29/37 (9): (valve1.fluidOut.q, valve1.fluidOut.cp, valve1.fluidOut.cv, valve1.fluidOut.beta, valve1.fluidOut.kappa, valve1.fluidOut.drhodp_hxi, valve1.fluidOut.drhodh_pxi, _, valve1.fluidOut.w, valve1.fluidOut.gamma) = TILMedia.Internals.VLEFluidObjectFunctions.additionalProperties_phxi(massFlowSource_XRG5.p, valve1.summary.outlet.h, {}, valve1.fluidOut.vleFluidPointer)

Variables:
1: valve1.fluidOut.beta:VARIABLE(unit = "1/K" protected = true )  "Isobaric thermal expansion coefficient" type: Real
2: valve1.fluidOut.kappa:VARIABLE(unit = "1/Pa" protected = true )  "Isothermal compressibility" type: Real
3: valve1.fluidOut.drhodp_hxi:VARIABLE(unit = "s2/m2" protected = true )  "1st derivative of density wrt pressure at specific enthalpy and mass fraction" type: Real
4: valve1.fluidOut.w:VARIABLE(unit = "m/s" protected = true )  "Speed of sound" type: Real
5: valve1.fluidOut.gamma:VARIABLE(protected = true )  "Heat capacity ratio aka isentropic expansion factor" type: Real
6: valve1.fluidOut.cv:VARIABLE(unit = "J/(kg.K)" protected = true )  "Specific isochoric heat capacity cv" type: Real
7: valve1.fluidOut.drhodh_pxi:VARIABLE(unit = "kg.s2/m5" protected = true )  "1st derivative of density wrt specific enthalpy at constant pressure and mass fraction" type: Real
8: valve1.fluidOut.cp:VARIABLE(unit = "J/(kg.K)" protected = true )  "Specific isobaric heat capacity cp" type: Real
9: valve1.fluidOut.q:VARIABLE(min = 0.0 max = 1.0 unit = "1" protected = true )  "Steam mass fraction (quality)" type: Real
10: injector1.mixingZone.phaseBorder.zoneAlloc_out[1]:VARIABLE(min = 0.0 unit = "kg/kg" nominal = 1.0 )  "Allocation of outlet mass flows to zones |1:liq|2:vap|" type: Real [1]
11: $cse21:VARIABLE(protected = true )  type: Real unreplaceable
12: quadruple1.m_flow:VARIABLE(nominal = 1.0 )  "Mass flow rate" type: Real
13: $cse23:VARIABLE(protected = true )  type: Real unreplaceable
14: injector1.mixingZone.phaseBorder.steamQuality_out[1]:VARIABLE(min = 0.0 unit = "kg/kg" nominal = 1.0 )  "Outlet steam quality" type: Real [1]
15: injector1.mixingZone.fluidOut[1].h:VARIABLE(unit = "J/kg" nominal = 1000.0 final = true )  "Specific enthalpy" type: Real [1]
16: valve1.fluidIn.d:VARIABLE(min = 0.0 unit = "kg/m3" protected = true )  "Density" type: Real
17: valve1.fluidIn.drhodp_hxi:VARIABLE(unit = "s2/m2" protected = true )  "1st derivative of density wrt pressure at specific enthalpy and mass fraction" type: Real
18: valve1.fluidIn.gamma:VARIABLE(protected = true )  "Heat capacity ratio aka isentropic expansion factor" type: Real
19: valve1.fluidIn.cp:VARIABLE(unit = "J/(kg.K)" protected = true )  "Specific isobaric heat capacity cp" type: Real
20: valve1.fluidIn.cv:VARIABLE(unit = "J/(kg.K)" protected = true )  "Specific isochoric heat capacity cv" type: Real
21: valve1.fluidIn.beta:VARIABLE(unit = "1/K" protected = true )  "Isobaric thermal expansion coefficient" type: Real
22: valve1.fluidIn.q:VARIABLE(min = 0.0 max = 1.0 unit = "1" protected = true )  "Steam mass fraction (quality)" type: Real
23: valve1.fluidIn.kappa:VARIABLE(unit = "1/Pa" protected = true )  "Isothermal compressibility" type: Real
24: valve1.fluidIn.w:VARIABLE(unit = "m/s" protected = true )  "Speed of sound" type: Real
25: valve1.fluidIn.drhodh_pxi:VARIABLE(unit = "kg.s2/m5" protected = true )  "1st derivative of density wrt specific enthalpy at constant pressure and mass fraction" type: Real
26: $cse72:VARIABLE(protected = true )  type: Real unreplaceable
27: valve1.iCom.gamma_in:VARIABLE(start = 2.0 protected = true )  "Heat capacity ratio at inlet" type: Real
28: $cse71:VARIABLE(protected = true )  type: Real unreplaceable
29: valve1.summary.inlet.h:VARIABLE(unit = "J/kg" nominal = 1000.0 )  "Specific enthalpy" type: Real
30: valve1.outlet.h_outflow:VARIABLE(unit = "J/kg" )  "Specific thermodynamic enthalpy close to the connection point if m_flow < 0" type: Real
31: $cse74:VARIABLE(protected = true )  type: Real unreplaceable
32: $cse52:VARIABLE(protected = true )  type: Real unreplaceable
33: valve1.pressureLoss.Delta_p_actual:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 protected = true )  "Actual pressure difference with respect to choking flow" type: Real
34: $cse53:VARIABLE(protected = true )  type: Real unreplaceable
35: valve1.pressureLoss.x_TChoked:VARIABLE(protected = true )  "Pressure ratio at which choking of flow occurs" type: Real
36: valve1.pressureLoss.F_gamma:VARIABLE(protected = true )  "Normalising factor for heat capacity ratio" type: Real
37: valve1.pressureLoss.gamma:VARIABLE()  "Heat capacity ratio at actual inlet" type: Real
38: valve1.iCom.gamma_out:VARIABLE(start = 2.0 protected = true )  "Heat capacity ratio at outlet" type: Real
39: $cse73:VARIABLE(protected = true )  type: Real unreplaceable
40: valve1.summary.outlet.h:VARIABLE(unit = "J/kg" nominal = 1000.0 )  "Specific enthalpy" type: Real
41: valve1.fluidOut.d:VARIABLE(min = 0.0 unit = "kg/m3" protected = true )  "Density" type: Real
42: valve1.iCom.rho_in:VARIABLE(min = 0.0 start = 1.0 unit = "kg/m3" nominal = 1000.0 protected = true )  "Inlet density" type: Real
43: valve1.pressureLoss.Y:VARIABLE()  "Expansion factor" type: Real
44: $cse54:VARIABLE(protected = true )  type: Real unreplaceable
45: valve1.pressureLoss.Delta_p_:VARIABLE(protected = true )  "(p_inlet-p_outlet)/p_inlet; naming in DIN EN 60534: x" type: Real
[/var/lib/jenkins1/ws/OpenModelicaLibraryTestingWork/OpenModelica/OMCompiler/Compiler/BackEnd/BackendDAEUtil.mo:9805:5-9806:77:writable] Error: Internal error BackendDAEUtil.traverseEqSystemStrongComponents failed with function:
omc_DAEMode_traverserStrongComponents
Notification: Performance of <failed> postOpt createDAEmodeBDAE (simulation): time 0.003271/1.606, allocations: 2.235 MB / 1.168 GB, free: 11.68 MB / 0.7482 GB
Error: post-optimization module createDAEmodeBDAE (simulation) failed.
Error: Internal error SimCode DAEmode: The model ClaRa.Components.VolumesValvesFittings.Fittings.Check.Test_SprayInjector could not be translated