Running: ./testmodel.py --libraries=/home/hudson/saved_omc/libraries/.openmodelica/libraries --ompython_omhome=/usr ThermofluidStream_ThermofluidStream.Idealized.Examples.TUMExercisesThermodynamicCycles.Exercise4DieselEngine.AdiabaticPerfectGas.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 0.000851/0.000851, allocations: 100.4 kB / 19.7 MB, free: 452 kB / 13.93 MB " [Timeout remaining time 180] loadFile("/home/hudson/saved_omc/libraries/.openmodelica/libraries/Complex 4.1.0+maint.om/package.mo", uses=false) [Timeout 180] "Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/Complex 4.1.0+maint.om/package.mo): time 0.0009222/0.0009222, allocations: 213 kB / 23 MB, free: 2.98 MB / 13.93 MB " [Timeout remaining time 180] loadFile("/home/hudson/saved_omc/libraries/.openmodelica/libraries/Modelica 4.1.0+maint.om/package.mo", uses=false) [Timeout 180] "Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/Modelica 4.1.0+maint.om/package.mo): time 0.9597/0.9597, allocations: 230.6 MB / 256.8 MB, free: 9.625 MB / 202.7 MB " [Timeout remaining time 179] loadFile("/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermofluidStream 1.4.0/package.mo", uses=false) [Timeout 180] "Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermofluidStream 1.4.0/package.mo): time 0.7247/0.7247, allocations: 154.1 MB / 467.3 MB, free: 3.309 MB / 362.7 MB " [Timeout remaining time 179] Using package ThermofluidStream with version 1.4.0 (/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermofluidStream 1.4.0/package.mo) Using package Modelica with version 4.1.0 (/home/hudson/saved_omc/libraries/.openmodelica/libraries/Modelica 4.1.0+maint.om/package.mo) Using package Complex with version 4.1.0 (/home/hudson/saved_omc/libraries/.openmodelica/libraries/Complex 4.1.0+maint.om/package.mo) Using package ModelicaServices with version 4.1.0 (/home/hudson/saved_omc/libraries/.openmodelica/libraries/ModelicaServices 4.1.0+maint.om/package.mo) Running command: translateModel(ThermofluidStream.Idealized.Examples.TUMExercisesThermodynamicCycles.Exercise4DieselEngine.AdiabaticPerfectGas,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|T1|T3|Time|_derdummy|_dummy|combustion.L|combustion.P|combustion.Q_flow|combustion.T_out_fixed|combustion.assertionLevel|combustion.clip_p_out|combustion.dT|combustion.dT_fixed|combustion.dh|combustion.dh_fixed|combustion.dp|combustion.dr_corr|combustion.du|combustion.h_in|combustion.h_out|combustion.h_out_fixed|combustion.initM_flow|der.combustion.inlet.m_flow.|combustion.inlet.m_flow|combustion.inlet.r|combustion.inlet.state.T|combustion.inlet.state.p|combustion.m_acceleration_0|combustion.m_flow|combustion.m_flowStateSelect|combustion.m_flow_0|combustion.outlet.m_flow|combustion.outlet.r|combustion.outlet.state.T|combustion.outlet.state.p|combustion.outletSpec|combustion.outletSpec_actual|combustion.outletValueSpec|combustion.p|combustion.p_in|combustion.p_inf|combustion.p_min|combustion.p_out|combustion.q|combustion.rho_in|combustion.rho_out|combustion.singularityRegime|combustion.systemSpec|combustion.u_in|combustion.u_out|combustion.v_in|combustion.v_out|combustion.w_amb|combustion.w_exp|combustion.w_exp_net|compression.L|compression.P|compression.P_nom|compression.P_out|compression.TC|compression.adiabaticModel.T_out|compression.adiabaticModel.T_out_is|compression.adiabaticModel.Z_in|compression.adiabaticModel.Z_out|compression.adiabaticModel.assertionLevel|compression.adiabaticModel.cp|compression.adiabaticModel.cpSpec|compression.adiabaticModel.cp_fixed|compression.adiabaticModel.cp_in|compression.adiabaticModel.cp_out|compression.adiabaticModel.delta_cp_rel|compression.adiabaticModel.delta_gamma_rel|compression.adiabaticModel.eta_is|compression.adiabaticModel.gamma|compression.adiabaticModel.gammaSpec|compression.adiabaticModel.gamma_fixed|compression.adiabaticModel.gamma_in|compression.adiabaticModel.gamma_out|compression.adiabaticModel.h_out|compression.adiabaticModel.isCpWithinTol|compression.adiabaticModel.isGammaWithinTol|compression.adiabaticModel.isInletIdealGas|compression.adiabaticModel.isOutletIdealGas|compression.adiabaticModel.p_out|compression.adiabaticModel.relTolCp|compression.adiabaticModel.relTolGamma|compression.adiabaticModel.relTolZ|compression.adiabaticModel.state_in.T|compression.adiabaticModel.state_in.p|compression.adiabaticModel.state_out.T|compression.adiabaticModel.state_out.p|compression.adiabaticModel.w_t|compression.adiabaticModel.w_t_is|compression.assertionLevel|compression.clip_p_out|compression.dh|compression.dp|compression.dp_fixed|compression.dp_nom|compression.dp_start|compression.dr_corr|compression.etaSpec|compression.eta_actual|compression.eta_fixed|compression.eta_is|compression.h_in|compression.h_out|compression.initM_flow|der.compression.inlet.m_flow.|compression.inlet.m_flow|compression.inlet.r|compression.inlet.state.T|compression.inlet.state.p|compression.m_acceleration_0|compression.m_flow|compression.m_flowStateSelect|compression.m_flow_0|compression.outlet.m_flow|compression.outlet.r|compression.outlet.state.T|compression.outlet.state.p|compression.outletSpec|compression.outletSpec_actual|compression.outletValueSpec|compression.pRatio|compression.pRatio_fixed|compression.p_in|compression.p_min|compression.p_out|compression.p_out_fixed|compression.singularityRegime|compressionRatio|density1.y|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|efficiency.displayVariablefinal|efficiency.showNumber|efficiency.significantDigits|exhaustTemperature.displayVariablefinal|exhaustTemperature.showNumber|exhaustTemperature.significantDigits|expansion.L|expansion.P|expansion.P_nom|expansion.P_out|expansion.TC|expansion.adiabaticModel.T_out|expansion.adiabaticModel.T_out_is|expansion.adiabaticModel.Z_in|expansion.adiabaticModel.Z_out|expansion.adiabaticModel.assertionLevel|expansion.adiabaticModel.cp|expansion.adiabaticModel.cpSpec|expansion.adiabaticModel.cp_fixed|expansion.adiabaticModel.cp_in|expansion.adiabaticModel.cp_out|expansion.adiabaticModel.delta_cp_rel|expansion.adiabaticModel.delta_gamma_rel|expansion.adiabaticModel.eta_is|expansion.adiabaticModel.gamma|expansion.adiabaticModel.gammaSpec|expansion.adiabaticModel.gamma_fixed|expansion.adiabaticModel.gamma_in|expansion.adiabaticModel.gamma_out|expansion.adiabaticModel.h_out|expansion.adiabaticModel.isCpWithinTol|expansion.adiabaticModel.isGammaWithinTol|expansion.adiabaticModel.isInletIdealGas|expansion.adiabaticModel.isOutletIdealGas|expansion.adiabaticModel.p_out|expansion.adiabaticModel.relTolCp|expansion.adiabaticModel.relTolGamma|expansion.adiabaticModel.relTolZ|expansion.adiabaticModel.state_in.T|expansion.adiabaticModel.state_in.p|expansion.adiabaticModel.state_out.T|expansion.adiabaticModel.state_out.p|expansion.adiabaticModel.w_t|expansion.adiabaticModel.w_t_is|expansion.assertionLevel|expansion.clip_p_out|expansion.dh|expansion.dp|expansion.dp_fixed|expansion.dp_nom|expansion.dp_start|expansion.dr_corr|expansion.etaSpec|expansion.eta_actual|expansion.eta_fixed|expansion.eta_is|expansion.h_in|expansion.h_out|expansion.initM_flow|der.expansion.inlet.m_flow.|expansion.inlet.m_flow|expansion.inlet.r|expansion.inlet.state.T|expansion.inlet.state.p|expansion.m_acceleration_0|expansion.m_flow|expansion.m_flowStateSelect|expansion.m_flow_0|expansion.outlet.m_flow|expansion.outlet.r|expansion.outlet.state.T|expansion.outlet.state.p|expansion.outletSpec|expansion.outletSpec_actual|expansion.outletSpec_prescribed|expansion.outletValueSpec|expansion.pRatio|expansion.pRatio_fixed|expansion.p_in|expansion.p_min|expansion.p_out|expansion.p_out_fixed|expansion.singularityRegime|gamma|gasExchange.L|gasExchange.P|gasExchange.P_out|gasExchange.Q_flow|gasExchange.T_out_fixed|gasExchange.assertionLevel|gasExchange.clip_p_out|gasExchange.dT|gasExchange.dT_fixed|gasExchange.dp|gasExchange.dp_start|gasExchange.dr_corr|gasExchange.du|gasExchange.h_in|gasExchange.h_out|gasExchange.initM_flow|der.gasExchange.inlet.m_flow.|gasExchange.inlet.m_flow|gasExchange.inlet.r|gasExchange.inlet.state.T|gasExchange.inlet.state.p|gasExchange.m_acceleration_0|gasExchange.m_flow|gasExchange.m_flowStateSelect|gasExchange.m_flow_0|gasExchange.outlet.m_flow|gasExchange.outlet.r|gasExchange.outlet.state.T|gasExchange.outlet.state.p|gasExchange.outletSpec|gasExchange.outletSpec_actual|gasExchange.outletValueSpec|gasExchange.p_in|gasExchange.p_min|gasExchange.p_out|gasExchange.rho|gasExchange.singularityRegime|gasExchange.systemSpec|gasExchange.u_in|gasExchange.u_out|gasExchange.w_p|inverseBlockConstraints.u1|inverseBlockConstraints.u2|inverseBlockConstraints.y1|inverseBlockConstraints.y2|loopBreaker.L|loopBreaker.T_out|loopBreaker.T_out_fixed|loopBreaker.XiSpec|loopBreaker.assertionLevel|loopBreaker.dh|loopBreaker.dm_flow|loopBreaker.dp|loopBreaker.h_out|loopBreaker.h_out_fixed|loopBreaker.inlet.m_flow|loopBreaker.inlet.r|loopBreaker.inlet.state.T|loopBreaker.inlet.state.p|loopBreaker.m_flowSpec|loopBreaker.m_flow_in|loopBreaker.m_flow_in_par|der.loopBreaker.outlet.m_flow.|loopBreaker.outlet.m_flow|loopBreaker.outlet.r|loopBreaker.outlet.state.T|loopBreaker.outlet.state.p|loopBreaker.pSpec|loopBreaker.p_out|loopBreaker.p_out_fixed|loopBreaker.thermalSpec|loopBreaker.thermalValueSpec|loopBreaker.tol_Xi|loopBreaker.tol_h|loopBreaker.tol_m_flow|loopBreaker.tol_p|m_flow|maximumPressure.displayVariablefinal|maximumPressure.showNumber|maximumPressure.significantDigits|netWork.displayVariablefinal|netWork.showNumber|netWork.significantDigits|p1|p2|rho1|rho2|sensorDensity1.TC|sensorDensity1.digits|sensorDensity1.direct_value|sensorDensity1.getQuantity.quantity|sensorDensity1.getQuantity.r|sensorDensity1.getQuantity.rho_min|sensorDensity1.getQuantity.state.T|sensorDensity1.getQuantity.state.p|sensorDensity1.getQuantity.value|sensorDensity1.init|sensorDensity1.inlet.m_flow|sensorDensity1.inlet.r|sensorDensity1.inlet.state.T|sensorDensity1.inlet.state.p|sensorDensity1.quantity|sensorDensity1.rho_min|sensorDensity1.value|sensorDensity1.value_0|sensorDensity1.value_out|shaftPower.E_flow_in.1.|shaftPower.E_flow_in.2.|shaftPower.E_flow_in.3.|shaftPower.E_flow_out|v1|v2",fileNamePrefix="ThermofluidStream_ThermofluidStream.Idealized.Examples.TUMExercisesThermodynamicCycles.Exercise4DieselEngine.AdiabaticPerfectGas") translateModel(ThermofluidStream.Idealized.Examples.TUMExercisesThermodynamicCycles.Exercise4DieselEngine.AdiabaticPerfectGas,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|T1|T3|Time|_derdummy|_dummy|combustion.L|combustion.P|combustion.Q_flow|combustion.T_out_fixed|combustion.assertionLevel|combustion.clip_p_out|combustion.dT|combustion.dT_fixed|combustion.dh|combustion.dh_fixed|combustion.dp|combustion.dr_corr|combustion.du|combustion.h_in|combustion.h_out|combustion.h_out_fixed|combustion.initM_flow|der.combustion.inlet.m_flow.|combustion.inlet.m_flow|combustion.inlet.r|combustion.inlet.state.T|combustion.inlet.state.p|combustion.m_acceleration_0|combustion.m_flow|combustion.m_flowStateSelect|combustion.m_flow_0|combustion.outlet.m_flow|combustion.outlet.r|combustion.outlet.state.T|combustion.outlet.state.p|combustion.outletSpec|combustion.outletSpec_actual|combustion.outletValueSpec|combustion.p|combustion.p_in|combustion.p_inf|combustion.p_min|combustion.p_out|combustion.q|combustion.rho_in|combustion.rho_out|combustion.singularityRegime|combustion.systemSpec|combustion.u_in|combustion.u_out|combustion.v_in|combustion.v_out|combustion.w_amb|combustion.w_exp|combustion.w_exp_net|compression.L|compression.P|compression.P_nom|compression.P_out|compression.TC|compression.adiabaticModel.T_out|compression.adiabaticModel.T_out_is|compression.adiabaticModel.Z_in|compression.adiabaticModel.Z_out|compression.adiabaticModel.assertionLevel|compression.adiabaticModel.cp|compression.adiabaticModel.cpSpec|compression.adiabaticModel.cp_fixed|compression.adiabaticModel.cp_in|compression.adiabaticModel.cp_out|compression.adiabaticModel.delta_cp_rel|compression.adiabaticModel.delta_gamma_rel|compression.adiabaticModel.eta_is|compression.adiabaticModel.gamma|compression.adiabaticModel.gammaSpec|compression.adiabaticModel.gamma_fixed|compression.adiabaticModel.gamma_in|compression.adiabaticModel.gamma_out|compression.adiabaticModel.h_out|compression.adiabaticModel.isCpWithinTol|compression.adiabaticModel.isGammaWithinTol|compression.adiabaticModel.isInletIdealGas|compression.adiabaticModel.isOutletIdealGas|compression.adiabaticModel.p_out|compression.adiabaticModel.relTolCp|compression.adiabaticModel.relTolGamma|compression.adiabaticModel.relTolZ|compression.adiabaticModel.state_in.T|compression.adiabaticModel.state_in.p|compression.adiabaticModel.state_out.T|compression.adiabaticModel.state_out.p|compression.adiabaticModel.w_t|compression.adiabaticModel.w_t_is|compression.assertionLevel|compression.clip_p_out|compression.dh|compression.dp|compression.dp_fixed|compression.dp_nom|compression.dp_start|compression.dr_corr|compression.etaSpec|compression.eta_actual|compression.eta_fixed|compression.eta_is|compression.h_in|compression.h_out|compression.initM_flow|der.compression.inlet.m_flow.|compression.inlet.m_flow|compression.inlet.r|compression.inlet.state.T|compression.inlet.state.p|compression.m_acceleration_0|compression.m_flow|compression.m_flowStateSelect|compression.m_flow_0|compression.outlet.m_flow|compression.outlet.r|compression.outlet.state.T|compression.outlet.state.p|compression.outletSpec|compression.outletSpec_actual|compression.outletValueSpec|compression.pRatio|compression.pRatio_fixed|compression.p_in|compression.p_min|compression.p_out|compression.p_out_fixed|compression.singularityRegime|compressionRatio|density1.y|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|efficiency.displayVariablefinal|efficiency.showNumber|efficiency.significantDigits|exhaustTemperature.displayVariablefinal|exhaustTemperature.showNumber|exhaustTemperature.significantDigits|expansion.L|expansion.P|expansion.P_nom|expansion.P_out|expansion.TC|expansion.adiabaticModel.T_out|expansion.adiabaticModel.T_out_is|expansion.adiabaticModel.Z_in|expansion.adiabaticModel.Z_out|expansion.adiabaticModel.assertionLevel|expansion.adiabaticModel.cp|expansion.adiabaticModel.cpSpec|expansion.adiabaticModel.cp_fixed|expansion.adiabaticModel.cp_in|expansion.adiabaticModel.cp_out|expansion.adiabaticModel.delta_cp_rel|expansion.adiabaticModel.delta_gamma_rel|expansion.adiabaticModel.eta_is|expansion.adiabaticModel.gamma|expansion.adiabaticModel.gammaSpec|expansion.adiabaticModel.gamma_fixed|expansion.adiabaticModel.gamma_in|expansion.adiabaticModel.gamma_out|expansion.adiabaticModel.h_out|expansion.adiabaticModel.isCpWithinTol|expansion.adiabaticModel.isGammaWithinTol|expansion.adiabaticModel.isInletIdealGas|expansion.adiabaticModel.isOutletIdealGas|expansion.adiabaticModel.p_out|expansion.adiabaticModel.relTolCp|expansion.adiabaticModel.relTolGamma|expansion.adiabaticModel.relTolZ|expansion.adiabaticModel.state_in.T|expansion.adiabaticModel.state_in.p|expansion.adiabaticModel.state_out.T|expansion.adiabaticModel.state_out.p|expansion.adiabaticModel.w_t|expansion.adiabaticModel.w_t_is|expansion.assertionLevel|expansion.clip_p_out|expansion.dh|expansion.dp|expansion.dp_fixed|expansion.dp_nom|expansion.dp_start|expansion.dr_corr|expansion.etaSpec|expansion.eta_actual|expansion.eta_fixed|expansion.eta_is|expansion.h_in|expansion.h_out|expansion.initM_flow|der.expansion.inlet.m_flow.|expansion.inlet.m_flow|expansion.inlet.r|expansion.inlet.state.T|expansion.inlet.state.p|expansion.m_acceleration_0|expansion.m_flow|expansion.m_flowStateSelect|expansion.m_flow_0|expansion.outlet.m_flow|expansion.outlet.r|expansion.outlet.state.T|expansion.outlet.state.p|expansion.outletSpec|expansion.outletSpec_actual|expansion.outletSpec_prescribed|expansion.outletValueSpec|expansion.pRatio|expansion.pRatio_fixed|expansion.p_in|expansion.p_min|expansion.p_out|expansion.p_out_fixed|expansion.singularityRegime|gamma|gasExchange.L|gasExchange.P|gasExchange.P_out|gasExchange.Q_flow|gasExchange.T_out_fixed|gasExchange.assertionLevel|gasExchange.clip_p_out|gasExchange.dT|gasExchange.dT_fixed|gasExchange.dp|gasExchange.dp_start|gasExchange.dr_corr|gasExchange.du|gasExchange.h_in|gasExchange.h_out|gasExchange.initM_flow|der.gasExchange.inlet.m_flow.|gasExchange.inlet.m_flow|gasExchange.inlet.r|gasExchange.inlet.state.T|gasExchange.inlet.state.p|gasExchange.m_acceleration_0|gasExchange.m_flow|gasExchange.m_flowStateSelect|gasExchange.m_flow_0|gasExchange.outlet.m_flow|gasExchange.outlet.r|gasExchange.outlet.state.T|gasExchange.outlet.state.p|gasExchange.outletSpec|gasExchange.outletSpec_actual|gasExchange.outletValueSpec|gasExchange.p_in|gasExchange.p_min|gasExchange.p_out|gasExchange.rho|gasExchange.singularityRegime|gasExchange.systemSpec|gasExchange.u_in|gasExchange.u_out|gasExchange.w_p|inverseBlockConstraints.u1|inverseBlockConstraints.u2|inverseBlockConstraints.y1|inverseBlockConstraints.y2|loopBreaker.L|loopBreaker.T_out|loopBreaker.T_out_fixed|loopBreaker.XiSpec|loopBreaker.assertionLevel|loopBreaker.dh|loopBreaker.dm_flow|loopBreaker.dp|loopBreaker.h_out|loopBreaker.h_out_fixed|loopBreaker.inlet.m_flow|loopBreaker.inlet.r|loopBreaker.inlet.state.T|loopBreaker.inlet.state.p|loopBreaker.m_flowSpec|loopBreaker.m_flow_in|loopBreaker.m_flow_in_par|der.loopBreaker.outlet.m_flow.|loopBreaker.outlet.m_flow|loopBreaker.outlet.r|loopBreaker.outlet.state.T|loopBreaker.outlet.state.p|loopBreaker.pSpec|loopBreaker.p_out|loopBreaker.p_out_fixed|loopBreaker.thermalSpec|loopBreaker.thermalValueSpec|loopBreaker.tol_Xi|loopBreaker.tol_h|loopBreaker.tol_m_flow|loopBreaker.tol_p|m_flow|maximumPressure.displayVariablefinal|maximumPressure.showNumber|maximumPressure.significantDigits|netWork.displayVariablefinal|netWork.showNumber|netWork.significantDigits|p1|p2|rho1|rho2|sensorDensity1.TC|sensorDensity1.digits|sensorDensity1.direct_value|sensorDensity1.getQuantity.quantity|sensorDensity1.getQuantity.r|sensorDensity1.getQuantity.rho_min|sensorDensity1.getQuantity.state.T|sensorDensity1.getQuantity.state.p|sensorDensity1.getQuantity.value|sensorDensity1.init|sensorDensity1.inlet.m_flow|sensorDensity1.inlet.r|sensorDensity1.inlet.state.T|sensorDensity1.inlet.state.p|sensorDensity1.quantity|sensorDensity1.rho_min|sensorDensity1.value|sensorDensity1.value_0|sensorDensity1.value_out|shaftPower.E_flow_in.1.|shaftPower.E_flow_in.2.|shaftPower.E_flow_in.3.|shaftPower.E_flow_out|v1|v2",fileNamePrefix="ThermofluidStream_ThermofluidStream.Idealized.Examples.TUMExercisesThermodynamicCycles.Exercise4DieselEngine.AdiabaticPerfectGas") [Timeout 660] "Notification: Performance of FrontEnd - loaded program: time 0.00109/0.00109, allocations: 87.86 kB / 0.6443 GB, free: 28.57 MB / 490.7 MB Notification: Performance of FrontEnd - Absyn->SCode: time 0.1368/0.1379, allocations: 88.78 MB / 0.731 GB, free: 3.602 MB / 0.5417 GB Notification: Performance of NFInst.instantiate(ThermofluidStream.Idealized.Examples.TUMExercisesThermodynamicCycles.Exercise4DieselEngine.AdiabaticPerfectGas): time 0.4479/0.5858, allocations: 137.8 MB / 0.8655 GB, free: 15.98 MB / 0.6511 GB Notification: Performance of NFInst.instExpressions: time 0.008682/0.5945, allocations: 8.711 MB / 0.874 GB, free: 15.32 MB / 0.6511 GB Notification: Performance of NFInst.updateImplicitVariability: time 0.001333/0.5958, allocations: 51.59 kB / 0.8741 GB, free: 15.29 MB / 0.6511 GB Notification: Performance of NFTyping.typeComponents: time 0.00108/0.5969, allocations: 434.6 kB / 0.8745 GB, free: 15.12 MB / 0.6511 GB Notification: Performance of NFTyping.typeBindings: time 0.003589/0.6005, allocations: 1.417 MB / 0.8759 GB, free: 14.67 MB / 0.6511 GB Notification: Performance of NFTyping.typeClassSections: time 0.002335/0.6028, allocations: 1.035 MB / 0.8769 GB, free: 14.51 MB / 0.6511 GB Notification: Performance of NFFlatten.flatten: time 0.00234/0.6051, allocations: 1.837 MB / 0.8787 GB, free: 13.91 MB / 0.6511 GB Notification: Performance of NFFlatten.resolveConnections: time 0.0003255/0.6055, allocations: 135 kB / 0.8788 GB, free: 13.84 MB / 0.6511 GB Notification: Performance of NFEvalConstants.evaluate: time 0.001326/0.6068, allocations: 0.75 MB / 0.8795 GB, free: 13.64 MB / 0.6511 GB Notification: Performance of NFSimplifyModel.simplify: time 0.001221/0.608, allocations: 0.8498 MB / 0.8804 GB, free: 13.48 MB / 0.6511 GB Notification: Performance of NFPackage.collectConstants: time 0.0001902/0.6082, allocations: 84.28 kB / 0.8804 GB, free: 13.48 MB / 0.6511 GB Notification: Performance of NFFlatten.collectFunctions: time 0.002796/0.611, allocations: 1.284 MB / 0.8817 GB, free: 13.19 MB / 0.6511 GB Notification: Performance of NFScalarize.scalarize: time 0.000212/0.6112, allocations: 237.5 kB / 0.8819 GB, free: 13.04 MB / 0.6511 GB Notification: Performance of NFVerifyModel.verify: time 0.0005704/0.6118, allocations: 0.4941 MB / 0.8824 GB, free: 12.79 MB / 0.6511 GB Notification: Performance of NFConvertDAE.convert: time 0.003211/0.615, allocations: 2.08 MB / 0.8844 GB, free: 12.09 MB / 0.6511 GB Notification: Performance of FrontEnd - DAE generated: time 4.308e-06/0.615, allocations: 0 / 0.8844 GB, free: 12.09 MB / 0.6511 GB Notification: Performance of FrontEnd: time 1.963e-06/0.615, allocations: 1.562 kB / 0.8844 GB, free: 12.09 MB / 0.6511 GB Notification: Performance of Transformations before backend: time 4.167e-05/0.615, allocations: 2.625 kB / 0.8844 GB, free: 12.09 MB / 0.6511 GB Notification: Model statistics after passing the front-end and creating the data structures used by the back-end: * Number of equations: 218 * Number of variables: 218 Notification: Performance of Generate backend data structure: time 0.002433/0.6175, allocations: 1.581 MB / 0.886 GB, free: 11.09 MB / 0.6511 GB Notification: Performance of prepare preOptimizeDAE: time 4.388e-05/0.6175, allocations: 8.406 kB / 0.886 GB, free: 11.09 MB / 0.6511 GB Notification: Performance of preOpt normalInlineFunction (simulation): time 0.0002513/0.6178, allocations: 150.5 kB / 0.8861 GB, free: 11.01 MB / 0.6511 GB Notification: Performance of preOpt evaluateParameters (simulation): time 0.001242/0.619, allocations: 0.8215 MB / 0.8869 GB, free: 10.55 MB / 0.6511 GB Notification: Performance of preOpt simplifyIfEquations (simulation): time 0.0001227/0.6191, allocations: 172.4 kB / 0.8871 GB, free: 10.39 MB / 0.6511 GB Notification: Performance of preOpt expandDerOperator (simulation): time 8.128e-05/0.6192, allocations: 88.56 kB / 0.8872 GB, free: 10.36 MB / 0.6511 GB Notification: Performance of preOpt clockPartitioning (simulation): time 0.001222/0.6204, allocations: 1.298 MB / 0.8885 GB, free: 9.527 MB / 0.6511 GB Notification: Performance of preOpt findStateOrder (simulation): time 1.815e-05/0.6205, allocations: 10.78 kB / 0.8885 GB, free: 9.52 MB / 0.6511 GB Notification: Performance of preOpt replaceEdgeChange (simulation): time 5.334e-05/0.6205, allocations: 37.28 kB / 0.8885 GB, free: 9.492 MB / 0.6511 GB Notification: Performance of preOpt inlineArrayEqn (simulation): time 1.294e-05/0.6205, allocations: 21.38 kB / 0.8885 GB, free: 9.492 MB / 0.6511 GB Notification: Performance of preOpt removeEqualRHS (simulation): time 0.001363/0.6219, allocations: 0.9712 MB / 0.8895 GB, free: 9.156 MB / 0.6511 GB Notification: Performance of preOpt removeSimpleEquations (simulation): time 0.003167/0.625, allocations: 3.214 MB / 0.8926 GB, free: 6.652 MB / 0.6511 GB Notification: Performance of preOpt comSubExp (simulation): time 0.0009468/0.626, allocations: 0.7785 MB / 0.8934 GB, free: 6.227 MB / 0.6511 GB Notification: Performance of preOpt resolveLoops (simulation): time 0.0003709/0.6264, allocations: 353.6 kB / 0.8937 GB, free: 6.043 MB / 0.6511 GB Notification: Performance of preOpt evalFunc (simulation): time 0.002036/0.6284, allocations: 1.614 MB / 0.8953 GB, free: 4.949 MB / 0.6511 GB Notification: Performance of preOpt encapsulateWhenConditions (simulation): time 3.388e-05/0.6284, allocations: 48.78 kB / 0.8953 GB, free: 4.898 MB / 0.6511 GB Notification: Performance of pre-optimization done (n=82): time 2.375e-06/0.6284, allocations: 0 / 0.8953 GB, free: 4.898 MB / 0.6511 GB Notification: Performance of matching and sorting (n=82): time 0.00148/0.6299, allocations: 1.022 MB / 0.8963 GB, free: 4.395 MB / 0.6511 GB Notification: Performance of inlineWhenForInitialization (initialization): time 4.342e-05/0.63, allocations: 91.95 kB / 0.8964 GB, free: 4.297 MB / 0.6511 GB Notification: Performance of selectInitializationVariablesDAE (initialization): time 0.0005799/0.6305, allocations: 0.736 MB / 0.8971 GB, free: 3.859 MB / 0.6511 GB Notification: Performance of collectPreVariables (initialization): time 3.868e-05/0.6306, allocations: 40.58 kB / 0.8972 GB, free: 3.816 MB / 0.6511 GB Notification: Performance of collectInitialEqns (initialization): time 0.0002752/0.6309, allocations: 0.5272 MB / 0.8977 GB, free: 3.344 MB / 0.6511 GB Notification: Performance of collectInitialBindings (initialization): time 0.000143/0.631, allocations: 295.1 kB / 0.898 GB, free: 3.094 MB / 0.6511 GB Notification: Performance of simplifyInitialFunctions (initialization): time 0.0001508/0.6311, allocations: 171.3 kB / 0.8981 GB, free: 2.988 MB / 0.6511 GB Notification: Performance of setup shared object (initialization): time 0.0001004/0.6312, allocations: 346.3 kB / 0.8985 GB, free: 2.652 MB / 0.6511 GB Notification: Performance of preBalanceInitialSystem (initialization): time 0.0002676/0.6315, allocations: 232.1 kB / 0.8987 GB, free: 2.543 MB / 0.6511 GB Notification: Performance of partitionIndependentBlocks (initialization): time 0.0004172/0.6319, allocations: 0.5053 MB / 0.8992 GB, free: 2.082 MB / 0.6511 GB Notification: Performance of analyzeInitialSystem (initialization): time 0.0009634/0.6329, allocations: 0.7625 MB / 0.8999 GB, free: 1.512 MB / 0.6511 GB Notification: Performance of solveInitialSystemEqSystem (initialization): time 4.499e-06/0.6329, allocations: 2.938 kB / 0.8999 GB, free: 1.512 MB / 0.6511 GB Notification: Performance of matching and sorting (n=115) (initialization): time 0.001014/0.6339, allocations: 0.9234 MB / 0.9008 GB, free: 1.039 MB / 0.6511 GB Notification: Performance of prepare postOptimizeDAE: time 2.013e-05/0.6339, allocations: 10.28 kB / 0.9008 GB, free: 1.039 MB / 0.6511 GB Notification: Performance of postOpt simplifyComplexFunction (initialization): time 9.187e-06/0.6339, allocations: 7.844 kB / 0.9008 GB, free: 1.039 MB / 0.6511 GB Notification: Performance of postOpt tearingSystem (initialization): time 0.0004209/0.6344, allocations: 131.7 kB / 0.901 GB, free: 0.9805 MB / 0.6511 GB Notification: Performance of postOpt solveSimpleEquations (initialization): time 0.0003781/0.6347, allocations: 209.3 kB / 0.9012 GB, free: 0.9297 MB / 0.6511 GB Notification: Performance of postOpt calculateStrongComponentJacobians (initialization): time 0.0003587/0.6351, allocations: 0.6103 MB / 0.9018 GB, free: 368 kB / 0.6511 GB Notification: Performance of postOpt simplifyAllExpressions (initialization): time 0.0003041/0.6354, allocations: 90.05 kB / 0.9019 GB, free: 304 kB / 0.6511 GB Notification: Performance of postOpt collapseArrayExpressions (initialization): time 5.34e-05/0.6355, allocations: 43.52 kB / 0.9019 GB, free: 292 kB / 0.6511 GB Notification: Model statistics after passing the back-end for initialization: * Number of independent subsystems: 34 * Number of states: 0 () * Number of discrete variables: 0 () * Number of discrete states: 0 () * Number of clocked states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for initialization (109): * Single equations (assignments): 108 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 0 * When equations: 0 * If-equations: 0 * Equation systems (not torn): 0 * Torn equation systems: 1 * Mixed (continuous/discrete) equation systems: 0 Notification: Torn system details for strict tearing set: * Linear torn systems (#iteration vars, #inner vars, density): 0 systems * Non-linear torn systems (#iteration vars, #inner vars): 1 system {(1,6)} Notification: Performance of prepare postOptimizeDAE: time 0.0002691/0.6357, allocations: 245.7 kB / 0.9021 GB, free: 84 kB / 0.6511 GB Notification: Performance of postOpt lateInlineFunction (simulation): time 0.0001008/0.6358, allocations: 114.1 kB / 0.9022 GB, free: 20 kB / 0.6511 GB Notification: Performance of postOpt wrapFunctionCalls (simulation): time 0.00133/0.6372, allocations: 1.177 MB / 0.9034 GB, free: 15.35 MB / 0.6667 GB Notification: Performance of postOpt inlineArrayEqn (simulation): time 1.115e-05/0.6372, allocations: 7.938 kB / 0.9034 GB, free: 15.35 MB / 0.6667 GB Notification: Performance of postOpt constantLinearSystem (simulation): time 6.121e-06/0.6372, allocations: 3.938 kB / 0.9034 GB, free: 15.34 MB / 0.6667 GB Notification: Performance of postOpt simplifysemiLinear (simulation): time 6.953e-06/0.6372, allocations: 7.922 kB / 0.9034 GB, free: 15.34 MB / 0.6667 GB Notification: Performance of postOpt removeSimpleEquations (simulation): time 0.001543/0.6387, allocations: 1.535 MB / 0.9049 GB, free: 14.36 MB / 0.6667 GB Notification: Performance of postOpt simplifyComplexFunction (simulation): time 5.18e-06/0.6387, allocations: 2.344 kB / 0.9049 GB, free: 14.36 MB / 0.6667 GB Notification: Performance of postOpt solveSimpleEquations (simulation): time 0.000253/0.639, allocations: 134.9 kB / 0.905 GB, free: 14.32 MB / 0.6667 GB Notification: Performance of postOpt tearingSystem (simulation): time 0.0002734/0.6393, allocations: 119.9 kB / 0.9052 GB, free: 14.27 MB / 0.6667 GB Notification: Performance of postOpt inputDerivativesUsed (simulation): time 3.192e-05/0.6393, allocations: 19.84 kB / 0.9052 GB, free: 14.25 MB / 0.6667 GB Notification: Performance of postOpt calculateStrongComponentJacobians (simulation): time 0.000327/0.6396, allocations: 0.6313 MB / 0.9058 GB, free: 13.67 MB / 0.6667 GB Notification: Performance of postOpt calculateStateSetsJacobians (simulation): time 4.749e-06/0.6396, allocations: 11.03 kB / 0.9058 GB, free: 13.66 MB / 0.6667 GB Notification: Performance of postOpt symbolicJacobian (simulation): time 0.000908/0.6405, allocations: 0.9514 MB / 0.9067 GB, free: 13.07 MB / 0.6667 GB Notification: Performance of postOpt removeConstants (simulation): time 0.0002337/0.6408, allocations: 193.7 kB / 0.9069 GB, free: 12.93 MB / 0.6667 GB Notification: Performance of postOpt simplifyTimeIndepFuncCalls (simulation): time 6.082e-05/0.6408, allocations: 24.25 kB / 0.9069 GB, free: 12.91 MB / 0.6667 GB Notification: Performance of postOpt simplifyAllExpressions (simulation): time 0.0002236/0.641, allocations: 29.3 kB / 0.907 GB, free: 12.89 MB / 0.6667 GB Notification: Performance of postOpt findZeroCrossings (simulation): time 6.734e-05/0.6411, allocations: 58.11 kB / 0.907 GB, free: 12.86 MB / 0.6667 GB Notification: Performance of postOpt collapseArrayExpressions (simulation): time 3.433e-05/0.6412, allocations: 26.31 kB / 0.907 GB, free: 12.85 MB / 0.6667 GB Notification: Performance of sorting global known variables: time 0.0003843/0.6415, allocations: 0.5071 MB / 0.9075 GB, free: 12.55 MB / 0.6667 GB Notification: Performance of sort global known variables: time 6e-08/0.6415, allocations: 0 / 0.9075 GB, free: 12.55 MB / 0.6667 GB Notification: Performance of remove unused functions: time 0.0008155/0.6424, allocations: 404.8 kB / 0.9079 GB, free: 12.43 MB / 0.6667 GB Notification: Model statistics after passing the back-end for simulation: * Number of independent subsystems: 9 * Number of states: 0 () * Number of discrete variables: 0 () * Number of discrete states: 0 () * Number of clocked states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for simulation (75): * Single equations (assignments): 71 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 3 * When equations: 0 * If-equations: 0 * Equation systems (not torn): 0 * Torn equation systems: 1 * Mixed (continuous/discrete) equation systems: 0 Notification: Torn system details for strict tearing set: * Linear torn systems (#iteration vars, #inner vars, density): 0 systems * Non-linear torn systems (#iteration vars, #inner vars): 1 system {(1,7)} Notification: Performance of Backend phase and start with SimCode phase: time 0.0005125/0.6429, allocations: 470.8 kB / 0.9084 GB, free: 12.19 MB / 0.6667 GB Notification: Performance of simCode: created initialization part: time 0.0008174/0.6437, allocations: 0.6496 MB / 0.909 GB, free: 11.91 MB / 0.6667 GB Notification: Performance of simCode: created event and clocks part: time 3.527e-06/0.6437, allocations: 4.688 kB / 0.909 GB, free: 11.91 MB / 0.6667 GB Notification: Performance of simCode: created simulation system equations: time 0.0003526/0.644, allocations: 325.2 kB / 0.9093 GB, free: 11.77 MB / 0.6667 GB Notification: Performance of simCode: created of all other equations (e.g. parameter, nominal, assert, etc): time 0.001351/0.6454, allocations: 0.5787 MB / 0.9099 GB, free: 11.47 MB / 0.6667 GB Notification: Performance of simCode: created linear, non-linear and system jacobian parts: time 0.00231/0.6477, allocations: 1.787 MB / 0.9116 GB, free: 10.36 MB / 0.6667 GB Notification: Performance of simCode: some other stuff during SimCode phase: time 0.0002886/0.648, allocations: 457 kB / 0.9121 GB, free: 10.1 MB / 0.6667 GB Notification: Performance of simCode: all other stuff during SimCode phase: time 0.0001682/0.6482, allocations: 111.5 kB / 0.9122 GB, free: 10.07 MB / 0.6667 GB Notification: Performance of SimCode: time 9.01e-07/0.6482, allocations: 0 / 0.9122 GB, free: 10.07 MB / 0.6667 GB Notification: Performance of Templates: time 0.0279/0.6761, allocations: 23.96 MB / 0.9356 GB, free: 7.93 MB / 0.6823 GB " [Timeout remaining time 659] make -j1 -f ThermofluidStream_ThermofluidStream.Idealized.Examples.TUMExercisesThermodynamicCycles.Exercise4DieselEngine.AdiabaticPerfectGas.makefile [Timeout 660] (rm -f ThermofluidStream_ThermofluidStream.Idealized.Examples.TUMExercisesThermodynamicCycles.Exercise4DieselEngine.AdiabaticPerfectGas.pipe ; mkfifo ThermofluidStream_ThermofluidStream.Idealized.Examples.TUMExercisesThermodynamicCycles.Exercise4DieselEngine.AdiabaticPerfectGas.pipe ; head -c 1048576 < ThermofluidStream_ThermofluidStream.Idealized.Examples.TUMExercisesThermodynamicCycles.Exercise4DieselEngine.AdiabaticPerfectGas.pipe >> ../files/ThermofluidStream_ThermofluidStream.Idealized.Examples.TUMExercisesThermodynamicCycles.Exercise4DieselEngine.AdiabaticPerfectGas.sim & ./ThermofluidStream_ThermofluidStream.Idealized.Examples.TUMExercisesThermodynamicCycles.Exercise4DieselEngine.AdiabaticPerfectGas -emit_protected > ThermofluidStream_ThermofluidStream.Idealized.Examples.TUMExercisesThermodynamicCycles.Exercise4DieselEngine.AdiabaticPerfectGas.pipe 2>&1) [Timeout 1200] diffSimulationResults("ThermofluidStream_ThermofluidStream.Idealized.Examples.TUMExercisesThermodynamicCycles.Exercise4DieselEngine.AdiabaticPerfectGas_res.mat","/mnt/ReferenceFiles/ThermofluidStream-main-regression/ReferenceData/ThermofluidStream.Idealized.Examples.TUMExercisesThermodynamicCycles.Exercise4DieselEngine.AdiabaticPerfectGas_ref.mat","/var/lib/jenkins/ws/OpenModelicaLibraryTestingWork/OpenModelicaLibraryTesting/files/ThermofluidStream_ThermofluidStream.Idealized.Examples.TUMExercisesThermodynamicCycles.Exercise4DieselEngine.AdiabaticPerfectGas.diff",relTol=0.003,relTolDiffMinMax=0.003,rangeDelta=0.001) [Timeout 660] "Error: Could not read variable CPUtime in file ThermofluidStream_ThermofluidStream.Idealized.Examples.TUMExercisesThermodynamicCycles.Exercise4DieselEngine.AdiabaticPerfectGas_res.mat. Warning: Get data of variable CPUtime from file ThermofluidStream_ThermofluidStream.Idealized.Examples.TUMExercisesThermodynamicCycles.Exercise4DieselEngine.AdiabaticPerfectGas_res.mat failed! Error: Could not read variable EventCounter in file ThermofluidStream_ThermofluidStream.Idealized.Examples.TUMExercisesThermodynamicCycles.Exercise4DieselEngine.AdiabaticPerfectGas_res.mat. Warning: Get data of variable EventCounter from file ThermofluidStream_ThermofluidStream.Idealized.Examples.TUMExercisesThermodynamicCycles.Exercise4DieselEngine.AdiabaticPerfectGas_res.mat failed! Error: Could not read variable NonlinearSystems.initialization[1].Calls in file ThermofluidStream_ThermofluidStream.Idealized.Examples.TUMExercisesThermodynamicCycles.Exercise4DieselEngine.AdiabaticPerfectGas_res.mat. Warning: Get data of variable NonlinearSystems.initialization[1].Calls from file ThermofluidStream_ThermofluidStream.Idealized.Examples.TUMExercisesThermodynamicCycles.Exercise4DieselEngine.AdiabaticPerfectGas_res.mat failed! Error: Could not read variable NonlinearSystems.initialization[1].Iterations in file ThermofluidStream_ThermofluidStream.Idealized.Examples.TUMExercisesThermodynamicCycles.Exercise4DieselEngine.AdiabaticPerfectGas_res.mat. Warning: Get data of variable NonlinearSystems.initialization[1].Iterations from file ThermofluidStream_ThermofluidStream.Idealized.Examples.TUMExercisesThermodynamicCycles.Exercise4DieselEngine.AdiabaticPerfectGas_res.mat failed! Error: Could not read variable NonlinearSystems.initialization[1].Jacobians in file ThermofluidStream_ThermofluidStream.Idealized.Examples.TUMExercisesThermodynamicCycles.Exercise4DieselEngine.AdiabaticPerfectGas_res.mat. Warning: Get data of variable NonlinearSystems.initialization[1].Jacobians from file ThermofluidStream_ThermofluidStream.Idealized.Examples.TUMExercisesThermodynamicCycles.Exercise4DieselEngine.AdiabaticPerfectGas_res.mat failed! Error: Could not read variable NonlinearSystems.initialization[1].Residues in file ThermofluidStream_ThermofluidStream.Idealized.Examples.TUMExercisesThermodynamicCycles.Exercise4DieselEngine.AdiabaticPerfectGas_res.mat. Warning: Get data of variable NonlinearSystems.initialization[1].Residues from file ThermofluidStream_ThermofluidStream.Idealized.Examples.TUMExercisesThermodynamicCycles.Exercise4DieselEngine.AdiabaticPerfectGas_res.mat failed! Error: Could not read variable _derdummy in file ThermofluidStream_ThermofluidStream.Idealized.Examples.TUMExercisesThermodynamicCycles.Exercise4DieselEngine.AdiabaticPerfectGas_res.mat. Warning: Get data of variable _derdummy from file ThermofluidStream_ThermofluidStream.Idealized.Examples.TUMExercisesThermodynamicCycles.Exercise4DieselEngine.AdiabaticPerfectGas_res.mat failed! Error: Could not read variable _dummy in file ThermofluidStream_ThermofluidStream.Idealized.Examples.TUMExercisesThermodynamicCycles.Exercise4DieselEngine.AdiabaticPerfectGas_res.mat. Warning: Get data of variable _dummy from file ThermofluidStream_ThermofluidStream.Idealized.Examples.TUMExercisesThermodynamicCycles.Exercise4DieselEngine.AdiabaticPerfectGas_res.mat failed! Error: Could not read variable combustion.P in file ThermofluidStream_ThermofluidStream.Idealized.Examples.TUMExercisesThermodynamicCycles.Exercise4DieselEngine.AdiabaticPerfectGas_res.mat. Warning: Get data of variable combustion.P from file ThermofluidStream_ThermofluidStream.Idealized.Examples.TUMExercisesThermodynamicCycles.Exercise4DieselEngine.AdiabaticPerfectGas_res.mat failed! Error: Could not read variable combustion.assertionLevel in file ThermofluidStream_ThermofluidStream.Idealized.Examples.TUMExercisesThermodynamicCycles.Exercise4DieselEngine.AdiabaticPerfectGas_res.mat. Warning: Get data of variable combustion.assertionLevel from file ThermofluidStream_ThermofluidStream.Idealized.Examples.TUMExercisesThermodynamicCycles.Exercise4DieselEngine.AdiabaticPerfectGas_res.mat failed! Error: Could not read variable combustion.dh_fixed in file ThermofluidStream_ThermofluidStream.Idealized.Examples.TUMExercisesThermodynamicCycles.Exercise4DieselEngine.AdiabaticPerfectGas_res.mat. Warning: Get data of variable combustion.dh_fixed from file ThermofluidStream_ThermofluidStream.Idealized.Examples.TUMExercisesThermodynamicCycles.Exercise4DieselEngine.AdiabaticPerfectGas_res.mat failed! Error: Could not read variable combustion.du in file ThermofluidStream_ThermofluidStream.Idealized.Examples.TUMExercisesThermodynamicCycles.Exercise4DieselEngine.AdiabaticPerfectGas_res.mat. Warning: Get data of variable combustion.du from file ThermofluidStream_ThermofluidStream.Idealized.Examples.TUMExercisesThermodynamicCycles.Exercise4DieselEngine.AdiabaticPerfectGas_res.mat failed! Error: Could not read variable combustion.h_out_fixed in file ThermofluidStream_ThermofluidStream.Idealized.Examples.TUMExercisesThermodynamicCycles.Exercise4DieselEngine.AdiabaticPerfectGas_res.mat. Warning: Get data of variable combustion.h_out_fixed from file ThermofluidStream_ThermofluidStream.Idealized.Examples.TUMExercisesThermodynamicCycles.Exercise4DieselEngine.AdiabaticPerfectGas_res.mat failed! Error: Could not read variable combustion.inlet.der(m_flow) in file ThermofluidStream_ThermofluidStream.Idealized.Examples.TUMExercisesThermodynamicCycles.Exercise4DieselEngine.AdiabaticPerfectGas_res.mat. Warning: Get data of variable combustion.inlet.der(m_flow) from file ThermofluidStream_ThermofluidStream.Idealized.Examples.TUMExercisesThermodynamicCycles.Exercise4DieselEngine.AdiabaticPerfectGas_res.mat failed! Error: Could not read variable combustion.p_inf in file ThermofluidStream_ThermofluidStream.Idealized.Examples.TUMExercisesThermodynamicCycles.Exercise4DieselEngine.AdiabaticPerfectGas_res.mat. Warning: Get data of variable combustion.p_inf from file ThermofluidStream_ThermofluidStream.Idealized.Examples.TUMExercisesThermodynamicCycles.Exercise4DieselEngine.AdiabaticPerfectGas_res.mat failed! Error: Could not read variable combustion.rho_in in file ThermofluidStream_ThermofluidStream.Idealized.Examples.TUMExercisesThermodynamicCycles.Exercise4DieselEngine.AdiabaticPerfectGas_res.mat. Warning: Get data of variable combustion.rho_in from file ThermofluidStream_ThermofluidStream.Idealized.Examples.TUMExercisesThermodynamicCycles.Exercise4DieselEngine.AdiabaticPerfectGas_res.mat failed! Error: Could not read variable combustion.rho_out in file ThermofluidStream_ThermofluidStream.Idealized.Examples.TUMExercisesThermodynamicCycles.Exercise4DieselEngine.AdiabaticPerfectGas_res.mat. Warning: Get data of variable combustion.rho_out from file ThermofluidStream_ThermofluidStream.Idealized.Examples.TUMExercisesThermodynamicCycles.Exercise4DieselEngine.AdiabaticPerfectGas_res.mat failed! Error: Could not read variable combustion.u_in in file ThermofluidStream_ThermofluidStream.Idealized.Examples.TUMExercisesThermodynamicCycles.Exercise4DieselEngine.AdiabaticPerfectGas_res.mat. Warning: Get data of variable combustion.u_in from file ThermofluidStream_ThermofluidStream.Idealized.Examples.TUMExercisesThermodynamicCycles.Exercise4DieselEngine.AdiabaticPerfectGas_res.mat failed! Error: Could not read variable combustion.u_out in file ThermofluidStream_ThermofluidStream.Idealized.Examples.TUMExercisesThermodynamicCycles.Exercise4DieselEngine.AdiabaticPerfectGas_res.mat. Warning: Get data of variable combustion.u_out from file ThermofluidStream_ThermofluidStream.Idealized.Examples.TUMExercisesThermodynamicCycles.Exercise4DieselEngine.AdiabaticPerfectGas_res.mat failed! Error: Could not read variable combustion.v_in in file ThermofluidStream_ThermofluidStream.Idealized.Examples.TUMExercisesThermodynamicCycles.Exercise4DieselEngine.AdiabaticPerfectGas_res.mat. Warning: Get data of variable combustion.v_in from file ThermofluidStream_ThermofluidStream.Idealized.Examples.TUMExercisesThermodynamicCycles.Exercise4DieselEngine.AdiabaticPerfectGas_res.mat failed! Error: Could not read variable combustion.v_out in file ThermofluidStream_ThermofluidStream.Idealized.Examples.TUMExercisesThermodynamicCycles.Exercise4DieselEngine.AdiabaticPerfectGas_res.mat. Warning: Get data of variable combustion.v_out from file ThermofluidStream_ThermofluidStream.Idealized.Examples.TUMExercisesThermodynamicCycles.Exercise4DieselEngine.AdiabaticPerfectGas_res.mat failed! Error: Could not read variable combustion.w_amb in file ThermofluidStream_ThermofluidStream.Idealized.Examples.TUMExercisesThermodynamicCycles.Exercise4DieselEngine.AdiabaticPerfectGas_res.mat. Warning: Get data of variable combustion.w_amb from file ThermofluidStream_ThermofluidStream.Idealized.Examples.TUMExercisesThermodynamicCycles.Exercise4DieselEngine.AdiabaticPerfectGas_res.mat failed! Error: Could not read variable combustion.w_exp in file ThermofluidStream_ThermofluidStream.Idealized.Examples.TUMExercisesThermodynamicCycles.Exercise4DieselEngine.AdiabaticPerfectGas_res.mat. Warning: Get data of variable combustion.w_exp from file ThermofluidStream_ThermofluidStream.Idealized.Examples.TUMExercisesThermodynamicCycles.Exercise4DieselEngine.AdiabaticPerfectGas_res.mat failed! Error: Could not read variable combustion.w_exp_net in file ThermofluidStream_ThermofluidStream.Idealized.Examples.TUMExercisesThermodynamicCycles.Exercise4DieselEngine.AdiabaticPerfectGas_res.mat. Warning: Get data of variable combustion.w_exp_net from file ThermofluidStream_ThermofluidStream.Idealized.Examples.TUMExercisesThermodynamicCycles.Exercise4DieselEngine.AdiabaticPerfectGas_res.mat failed! Error: Could not read variable compression.P_nom in file ThermofluidStream_ThermofluidStream.Idealized.Examples.TUMExercisesThermodynamicCycles.Exercise4DieselEngine.AdiabaticPerfectGas_res.mat. Warning: Get data of variable compression.P_nom from file ThermofluidStream_ThermofluidStream.Idealized.Examples.TUMExercisesThermodynamicCycles.Exercise4DieselEngine.AdiabaticPerfectGas_res.mat failed! Error: Could not read variable compression.TC in file ThermofluidStream_ThermofluidStream.Idealized.Examples.TUMExercisesThermodynamicCycles.Exercise4DieselEngine.AdiabaticPerfectGas_res.mat. Warning: Get data of variable compression.TC from file ThermofluidStream_ThermofluidStream.Idealized.Examples.TUMExercisesThermodynamicCycles.Exercise4DieselEngine.AdiabaticPerfectGas_res.mat failed! Error: Could not read variable compression.adiabaticModel.cp_fixed in file ThermofluidStream_ThermofluidStream.Idealized.Examples.TUMExercisesThermodynamicCycles.Exercise4DieselEngine.AdiabaticPerfectGas_res.mat. Warning: Get data of variable compression.adiabaticModel.cp_fixed from file ThermofluidStream_ThermofluidStream.Idealized.Examples.TUMExercisesThermodynamicCycles.Exercise4DieselEngine.AdiabaticPerfectGas_res.mat failed! Error: Could not read variable compression.adiabaticModel.gamma_fixed in file ThermofluidStream_ThermofluidStream.Idealized.Examples.TUMExercisesThermodynamicCycles.Exercise4DieselEngine.AdiabaticPerfectGas_res.mat. Warning: Get data of variable compression.adiabaticModel.gamma_fixed from file ThermofluidStream_ThermofluidStream.Idealized.Examples.TUMExercisesThermodynamicCycles.Exercise4DieselEngine.AdiabaticPerfectGas_res.mat failed! Error: Could not read variable compression.assertionLevel in file ThermofluidStream_ThermofluidStream.Idealized.Examples.TUMExercisesThermodynamicCycles.Exercise4DieselEngine.AdiabaticPerfectGas_res.mat. Warning: Get data of variable compression.assertionLevel from file ThermofluidStream_ThermofluidStream.Idealized.Examples.TUMExercisesThermodynamicCycles.Exercise4DieselEngine.AdiabaticPerfectGas_res.mat failed! Error: Could not read variable compression.dp_fixed in file ThermofluidStream_ThermofluidStream.Idealized.Examples.TUMExercisesThermodynamicCycles.Exercise4DieselEngine.AdiabaticPerfectGas_res.mat. Warning: Get data of variable compression.dp_fixed from file ThermofluidStream_ThermofluidStream.Idealized.Examples.TUMExercisesThermodynamicCycles.Exercise4DieselEngine.AdiabaticPerfectGas_res.mat failed! Error: Could not read variable compression.dp_nom in file ThermofluidStream_ThermofluidStream.Idealized.Examples.TUMExercisesThermodynamicCycles.Exercise4DieselEngine.AdiabaticPerfectGas_res.mat. Warning: Get data of variable compression.dp_nom from file ThermofluidStream_ThermofluidStream.Idealized.Examples.TUMExercisesThermodynamicCycles.Exercise4DieselEngine.AdiabaticPerfectGas_res.mat failed! Error: Could not read variable compression.dp_start in file ThermofluidStream_ThermofluidStream.Idealized.Examples.TUMExercisesThermodynamicCycles.Exercise4DieselEngine.AdiabaticPerfectGas_res.mat. Warning: Get data of variable compression.dp_start from file ThermofluidStream_ThermofluidStream.Idealized.Examples.TUMExercisesThermodynamicCycles.Exercise4DieselEngine.AdiabaticPerfectGas_res.mat failed! Error: Could not read variable compression.inlet.der(m_flow) in file ThermofluidStream_ThermofluidStream.Idealized.Examples.TUMExercisesThermodynamicCycles.Exercise4DieselEngine.AdiabaticPerfectGas_res.mat. Warning: Get data of variable compression.inlet.der(m_flow) from file ThermofluidStream_ThermofluidStream.Idealized.Examples.TUMExercisesThermodynamicCycles.Exercise4DieselEngine.AdiabaticPerfectGas_res.mat failed! Error: Could not read variable compression.p_out_fixed in file ThermofluidStream_ThermofluidStream.Idealized.Examples.TUMExercisesThermodynamicCycles.Exercise4DieselEngine.AdiabaticPerfectGas_res.mat. Warning: Get data of variable compression.p_out_fixed from file ThermofluidStream_ThermofluidStream.Idealized.Examples.TUMExercisesThermodynamicCycles.Exercise4DieselEngine.AdiabaticPerfectGas_res.mat failed! Error: Could not read variable dropOfCommons.instanceNameColor[1] in file ThermofluidStream_ThermofluidStream.Idealized.Examples.TUMExercisesThermodynamicCycles.Exercise4DieselEngine.AdiabaticPerfectGas_res.mat. Warning: Get data of variable dropOfCommons.instanceNameColor[1] from file ThermofluidStream_ThermofluidStream.Idealized.Examples.TUMExercisesThermodynamicCycles.Exercise4DieselEngine.AdiabaticPerfectGas_res.mat failed! Error: Could not read variable dropOfCommons.instanceNameColor[2] in file ThermofluidStream_ThermofluidStream.Idealized.Examples.TUMExercisesThermodynamicCycles.Exercise4DieselEngine.AdiabaticPerfectGas_res.mat. Warning: Get data of variable dropOfCommons.instanceNameColor[2] from file ThermofluidStream_ThermofluidStream.Idealized.Examples.TUMExercisesThermodynamicCycles.Exercise4DieselEngine.AdiabaticPerfectGas_res.mat failed! Error: Could not read variable dropOfCommons.instanceNameColor[3] in file ThermofluidStream_ThermofluidStream.Idealized.Examples.TUMExercisesThermodynamicCycles.Exercise4DieselEngine.AdiabaticPerfectGas_res.mat. Warning: Get data of variable dropOfCommons.instanceNameColor[3] from file ThermofluidStream_ThermofluidStream.Idealized.Examples.TUMExercisesThermodynamicCycles.Exercise4DieselEngine.AdiabaticPerfectGas_res.mat failed! Error: Could not read variable expansion.P_nom in file ThermofluidStream_ThermofluidStream.Idealized.Examples.TUMExercisesThermodynamicCycles.Exercise4DieselEngine.AdiabaticPerfectGas_res.mat. Warning: Get data of variable expansion.P_nom from file ThermofluidStream_ThermofluidStream.Idealized.Examples.TUMExercisesThermodynamicCycles.Exercise4DieselEngine.AdiabaticPerfectGas_res.mat failed! Error: Could not read variable expansion.TC in file ThermofluidStream_ThermofluidStream.Idealized.Examples.TUMExercisesThermodynamicCycles.Exercise4DieselEngine.AdiabaticPerfectGas_res.mat. Warning: Get data of variable expansion.TC from file ThermofluidStream_ThermofluidStream.Idealized.Examples.TUMExercisesThermodynamicCycles.Exercise4DieselEngine.AdiabaticPerfectGas_res.mat failed! Error: Could not read variable expansion.adiabaticModel.cp_fixed in file ThermofluidStream_ThermofluidStream.Idealized.Examples.TUMExercisesThermodynamicCycles.Exercise4DieselEngine.AdiabaticPerfectGas_res.mat. Warning: Get data of variable expansion.adiabaticModel.cp_fixed from file ThermofluidStream_ThermofluidStream.Idealized.Examples.TUMExercisesThermodynamicCycles.Exercise4DieselEngine.AdiabaticPerfectGas_res.mat failed! Error: Could not read variable expansion.adiabaticModel.gamma_fixed in file ThermofluidStream_ThermofluidStream.Idealized.Examples.TUMExercisesThermodynamicCycles.Exercise4DieselEngine.AdiabaticPerfectGas_res.mat. Warning: Get data of variable expansion.adiabaticModel.gamma_fixed from file ThermofluidStream_ThermofluidStream.Idealized.Examples.TUMExercisesThermodynamicCycles.Exercise4DieselEngine.AdiabaticPerfectGas_res.mat failed! Error: Could not read variable expansion.assertionLevel in file ThermofluidStream_ThermofluidStream.Idealized.Examples.TUMExercisesThermodynamicCycles.Exercise4DieselEngine.AdiabaticPerfectGas_res.mat. Warning: Get data of variable expansion.assertionLevel from file ThermofluidStream_ThermofluidStream.Idealized.Examples.TUMExercisesThermodynamicCycles.Exercise4DieselEngine.AdiabaticPerfectGas_res.mat failed! Error: Could not read variable expansion.dp_fixed in file ThermofluidStream_ThermofluidStream.Idealized.Examples.TUMExercisesThermodynamicCycles.Exercise4DieselEngine.AdiabaticPerfectGas_res.mat. Warning: Get data of variable expansion.dp_fixed from file ThermofluidStream_ThermofluidStream.Idealized.Examples.TUMExercisesThermodynamicCycles.Exercise4DieselEngine.AdiabaticPerfectGas_res.mat failed! Error: Could not read variable expansion.dp_nom in file ThermofluidStream_ThermofluidStream.Idealized.Examples.TUMExercisesThermodynamicCycles.Exercise4DieselEngine.AdiabaticPerfectGas_res.mat. Warning: Get data of variable expansion.dp_nom from file ThermofluidStream_ThermofluidStream.Idealized.Examples.TUMExercisesThermodynamicCycles.Exercise4DieselEngine.AdiabaticPerfectGas_res.mat failed! Error: Could not read variable expansion.dp_start in file ThermofluidStream_ThermofluidStream.Idealized.Examples.TUMExercisesThermodynamicCycles.Exercise4DieselEngine.AdiabaticPerfectGas_res.mat. Warning: Get data of variable expansion.dp_start from file ThermofluidStream_ThermofluidStream.Idealized.Examples.TUMExercisesThermodynamicCycles.Exercise4DieselEngine.AdiabaticPerfectGas_res.mat failed! Error: Could not read variable expansion.inlet.der(m_flow) in file ThermofluidStream_ThermofluidStream.Idealized.Examples.TUMExercisesThermodynamicCycles.Exercise4DieselEngine.AdiabaticPerfectGas_res.mat. Warning: Get data of variable expansion.inlet.der(m_flow) from file ThermofluidStream_ThermofluidStream.Idealized.Examples.TUMExercisesThermodynamicCycles.Exercise4DieselEngine.AdiabaticPerfectGas_res.mat failed! Error: Could not read variable expansion.pRatio_fixed in file ThermofluidStream_ThermofluidStream.Idealized.Examples.TUMExercisesThermodynamicCycles.Exercise4DieselEngine.AdiabaticPerfectGas_res.mat. Warning: Get data of variable expansion.pRatio_fixed from file ThermofluidStream_ThermofluidStream.Idealized.Examples.TUMExercisesThermodynamicCycles.Exercise4DieselEngine.AdiabaticPerfectGas_res.mat failed! Error: Could not read variable expansion.p_out_fixed in file ThermofluidStream_ThermofluidStream.Idealized.Examples.TUMExercisesThermodynamicCycles.Exercise4DieselEngine.AdiabaticPerfectGas_res.mat. Warning: Get data of variable expansion.p_out_fixed from file ThermofluidStream_ThermofluidStream.Idealized.Examples.TUMExercisesThermodynamicCycles.Exercise4DieselEngine.AdiabaticPerfectGas_res.mat failed! Error: Could not read variable gasExchange.assertionLevel in file ThermofluidStream_ThermofluidStream.Idealized.Examples.TUMExercisesThermodynamicCycles.Exercise4DieselEngine.AdiabaticPerfectGas_res.mat. Warning: Get data of variable gasExchange.assertionLevel from file ThermofluidStream_ThermofluidStream.Idealized.Examples.TUMExercisesThermodynamicCycles.Exercise4DieselEngine.AdiabaticPerfectGas_res.mat failed! Error: Could not read variable gasExchange.dp_start in file ThermofluidStream_ThermofluidStream.Idealized.Examples.TUMExercisesThermodynamicCycles.Exercise4DieselEngine.AdiabaticPerfectGas_res.mat. Warning: Get data of variable gasExchange.dp_start from file ThermofluidStream_ThermofluidStream.Idealized.Examples.TUMExercisesThermodynamicCycles.Exercise4DieselEngine.AdiabaticPerfectGas_res.mat failed! Error: Could not read variable gasExchange.inlet.der(m_flow) in file ThermofluidStream_ThermofluidStream.Idealized.Examples.TUMExercisesThermodynamicCycles.Exercise4DieselEngine.AdiabaticPerfectGas_res.mat. Warning: Get data of variable gasExchange.inlet.der(m_flow) from file ThermofluidStream_ThermofluidStream.Idealized.Examples.TUMExercisesThermodynamicCycles.Exercise4DieselEngine.AdiabaticPerfectGas_res.mat failed! Error: Could not read variable loopBreaker.h_out_fixed in file ThermofluidStream_ThermofluidStream.Idealized.Examples.TUMExercisesThermodynamicCycles.Exercise4DieselEngine.AdiabaticPerfectGas_res.mat. Warning: Get data of variable loopBreaker.h_out_fixed from file ThermofluidStream_ThermofluidStream.Idealized.Examples.TUMExercisesThermodynamicCycles.Exercise4DieselEngine.AdiabaticPerfectGas_res.mat failed! Error: Could not read variable loopBreaker.outlet.der(m_flow) in file ThermofluidStream_ThermofluidStream.Idealized.Examples.TUMExercisesThermodynamicCycles.Exercise4DieselEngine.AdiabaticPerfectGas_res.mat. Warning: Get data of variable loopBreaker.outlet.der(m_flow) from file ThermofluidStream_ThermofluidStream.Idealized.Examples.TUMExercisesThermodynamicCycles.Exercise4DieselEngine.AdiabaticPerfectGas_res.mat failed! " [Timeout remaining time 660] "" Variables in the reference:CPUtime,EventCounter,NonlinearSystems.initialization[1].Calls,NonlinearSystems.initialization[1].Iterations,NonlinearSystems.initialization[1].Jacobians,NonlinearSystems.initialization[1].Residues,T1,T3,Time,_derdummy,_dummy,combustion.L,combustion.P,combustion.Q_flow,combustion.T_out_fixed,combustion.assertionLevel,combustion.clip_p_out,combustion.dT,combustion.dT_fixed,combustion.dh,combustion.dh_fixed,combustion.dp,combustion.dr_corr,combustion.du,combustion.h_in,combustion.h_out,combustion.h_out_fixed,combustion.initM_flow,der(combustion.inlet.m_flow),combustion.inlet.m_flow,combustion.inlet.r,combustion.inlet.state.T,combustion.inlet.state.p,combustion.m_acceleration_0,combustion.m_flow,combustion.m_flowStateSelect,combustion.m_flow_0,combustion.outlet.m_flow,combustion.outlet.r,combustion.outlet.state.T,combustion.outlet.state.p,combustion.outletSpec,combustion.outletSpec_actual,combustion.outletValueSpec,combustion.p,combustion.p_in,combustion.p_inf,combustion.p_min,combustion.p_out,combustion.q,combustion.rho_in,combustion.rho_out,combustion.singularityRegime,combustion.systemSpec,combustion.u_in,combustion.u_out,combustion.v_in,combustion.v_out,combustion.w_amb,combustion.w_exp,combustion.w_exp_net,compression.L,compression.P,compression.P_nom,compression.P_out,compression.TC,compression.adiabaticModel.T_out,compression.adiabaticModel.T_out_is,compression.adiabaticModel.Z_in,compression.adiabaticModel.Z_out,compression.adiabaticModel.assertionLevel,compression.adiabaticModel.cp,compression.adiabaticModel.cpSpec,compression.adiabaticModel.cp_fixed,compression.adiabaticModel.cp_in,compression.adiabaticModel.cp_out,compression.adiabaticModel.delta_cp_rel,compression.adiabaticModel.delta_gamma_rel,compression.adiabaticModel.eta_is,compression.adiabaticModel.gamma,compression.adiabaticModel.gammaSpec,compression.adiabaticModel.gamma_fixed,compression.adiabaticModel.gamma_in,compression.adiabaticModel.gamma_out,compression.adiabaticModel.h_out,compression.adiabaticModel.isCpWithinTol,compression.adiabaticModel.isGammaWithinTol,compression.adiabaticModel.isInletIdealGas,compression.adiabaticModel.isOutletIdealGas,compression.adiabaticModel.p_out,compression.adiabaticModel.relTolCp,compression.adiabaticModel.relTolGamma,compression.adiabaticModel.relTolZ,compression.adiabaticModel.state_in.T,compression.adiabaticModel.state_in.p,compression.adiabaticModel.state_out.T,compression.adiabaticModel.state_out.p,compression.adiabaticModel.w_t,compression.adiabaticModel.w_t_is,compression.assertionLevel,compression.clip_p_out,compression.dh,compression.dp,compression.dp_fixed,compression.dp_nom,compression.dp_start,compression.dr_corr,compression.etaSpec,compression.eta_actual,compression.eta_fixed,compression.eta_is,compression.h_in,compression.h_out,compression.initM_flow,der(compression.inlet.m_flow),compression.inlet.m_flow,compression.inlet.r,compression.inlet.state.T,compression.inlet.state.p,compression.m_acceleration_0,compression.m_flow,compression.m_flowStateSelect,compression.m_flow_0,compression.outlet.m_flow,compression.outlet.r,compression.outlet.state.T,compression.outlet.state.p,compression.outletSpec,compression.outletSpec_actual,compression.outletValueSpec,compression.pRatio,compression.pRatio_fixed,compression.p_in,compression.p_min,compression.p_out,compression.p_out_fixed,compression.singularityRegime,compressionRatio,density1.y,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,efficiency.displayVariablefinal,efficiency.showNumber,efficiency.significantDigits,exhaustTemperature.displayVariablefinal,exhaustTemperature.showNumber,exhaustTemperature.significantDigits,expansion.L,expansion.P,expansion.P_nom,expansion.P_out,expansion.TC,expansion.adiabaticModel.T_out,expansion.adiabaticModel.T_out_is,expansion.adiabaticModel.Z_in,expansion.adiabaticModel.Z_out,expansion.adiabaticModel.assertionLevel,expansion.adiabaticModel.cp,expansion.adiabaticModel.cpSpec,expansion.adiabaticModel.cp_fixed,expansion.adiabaticModel.cp_in,expansion.adiabaticModel.cp_out,expansion.adiabaticModel.delta_cp_rel,expansion.adiabaticModel.delta_gamma_rel,expansion.adiabaticModel.eta_is,expansion.adiabaticModel.gamma,expansion.adiabaticModel.gammaSpec,expansion.adiabaticModel.gamma_fixed,expansion.adiabaticModel.gamma_in,expansion.adiabaticModel.gamma_out,expansion.adiabaticModel.h_out,expansion.adiabaticModel.isCpWithinTol,expansion.adiabaticModel.isGammaWithinTol,expansion.adiabaticModel.isInletIdealGas,expansion.adiabaticModel.isOutletIdealGas,expansion.adiabaticModel.p_out,expansion.adiabaticModel.relTolCp,expansion.adiabaticModel.relTolGamma,expansion.adiabaticModel.relTolZ,expansion.adiabaticModel.state_in.T,expansion.adiabaticModel.state_in.p,expansion.adiabaticModel.state_out.T,expansion.adiabaticModel.state_out.p,expansion.adiabaticModel.w_t,expansion.adiabaticModel.w_t_is,expansion.assertionLevel,expansion.clip_p_out,expansion.dh,expansion.dp,expansion.dp_fixed,expansion.dp_nom,expansion.dp_start,expansion.dr_corr,expansion.etaSpec,expansion.eta_actual,expansion.eta_fixed,expansion.eta_is,expansion.h_in,expansion.h_out,expansion.initM_flow,der(expansion.inlet.m_flow),expansion.inlet.m_flow,expansion.inlet.r,expansion.inlet.state.T,expansion.inlet.state.p,expansion.m_acceleration_0,expansion.m_flow,expansion.m_flowStateSelect,expansion.m_flow_0,expansion.outlet.m_flow,expansion.outlet.r,expansion.outlet.state.T,expansion.outlet.state.p,expansion.outletSpec,expansion.outletSpec_actual,expansion.outletSpec_prescribed,expansion.outletValueSpec,expansion.pRatio,expansion.pRatio_fixed,expansion.p_in,expansion.p_min,expansion.p_out,expansion.p_out_fixed,expansion.singularityRegime,gamma,gasExchange.L,gasExchange.P,gasExchange.P_out,gasExchange.Q_flow,gasExchange.T_out_fixed,gasExchange.assertionLevel,gasExchange.clip_p_out,gasExchange.dT,gasExchange.dT_fixed,gasExchange.dp,gasExchange.dp_start,gasExchange.dr_corr,gasExchange.du,gasExchange.h_in,gasExchange.h_out,gasExchange.initM_flow,der(gasExchange.inlet.m_flow),gasExchange.inlet.m_flow,gasExchange.inlet.r,gasExchange.inlet.state.T,gasExchange.inlet.state.p,gasExchange.m_acceleration_0,gasExchange.m_flow,gasExchange.m_flowStateSelect,gasExchange.m_flow_0,gasExchange.outlet.m_flow,gasExchange.outlet.r,gasExchange.outlet.state.T,gasExchange.outlet.state.p,gasExchange.outletSpec,gasExchange.outletSpec_actual,gasExchange.outletValueSpec,gasExchange.p_in,gasExchange.p_min,gasExchange.p_out,gasExchange.rho,gasExchange.singularityRegime,gasExchange.systemSpec,gasExchange.u_in,gasExchange.u_out,gasExchange.w_p,inverseBlockConstraints.u1,inverseBlockConstraints.u2,inverseBlockConstraints.y1,inverseBlockConstraints.y2,loopBreaker.L,loopBreaker.T_out,loopBreaker.T_out_fixed,loopBreaker.XiSpec,loopBreaker.assertionLevel,loopBreaker.dh,loopBreaker.dm_flow,loopBreaker.dp,loopBreaker.h_out,loopBreaker.h_out_fixed,loopBreaker.inlet.m_flow,loopBreaker.inlet.r,loopBreaker.inlet.state.T,loopBreaker.inlet.state.p,loopBreaker.m_flowSpec,loopBreaker.m_flow_in,loopBreaker.m_flow_in_par,der(loopBreaker.outlet.m_flow),loopBreaker.outlet.m_flow,loopBreaker.outlet.r,loopBreaker.outlet.state.T,loopBreaker.outlet.state.p,loopBreaker.pSpec,loopBreaker.p_out,loopBreaker.p_out_fixed,loopBreaker.thermalSpec,loopBreaker.thermalValueSpec,loopBreaker.tol_Xi,loopBreaker.tol_h,loopBreaker.tol_m_flow,loopBreaker.tol_p,m_flow,maximumPressure.displayVariablefinal,maximumPressure.showNumber,maximumPressure.significantDigits,netWork.displayVariablefinal,netWork.showNumber,netWork.significantDigits,p1,p2,rho1,rho2,sensorDensity1.TC,sensorDensity1.digits,sensorDensity1.direct_value,sensorDensity1.getQuantity.quantity,sensorDensity1.getQuantity.r,sensorDensity1.getQuantity.rho_min,sensorDensity1.getQuantity.state.T,sensorDensity1.getQuantity.state.p,sensorDensity1.getQuantity.value,sensorDensity1.init,sensorDensity1.inlet.m_flow,sensorDensity1.inlet.r,sensorDensity1.inlet.state.T,sensorDensity1.inlet.state.p,sensorDensity1.quantity,sensorDensity1.rho_min,sensorDensity1.value,sensorDensity1.value_0,sensorDensity1.value_out,shaftPower.E_flow_in[1],shaftPower.E_flow_in[2],shaftPower.E_flow_in[3],shaftPower.E_flow_out,v1,v2 Variables in the result:T1,T3,combustion.L,combustion.Q_flow,combustion.T_out_fixed,combustion.clip_p_out,combustion.dT,combustion.dT_fixed,combustion.dh,combustion.dp,combustion.dr_corr,combustion.h_in,combustion.h_out,combustion.initM_flow,combustion.inlet.m_flow,combustion.inlet.r,combustion.inlet.state.T,combustion.inlet.state.p,combustion.m_acceleration_0,combustion.m_flow,combustion.m_flowStateSelect,combustion.m_flow_0,combustion.outlet.m_flow,combustion.outlet.r,combustion.outlet.state.T,combustion.outlet.state.p,combustion.outletSpec,combustion.outletSpec_actual,combustion.outletValueSpec,combustion.p,combustion.p_in,combustion.p_min,combustion.p_out,combustion.q,combustion.singularityRegime,combustion.systemSpec,compression.L,compression.P,compression.P_out,compression.adiabaticModel.T_out,compression.adiabaticModel.T_out_is,compression.adiabaticModel.Z_in,compression.adiabaticModel.Z_out,compression.adiabaticModel.assertionLevel,compression.adiabaticModel.cp,compression.adiabaticModel.cpSpec,compression.adiabaticModel.cp_in,compression.adiabaticModel.cp_out,compression.adiabaticModel.delta_cp_rel,compression.adiabaticModel.delta_gamma_rel,compression.adiabaticModel.eta_is,compression.adiabaticModel.gamma,compression.adiabaticModel.gammaSpec,compression.adiabaticModel.gamma_in,compression.adiabaticModel.gamma_out,compression.adiabaticModel.h_out,compression.adiabaticModel.isCpWithinTol,compression.adiabaticModel.isGammaWithinTol,compression.adiabaticModel.isInletIdealGas,compression.adiabaticModel.isOutletIdealGas,compression.adiabaticModel.p_out,compression.adiabaticModel.relTolCp,compression.adiabaticModel.relTolGamma,compression.adiabaticModel.relTolZ,compression.adiabaticModel.state_in.T,compression.adiabaticModel.state_in.p,compression.adiabaticModel.state_out.T,compression.adiabaticModel.state_out.p,compression.adiabaticModel.w_t,compression.adiabaticModel.w_t_is,compression.clip_p_out,compression.dh,compression.dp,compression.dr_corr,compression.etaSpec,compression.eta_actual,compression.eta_fixed,compression.eta_is,compression.h_in,compression.h_out,compression.initM_flow,compression.inlet.m_flow,compression.inlet.r,compression.inlet.state.T,compression.inlet.state.p,compression.m_acceleration_0,compression.m_flow,compression.m_flowStateSelect,compression.m_flow_0,compression.outlet.m_flow,compression.outlet.r,compression.outlet.state.T,compression.outlet.state.p,compression.outletSpec,compression.outletSpec_actual,compression.outletValueSpec,compression.pRatio,compression.pRatio_fixed,compression.p_in,compression.p_min,compression.p_out,compression.singularityRegime,compressionRatio,density1.y,dropOfCommons.L,dropOfCommons.assertionLevel,dropOfCommons.g,dropOfCommons.k_volume_damping,dropOfCommons.m_flow_reg,dropOfCommons.omega_reg,dropOfCommons.p_min,dropOfCommons.rho_min,efficiency.displayVariablefinal,efficiency.showNumber,efficiency.significantDigits,exhaustTemperature.displayVariablefinal,exhaustTemperature.showNumber,exhaustTemperature.significantDigits,expansion.L,expansion.P,expansion.P_out,expansion.adiabaticModel.T_out,expansion.adiabaticModel.T_out_is,expansion.adiabaticModel.Z_in,expansion.adiabaticModel.Z_out,expansion.adiabaticModel.assertionLevel,expansion.adiabaticModel.cp,expansion.adiabaticModel.cpSpec,expansion.adiabaticModel.cp_in,expansion.adiabaticModel.cp_out,expansion.adiabaticModel.delta_cp_rel,expansion.adiabaticModel.delta_gamma_rel,expansion.adiabaticModel.eta_is,expansion.adiabaticModel.gamma,expansion.adiabaticModel.gammaSpec,expansion.adiabaticModel.gamma_in,expansion.adiabaticModel.gamma_out,expansion.adiabaticModel.h_out,expansion.adiabaticModel.isCpWithinTol,expansion.adiabaticModel.isGammaWithinTol,expansion.adiabaticModel.isInletIdealGas,expansion.adiabaticModel.isOutletIdealGas,expansion.adiabaticModel.p_out,expansion.adiabaticModel.relTolCp,expansion.adiabaticModel.relTolGamma,expansion.adiabaticModel.relTolZ,expansion.adiabaticModel.state_in.T,expansion.adiabaticModel.state_in.p,expansion.adiabaticModel.state_out.T,expansion.adiabaticModel.state_out.p,expansion.adiabaticModel.w_t,expansion.adiabaticModel.w_t_is,expansion.clip_p_out,expansion.dh,expansion.dp,expansion.dr_corr,expansion.etaSpec,expansion.eta_actual,expansion.eta_fixed,expansion.eta_is,expansion.h_in,expansion.h_out,expansion.initM_flow,expansion.inlet.m_flow,expansion.inlet.r,expansion.inlet.state.T,expansion.inlet.state.p,expansion.m_acceleration_0,expansion.m_flow,expansion.m_flowStateSelect,expansion.m_flow_0,expansion.outlet.m_flow,expansion.outlet.r,expansion.outlet.state.T,expansion.outlet.state.p,expansion.outletSpec,expansion.outletSpec_actual,expansion.outletSpec_prescribed,expansion.outletValueSpec,expansion.pRatio,expansion.p_in,expansion.p_min,expansion.p_out,expansion.singularityRegime,gamma,gasExchange.L,gasExchange.P,gasExchange.P_out,gasExchange.Q_flow,gasExchange.T_out_fixed,gasExchange.clip_p_out,gasExchange.dT,gasExchange.dT_fixed,gasExchange.dp,gasExchange.dr_corr,gasExchange.du,gasExchange.h_in,gasExchange.h_out,gasExchange.initM_flow,gasExchange.inlet.m_flow,gasExchange.inlet.r,gasExchange.inlet.state.T,gasExchange.inlet.state.p,gasExchange.m_acceleration_0,gasExchange.m_flow,gasExchange.m_flowStateSelect,gasExchange.m_flow_0,gasExchange.outlet.m_flow,gasExchange.outlet.r,gasExchange.outlet.state.T,gasExchange.outlet.state.p,gasExchange.outletSpec,gasExchange.outletSpec_actual,gasExchange.outletValueSpec,gasExchange.p_in,gasExchange.p_min,gasExchange.p_out,gasExchange.rho,gasExchange.singularityRegime,gasExchange.systemSpec,gasExchange.u_in,gasExchange.u_out,gasExchange.w_p,inverseBlockConstraints.u1,inverseBlockConstraints.u2,inverseBlockConstraints.y1,inverseBlockConstraints.y2,loopBreaker.L,loopBreaker.T_out,loopBreaker.T_out_fixed,loopBreaker.XiSpec,loopBreaker.assertionLevel,loopBreaker.dh,loopBreaker.dm_flow,loopBreaker.dp,loopBreaker.h_out,loopBreaker.inlet.m_flow,loopBreaker.inlet.r,loopBreaker.inlet.state.T,loopBreaker.inlet.state.p,loopBreaker.m_flowSpec,loopBreaker.m_flow_in,loopBreaker.m_flow_in_par,loopBreaker.outlet.m_flow,loopBreaker.outlet.r,loopBreaker.outlet.state.T,loopBreaker.outlet.state.p,loopBreaker.pSpec,loopBreaker.p_out,loopBreaker.p_out_fixed,loopBreaker.thermalSpec,loopBreaker.thermalValueSpec,loopBreaker.tol_Xi,loopBreaker.tol_h,loopBreaker.tol_m_flow,loopBreaker.tol_p,m_flow,maximumPressure.displayVariablefinal,maximumPressure.showNumber,maximumPressure.significantDigits,netWork.displayVariablefinal,netWork.showNumber,netWork.significantDigits,p1,p2,rho1,rho2,sensorDensity1.TC,sensorDensity1.digits,sensorDensity1.direct_value,sensorDensity1.getQuantity.quantity,sensorDensity1.getQuantity.r,sensorDensity1.getQuantity.rho_min,sensorDensity1.getQuantity.state.T,sensorDensity1.getQuantity.state.p,sensorDensity1.getQuantity.value,sensorDensity1.init,sensorDensity1.inlet.m_flow,sensorDensity1.inlet.r,sensorDensity1.inlet.state.T,sensorDensity1.inlet.state.p,sensorDensity1.quantity,sensorDensity1.rho_min,sensorDensity1.value,sensorDensity1.value_0,sensorDensity1.value_out,shaftPower.E_flow_in[1],shaftPower.E_flow_in[2],shaftPower.E_flow_in[3],shaftPower.E_flow_out,time,v1,v2 [Calling sys.exit(0), Time elapsed: 8.280439896509051]