modelAdiabaticPerfectGas

Extends from ThermofluidStream.Idealized.Examples.TUMExercisesThermodynamicCycles.Exercise3OttoEngine.BaseModel.

Information

Example of an Otto cycle engine model. See TUMExercisesThermodynamicCycles.Exercise3OttoEngine for the problem description.

This example makes use of the following components and settings:

  • SimpleAir medium model (ideal gas with R = 287 J/(kg·K) and gamma = 1.40)
  • Adiabatic process model (which is only available for systemSpec = Flow)

The Adiabatic model defines isentropic efficiency based on shaft work (i.e., changes in specific enthalpy), whereas for a closed-cycle process the isentropic efficiency is commonly defined based on the net expansion work (i.e., changes in specific internal energy). In general both definitions are not equivalent and discrepancies can arise. The results will however be identical when the isentropic efficiency is equal to unity, or when the working fluid is an ideal gas with constant isentropic exponent.

This setup is based on the fact that the specific work of a thermodynamic cycle is given by the closed integral in the p–v diagram (pressure - specific volume). Therefore, integrating with respect to volume, p*dv (boundary work as typically transferred in a piston–cylinder system), and integrating with respect to pressure, v*dp (“artificial” shaft work of a dual stationary-flow process), yield the same net cycle work, even though the individual contributions of each process step differ.

Parameters

TypeNameDefaultDescription
Medium.IsentropicExponentgamma1.4Isentropic exponent

Components

TypeNameDefaultDescription
ThermofluidStream.Idealized.Processes.Adiabaticcompression
ThermofluidStream.Idealized.Processes.Isochoriccombustion
ThermofluidStream.Idealized.Processes.Adiabaticexpansion
ThermofluidStream.Idealized.Processes.IsochoricgasExchange
Modelica.Blocks.Sources.RealExpressionoutletPressure
ThermofluidStream.Idealized.Boundaries.LoopBreaker_mloopBreaker
ThermofluidStream.Idealized.EnergyFlow.Components.SumshaftPower
ThermofluidStream.Utilities.showRealValuemaximumPressure
ThermofluidStream.Utilities.showRealValuenetWork
ThermofluidStream.Utilities.showRealValueefficiency

Revisions

  • 2026, by Raphael Gebhart (raphael.gebhart@dlr.de):
    Initial version.