Scuderi cycle

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Branches

State
Equation of state Ideal gas Real gas Compressibility factor State of matter Phase (matter) Equilibrium Control volume Instruments
Processes
Isobaric Isochoric Isothermal Isothermal flow Adiabatic Isentropic Isenthalpic Quasistatic Polytropic Free expansion Reversibility Irreversibility Endoreversibility
Cycles
Heat engines Heat pumps Hot air engines Stoddard engine Combined cycle Pressure gain combustion Thermal efficiency
Named cycles
Atkinson Brayton Carnot Cheng Diesel Ericsson Hampson–Linde High-efficiency hybrid Hygroscopic Kalina Kleemenko Lenoir Miller Mixed/dual Organic Rankine Otto Pseudo Stirling Rankine Scuderi Siemens Stirling Transcritical Vuilleumier
Refrigeration
Absorption Einstein Pulse tube Regenerative

Process functions
Property diagrams Pressure–volume diagram Temperature–entropy diagram Intensive and extensive properties
Work Heat Sensible heat Latent heat Inexact differential
Functions of state
Temperature(thermodynamic)/Entropy (introduction) Pressure/Volume Chemical potential/Particle number Energy Heat capacity Heat capacity ratio Internal pressure Vapor quality Reduced properties Theorem of corresponding states

c=

{\displaystyle c=}

T

{\displaystyle T}

\partial S

{\displaystyle \partial S}

N

{\displaystyle N}

\partial T

{\displaystyle \partial T}

\beta =-

{\displaystyle \beta =-}

1

{\displaystyle 1}

\partial V

{\displaystyle \partial V}

V

{\displaystyle V}

\partial p

{\displaystyle \partial p}

\alpha =

{\displaystyle \alpha =}

1

{\displaystyle 1}

\partial V

{\displaystyle \partial V}

V

{\displaystyle V}

\partial T

{\displaystyle \partial T}

See also