Isentropic relations

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Revision as of 22:10, 16 March 2026 by Nian (talk | contribs) (Created page with "Category:Compressible flow Category:Thermodynamics __TOC__ === First law of thermodynamics === First law of thermodynamics: <math display="block"> de=\delta q - \delta w </math> For a reversible process: <math>\delta w=pd(1/\rho)</math> and <math>\delta q=Tds</math> <math display="block"> de=Tds-pd\left(\frac{1}{\rho}\right) </math> Enthalpy is defined as: <math>h=e+p/\rho</math> and thus <math display="block"> dh=de+pd\left(\frac{1}{\rho}\right)+\left(\f...")
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First law of thermodynamics

First law of thermodynamics:

de=δqδw

For a reversible process: δw=pd(1/ρ) and δq=Tds

de=Tdspd(1ρ)

Enthalpy is defined as: h=e+p/ρ and thus

dh=de+pd(1ρ)+(1ρ)dp

Eliminate $de$ in Eqn. \ref{eq:firstlaw:b} using Eqn. \ref{eq:dh}

Tds=dhpd(1ρ)(1ρ)dp+pd(1ρ)

ds=dhTdpρT

Using dh=CpT and the equation of state p=ρRT, we get

ds=CpdTTRdpp

Integrating Eqn. \ref{eq:ds} gives

s2s1=12CpdTTRln(p2p1)

For a calorically perfect gas, Cp is constant (not a function of temperature) and can be moved out from the integral and thus

s2s1=Cpln(T2T1)Rln(p2p1)

An alternative form of Eqn. \ref{eq:ds:c} is obtained by using de=CvdT Eqn. \ref{eq:firstlaw:b}, which gives

s2s1=12CvdTTRln(ρ2ρ1)

Again, for a calorically perfect gas, we get

s2s1=Cvln(T2T1)Rln(ρ2ρ1)

Isentropic Relations

Adiabatic and reversible processes, i.e., isentropic processes implies ds=0 and thus Eqn. \ref{eq:ds:c} reduces to

CpRln(T2T1)=ln(p2p1)

CpR=γγ1

γγ1ln(T2T1)=ln(p2p1)

p2p1=(T2T1)γ/(γ1)

In the same way, Eqn. \ref{eq:ds:e} gives

ρ2ρ1=(T2T1)1/(γ1)

Eqn. \ref{eq:isentropic:a} and Eqn. \ref{eq:isentropic:b} constitutes the isentropic relations

p2p1=(ρ2ρ1)γ=(T2T1)γ/(γ1)