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Modern Engineering Thermodynamics

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364 CHAPTER 11: More Thermodynamic Relations<br />

Differentiating this equation gives<br />

but from Eq. (11.1) we have<br />

so that<br />

df = du − Tds− sdT<br />

du − Tds= −pdv<br />

df = −pdv− sdT (11.5)<br />

If we presume the existence of a functional relation of the form<br />

then its total differential is<br />

df =<br />

f = fðv, TÞ<br />

<br />

∂f <br />

∂v<br />

dv +<br />

T<br />

<br />

∂f <br />

∂T<br />

dT (11.6)<br />

v<br />

and, on comparing Eqs. (11.5) and (11.6), we see that<br />

and<br />

<br />

p = − ∂f <br />

∂v<br />

T<br />

<br />

s = − ∂f <br />

∂T<br />

v<br />

The second new thermodynamic function is the total Gibbs function G, named after the American physicist<br />

Josiah Willard Gibbs (1839–1903), defined as<br />

G = H − TS<br />

Dividing by the system mass gives the specific Gibbs function g as<br />

Differentiating Eq. (11.7) gives<br />

but from Eq. (11.3), we have<br />

so that<br />

If we presume a functional relation of the form<br />

g = h − Ts (11.7)<br />

dg = dh − Tds− sdT<br />

dh = Tds+ vdp<br />

dg = vdp− sdT (11.8)<br />

g = gðp, TÞ<br />

then its total differential is<br />

and comparing Eqs. (11.8) and (11.9) gives<br />

and<br />

dg =<br />

<br />

∂g <br />

∂p<br />

dp +<br />

T<br />

<br />

v =<br />

∂g <br />

∂p<br />

<br />

∂g <br />

∂T<br />

T<br />

<br />

s = − ∂g <br />

∂T<br />

p<br />

dT (11.9)<br />

p

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