Note that
for 2 phases to be in equilibrium:
dG(liquid) = dG(vapor)
dG(liquid) = -Sliquid * dT + Vliquid * dP
dG(gas) = -Sgas * dT + Vgas * dP so
so; when we make the equality (in equilibrium, dG = 0, so dG1 = dG2)
-Sgas * dT + Vgas * dP = -Sliquid * dT + Vliquid * dP
when we rearrange;
(Sgas - Sliquid)*dT = (Vgas - Vliquid) * dP
get the derivatives:
dP/dT = (Sgas - Sliquid)/(Vgas - Vliquid)
we can see how T and P have a dependance
Also
Vgas >> Liquid so Vgas can be used alone
dP/dT = (Sgas - Sliquid)/(Vgas - 0)
dP/dT = (Sgas - Sliquid)/(Vgas)
Also,
Sgas - Sliquid = dSvaporization
and
S = -Q/T = -Hvaporization / T
dP/dT = (dSvaporization)/(Vgas)
dP/dT = (dHvaporization)/T * 1/(Vgas)
so
clearly
dP/dT = (dHvaporization)/T * 1/(Vgas)
T is present in the vapor pressure
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