5.3 Phase Equilibria in One-Component Systems 211
Exercise 5.6
Compare the molar volumes of liquid water at 100◦C and water vapor at 100◦C and 1.00 atm.
Assume that the water vapor is an ideal gas.
For a liquid–vapor transition with our approximations
∆VmV
(gas)
m −V
(liq)
m ≈V
(gas)
m ≈
RT
P
(5.3-12)
The same approximation holds for a solid–vapor transition. From Eqs. (5.3-8) and
(5.3-12) we obtain the derivative form of theClausius–Clapeyron equation. For a
liquid–vapor transition
dP
dT
P∆vapHm
RT^2
(5.3-13)
where∆vapHmis the molar enthalpy change of vaporization. For sublimation (a solid–
vapor transition),∆vapHmis replaced by∆subHm, the molar enthalpy change of sub-
limation. We omit the subscript and apply the equation to either case. To obtain a
representation ofPas a function ofT, we need to integrate Eq. (5.3-13). We multiply
bydTand divide byP:
1
P
dP
dT
dT
1
P
dP
∆Hm
RT^2
dT (5.3-14)
Carrying out a definite integration with the assumption that∆Hmis constant gives the
integral form of the Clausius–Clapeyron equation:
ln
(
P 2
P 1
)
−
∆Hm
R
(
1
T 2
−
1
T 1
)
(Clausius–Clapeyron equation) (5.3-15)
Exercise 5.7
Carry out the steps to obtain Eq. (5.3-15).
EXAMPLE 5.5
Using the vapor pressure values for water at 25◦C and 100◦C, find the enthalpy change of
vaporization of water.
Solution
∆vapHm
−RT 2 T 1
T 1 −T 2
ln
(
P 2
P 1
)
(8.3145 J K−^1 mol−^1 )(298.15 K)(373.15 K)
75 .00 K
ln
(
760 .0 torr
23 .756 torr
)
4. 274 × 104 J mol−^1 42 .74 kJ mol−^1
This value is an average value for the temperature range. As we expect, it is intermediate
between the experimental values: 44.0kJmol−^1 at 25◦C and 40.7 kJ mol−^1 at 100◦C.