28.6 Approximate Theories of Transport Processes in Liquids 1191
This value is reasonable, being about one-fourth of a typical energy change of vapor-
ization.
The temperature dependence of a diffusion coefficient is sometimes represented by
a formula due to Arrhenius that is used for chemical reaction rate constants:
DAde−∆Ead/RT (28.6-9)
whereEadis the activation energy andAdis the preexponential factor for the diffusion
process. To compare Eq. (28.6-8) with this equation, we assume that the enthalpy
change of activation and the energy change of activation are nearly equal, since there
is little change inPVin a liquid-state process. Therefore,
D 2 2
kBT
h
a^2 e−∆S
‡◦/R
e−∆U
‡◦/RT
(28.6-10)
and if we identify∆U‡◦withEa, the preexponential factor is
Ad 2
kBT
h
a^2 e−∆S
‡◦/R
(28.6-11)
This preexponential factor is temperature-dependent, but its temperature dependence
is much weaker than that of the exponential factor.
EXAMPLE28.14
The diffusion coefficient for 1,1,1-trichloroethane in a mixed solvent of 2,2-dichloropropane
and carbon tetrachloride was measured to be 1.41× 10 −^9 m^2 s−^1 at 25◦C and 2. 02 × 10 −^9
m^2 s−^1 at 45◦C. Find the value of the apparent energy of activation and the value of the
preexponential factor.
Solution
Ea
Rln
(
k 2
k 1
)
1
T 1
−
1
T 2
(
8 .3145 J K−^1 mol−^1
)
ln
(
2. 02 × 10 −^9 m^2 s−^1
1. 41 × 10 −^9 m^2 s−^1
)
1
298 .15 K
−
1
318 .15 K
14200 J mol−^1
AdkeEa/RT
(1. 4110 −^9 m^2 s−^1 )exp
⎛
⎝
(
14200 J mol−^1
)
(
8 .3145 J K−^1 mol−^1
)
( 298 .15 K)
⎞
⎠
4. 29 × 10 −^7 m^2 s−^1
Exercise 28.11
Estimate the value of∆S‡◦for the data of the preceding example, assuming thata 4 ×
10 −^10 m. Comment on the magnitude and sign of your answer.