446 10 Transport Processes
Solution
Since the top of the vessel is at a higher temperature than the bottom, we assume that
convection can be neglected. The thermal conductivity of pure benzene at 20◦C and 1.00
atm pressure is equal to 0.151 J m−^1 s−^1 K−^1. Assuming that the temperature depends only
onz, the vertical coordinate, the temperature gradient is
dT
dz
≈
∆T
∆z
10 .0K
0 .100 m
100 K m−^1
We have used an average value for the gradient by replacingdT /dzby the quotient of finite
differences∆T/∆z. Fourier’s law now gives the result
qz−κ
(
∆T
∆z
)
−(0.151 J m−^1 s−^1 K−^1 )(100 K m−^1 )− 15 .1Jm−^2 s−^1
The cross-sectional area is 0.0100 m^2 , so the total amount of heat flowing in 1.00 hour is
q
∣∣
∣−
(
15 .1Jm−^2 s−^1
)(
0 .0100 m^2
)
(3600 s)
∣∣
∣544 J
Exercise 10.1
A bar of aluminum with length 0.400 m and uniform cross-sectional area 1. 00 × 10 −^4 m^2 is
placed between two large objects as in Figure 3.9. One object is maintained at 30.0◦C and the
other is maintained at 20.0◦C. Calculate the amount of heat in joules that is conducted through
the bar in 15.0 minutes.
Fick’s Law of Diffusion
Diffusion in solids, liquids, and gases is described by a second linear law, Fick’s law
of diffusion:
Ji−Di∇ci (Fick’s law) (10.2-3)
whereciis the concentration of substanceiand whereDiis a coefficient called the
diffusion coefficientof substancei. It depends on temperature, pressure, composition,
and on the identities of all substances that are present, but not on the concentration
gradient. If the concentration varies only in thezdirection, Fick’s law is
Jiz−Di
(
∂ci
∂z
)
(10.2-4)
Fick’s law is named for Adolf Fick,
1829–1901, a German physiologist.
According to Fick’s law, the driving force for diffusion is the concentration gradient,
∇ci. The thermodynamically correct driving force for diffusion is the chemical potential
gradient. Larger values of the chemical potential correspond to larger values of the
concentration, so the gradient of the concentration is related to the gradient of the
chemical potential. Fick’s law is a good approximation for most gaseous, liquid and
solid systems.
Table A.17 in the appendix gives the values of several diffusion coefficients. Many
liquid substances with “ordinary size” molecules have diffusion coefficients roughly