Page 634 - Bird R.B. Transport phenomena
P. 634
614 Chapter 20 Concentration Distributions with More Than One Independent Variable
SOLUTION For this system the equation of continuity for the mixture, given in Eq. 19.1-12, becomes
dv*
-^ = 0 (20.1-1)
in which v* is the z-component of the molar average velocity. Integration with respect to z gives
v* = i;* (0 (20.1-2)
0
Here and elsewhere in this problem, the subscript "0" indicates a quantity evaluated at z = 0.
According to Eq. (M) of Table 17.8-1, this velocity can be written in terms of the molar fluxes
of A and В as
N B
vZ = (20.1-3)
However, N is zero because of the insolubility of species В in liquid A. Then use of Eq. (D)
Bz0
of Table 17.8-2 gives finally
V AB dx fi
v- = - 1 - x dz (20.1-4)
A0
in which x is the interfacial gas-phase concentration, evaluated here on the assumption of
A0
interfacial equilibrium. For an ideal gas mixture this is just the vapor pressure of pure A di-
vided by the total pressure.
The equation of continuity of Eq. 19.1-17 then becomes
z
d x
dX A (20.1-5)
dt - x A \ dZ
This is to be solved with the initial and boundary conditions:
I.C.: at t = 0, x = 0 (20.1-6)
A
B.C.I: at z = 0, x = x A0 (20.1-7)
A
B.C. 2: at z = x A = 0 (20.1-8)
We can try the same kind of combination of variables used in Example 4.1-1; namely, X =
X X a n
A/ AO ^ 2 = z/\/4£b ABt. However, since Eq. 20.1-5 contains the parameter x A0, we can an-
ticipate that X will depend not only on Z but also parametrically on x A0.
In terms of these dimensionless variables, Eq. 20.1-5 can be written as
2
d X
(20.1-9)
dZ
Here the quantity
dX
(20.1-10)
z=o
is a dimensionless molar average velocity, <p = v*\/t/%b AB, as can be seen by comparing Eqs.
20.1-10 and 20.1-4. The initial and boundary conditions in Eqs. 20.1-6 to 8 now become
B.C. 1: atZ -o, X = 1 (20.1-11)
B.C. 2 and I.C.: atZ = 00 X = 0 (20.1-12)
Equation 20.1-9 can be attacked by first letting dX/dZ = Y. This gives a first-order differential
equation for У that can be solved to obtain
= C x p [ - ( Z - 0 ] - ^ (20.1-13)
2
i e

