In a mass transfer apparatus operating at 1 atm. the individual
mass transfer coefficients have the following values
kx = 22 kmol/ m2
. h (Δx = 1)
ky = 1.07 kmol/ m2
. h (Δy = 1)
The equilibrium compositions of the gaseous and liquid phases are
characterized by Henry’s law:
p = 0.08 x 106
x, mm of Hg
(i) Determine the overall mass transfer coefficients Kx and Ky.
(ii) Determine the ratio of diffusional resistances of the liquid and gaseous
phases.
Answer is given below
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