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.
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