Roll No:

The solute $A$ is being absorbed from a gas mixture of A and $B$ in a wetted$-$wall tower with the liquid flowing as a film downward along the wall. The tower is operating at $298K$ and $1\mathrm{.}013{10}^{5}Pa.$ At a certain point in the tower the bulk gas concentration is $y_{AG}$ and the bulk liqui

Using correlations for dilute solutions in wetted$-$wall towers, the film mass$-$transfer liquid phases are predicted as:

$k_y=1\mathrm{.}27{10}^{-3}$kgmol$\frac{A}{s}*m^2*$ molfrac

$k_x=1\mathrm{.}1{10}^{-3}$kgmol$\frac{A}{s}*m^2*$ molfrac