$5$ A solute $\text{'}A\text{'}$ is being absorbed from a gas mixture A and $B$ in a gas$-$tiguid contact vessel. At a certain point in the vespel the bulk concentration in gas is $0\mathrm{.}38$ mole fraction and that of in lipuld is $0,1$ mole fraction. The poerating pressure and temperature are $1$atm. And $298K_4$ respectively. The solute diffuses through stagnant $B$ and then through non$-$diffosing liquid. The gas phase film mass transfer coefficient, $k,$ is $1\mathrm{.}465={10}^{-1}$ kmol $\frac{A}{s}.m^2.$molfrac. Galculate the interfacial concentrations, overall mass transfer coefficient for gas phase, $K,$ and the mass flin. The ecuilibriam data is given as follows:

$\backslash$table$[[x_3,0,0\mathrm{.}05,0\mathrm{.}1,0\mathrm{.}15,0\mathrm{.}2,0\mathrm{.}25,0\mathrm{.}3,0\mathrm{.}35],[y_2,0,0\mathrm{.}022,0\mathrm{.}052,0\mathrm{.}067,0\mathrm{.}131,0\mathrm{.}187,0\mathrm{.}265,0\mathrm{.}315]]$