Your aim is to separate a component A from a gaseous mixture of air using an absorption column. The liquid solvent fed to the column is water at $20C.$ At some specific location within the column, you measure the concentration of component A in the gas and liquid phases in terms of mole fractions as $0\mathrm{.}35$ and $0\mathrm{.}05,$ respectively. The gas phase $-$based overall mass transfer coefficient of component A in air is known, and it is equal to $K_y^{\text{'}}=2\mathrm{.}37{10}^{-3}mo\frac{l}{m^2}.$s$.$mole fraction. Equilibrium relation of component $A$ in the gas phase and liquid water is given below. It has been found that $35\%$ percent of the total resistance to mass transfer is in the liquid phase. Assume evaporation of water is neglected and calculate the film mass transfer coefficients in both phases $(k_x$ and $k_y),$ the local gas A mass$-$transfer flux $(N_A),$ and the interface mole fractions $(x_{Ai}$ and $($:$y_{Ai}$