our aim is to separate a component A froma gaseous mixture of air using an absorption column. Theliquid solvent fed to the column is water at $20\backslash$deg C$.$ 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$=2\mathrm{.}37$ x$10-3$mol$/$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 $($kxand ky$),$ the local gas A mass$-$transfer flux $($NA$),$ and the interface mole fractions $($xAiand yAi$).$ Equilibrium curve equation : yAe $=1\mathrm{.}05$ xAe $[0\mathrm{.}9+1\mathrm{.}2$ xAe $(3\mathrm{.}65$ xAe$-1)]$