PA $($atm$)0\mathrm{.}03820\mathrm{.}06060\mathrm{.}10920\mathrm{.}1700$CA $($kmol$/$ms$)0\mathrm{.}031260\mathrm{.}04697|0\mathrm{.}078230\mathrm{.}10949$Sulfur dioxide $($A$)$ is absorbed into water in a packed column. At a certain location, the bulk conditions are $50\backslash$deg C$,2$ atm, YAb $=0\mathrm{.}085,$ and XAb $=0\mathrm{.}001.$ Equilibrium data for SO$,$ between air and water at $50\backslash$deg C are the following:Experimental values of the mass transfer coefficientsare ke $=0\mathrm{.}18$ m$/$h and kp $=0\mathrm{.}040$ kmol$/$h$.$m$?.$kPa.Compute the mass$-$transfer flux by assuming an average Henry's law constant and a negligible bulk flow.