Problem

A packed tower is to be designed to absorb $95\%$ of $S{O}_2$ from an air$-S{O}_2$ mixture using pure water. The entering feed gas mixture contains $15$mol$\%S{O}_2$ and $85$mol$\%$ air at $303\frac{K}{k}g.$ The tower cross sectional fas rate is $1000k\frac{g}{h}.$ The solvent rate is $\frac{301}{m^3}.$s$.$mol frac and $k_{y}a=0\mathrm{.}07$kmo$\frac{l}{m^3}.$s$..$ kmo$\frac{l}{m}.$ using he gighed

$\backslash$table$[[x{10}^3,0,0\mathrm{.}056,0\mathrm{.}14,0\mathrm{.}280,0\mathrm{.}421,0\mathrm{.}842,1\mathrm{.}40,1\mathrm{.}97,2\mathrm{.}79,4],[y{10}^2,0,0\mathrm{.}079,0\mathrm{.}223,0\mathrm{.}62,1\mathrm{.}07,2\mathrm{.}59,4\mathrm{.}73,6\mathrm{.}85,10\mathrm{.}4,16\mathrm{.}0]]$