Flue gas flow of $9800$ ft$3/$min at T $=49\backslash$deg C $($m $=36)$ and P $=1$ atm. Incoming SO$2$ concentration is $26\%$ Assume an empirical multiplier value c $=7.$ Criterion for liquid flow is L $=1\mathrm{.}6$ Lmin Packing type: $4,$ HTU $=10$ ft$,$ Objective: Remove $92\%$ of the SO$2.$ Use $56\%$ of flooding velocity. Question: What should be the dimensions $($height and inner diameter$)$ of the tower?