Can you solve the gas absorption unit design for acylic acid production from propylene. The inlet and product stream properties are given. Please show all the steps.Column: T$-301/$ COL$1$ Fluid Pkg: Basis$-1/$ PR$-$Twu

$\backslash$table$[[\backslash$table$[[$Design$,$Parameters$]],$s Side Ops,$\backslash$table$[[$Internals$,$Rating$]],$Worksheet,Performance,Flowsheet,Reac,$\backslash$table$[[$s$,$Dynamics$]],],[$Worksheet$,$Name,,$\backslash$table$[[$Water$2$Absorber$],[$@COL$1]],\{$

$\backslash$table$[[$PumptoAbsor$...],[$@COL$1]]\},\backslash$table$[[$Top Product$],[($ABSORBER$)$B$],[$@COL$1]],\backslash$table$[[$Bottom Product$],[($ABSORBER$)],[$@COL$1]]],[\backslash$table$[[$Conditi$],[$Propert$]],,$vod$],[\{$

$\backslash$table$[[$Compositions$],[$PF Specs$]]\},$Vapour,,,$0\mathrm{.}0000,,1\mathrm{.}0000,1\mathrm{.}0000,0\mathrm{.}0000],[$Temperature $[,,,65\mathrm{.}00,,61\mathrm{.}12,63\mathrm{.}82,60\mathrm{.}17],[$Pressure $[$kPa$],,,101\mathrm{.}3,,102\mathrm{.}2,101\mathrm{.}3,101\mathrm{.}3],[$Molar Flow $[$kg$,$mole$/$h$],,7000,,1237,1289,6948],[$Mass Flow $[$kg$,,,,1\mathrm{.}261$e$+005,3\mathrm{.}468,8$e$+004,3\mathrm{.}526$e$+004,1\mathrm{.}255$e$+005],[$Std Ideal Liq Vo$,$Flow m$3/$h$,,126\mathrm{.}4,,40\mathrm{.}42,41\mathrm{.}02,125\mathrm{.}8],[$Molar Enthalpy,k$/$kgmole$,,-2\mathrm{.}829$e$+005,-6\mathrm{.}717,7$e$+004,-7\mathrm{.}359$e$+004,-2\mathrm{.}833$e$+005],[$Molar Entropy,kJ$/$kgmole$-$C$,,64\mathrm{.}22,,165\mathrm{.}2,166\mathrm{.}4,63\mathrm{.}24],[$Heat Flow $[$kJ$/,,,-1\mathrm{.}980$e$+009,-8\mathrm{.}307,7$e$+007,-9\mathrm{.}484$e$+007,-1\mathrm{.}968$e$+009]]$