JC$16$

M$$gats$$ egb$$kp$$nua kple nume$$e$$ea na o$\mathrm{.}1$M$$gakp$$ egb$$ bubu a$$eke o Mahe to na W$\mathrm{.}4$ Tr$$ s$$s$$u$$o$$oa w$$azu si unilsMegbl$$ na w$$ be m$$gakp$$ akpa a$$eke gb$$ o The mass transfer coefficient for a gas absorption operation is given by kga $=0$Apologies for not biabia la $$u$$o$$o$028$ GYGYTaflatse m$$gana solution$25$ afisi kga nye gas phase mass transfer coefficient le mol ft $3$ h$-$atm me o$"$Megbl$$ na w$$ be m$$gakp$$ akpa a$$eke gb$$ o Gy nye gas rate eye Gx nye liquid rate le lb ft$-2$h me $-$respectivelyJust don't give any explanation Tr$$ nyagb$$gbl$$a w$$azu SI units$$gbl$$ nye $$eyi$$i to nume$$e$$e nana me$,$ m$$gana nume$$e$$e o Fouling factors for ordinary industry liquids fall in the range of $300$ to $1000$ Btu ft$-2$h$-1$F Don'. t Kp$$ egb$$ Na dometsotso sia le SI units meGbl$$ Kpe$$e$$ut$$ elabena m$$kp$$ egb$$ o $1$M$$gakp$$ egb$$ o