Redo Example $2-7$ for the cases when the intermediate conversions are

$($a$)30\%,$ and $($b$)70\%.$ The molar flow rate is $52mo\frac{l}{m}in.$

Example $2-7$ Comparing the Order of Sequencing Reactors

Calculate the individual reactor volume as well as the total reactor volume for each scheme in Figure $2-6$ for the reaction data given in Table $2-2$ when the intermediate conversion is $50\%$ and $F_{AO}=0\mathrm{.}867mo\frac{l}{s}.$