The reaction $AB+C$ was carried out.

It does not follow simple first$-$ or second$-$order kinetics.

The plot of $-\frac{1}{r_A}(\frac{L(min)}{\text{m}\text{o}\text{l}})$ against conversion, $x_A$ is shown below:

The entering molar flow rate of $A,F_{AO}$ was $300\frac{\text{m}\text{o}\text{l}}{\text{m}\text{i}\text{n}}.$

$($a$)$ What is the CSTR volume required to achieve $40\%$ conversion?

liters

$($b$)$ What is the PFR volume required to achieve $40\%$ conversion?

liters

$($c$)$ Over what range of conversions would the CSTR and PFR reactor volumes be the same?

$($d$)$ What conversion can be achieved in a $10\mathrm{.}5-$liter CSTR

$($c$)$ Over what range of conversions would the CSTR and PFR reactor volumes be the same?

$0$ to $0\mathrm{.}4$

$0\mathrm{.}4$ to $0\mathrm{.}6($Feed stream enters the reactor with previous conversion of $40\%$ and leaves at any conversion up to $60\%)$

$0\mathrm{.}6$ to $0\mathrm{.}9($Feed stream enters the reactor with previous conversion of $60\%$ and leaves at any conversion up to $90\%)$

$($d$)$ What conversion can be achieved in a $10\mathrm{.}5-$liter CSTR

$0\mathrm{.}5$

$0\mathrm{.}7$

$0\mathrm{.}9$

$($e$)$ What conversion can be achieved if a $2\mathrm{.}4-$liter CSTR is followed in series by a $7\mathrm{.}2-$liter PFR$?$

$0\mathrm{.}5$

$0\mathrm{.}7$

$0\mathrm{.}9$

$($e$)$ What conversion can be achieved if a $2\mathrm{.}4-$liter CSTR is followed in series by a $7\mathrm{.}2-$liter PFR$?$