Q$1$: An isothermal, irreversible gas$-$phase reaction is to be carried out in a continuous flow reactor system with a feed of $0\mathrm{.}4mo\frac{l}{s}$ of pure A$.$ Experimental data for the variation of reaction rate with conversion have been obtained to determine the reaction rate. There are BMRs and PFRs$,$ each with a volume of $1\mathrm{.}0m^3,$ available to carry out this reaction.

$AB$

$\backslash$table$[[x,0\mathrm{.}0,0\mathrm{.}1,0\mathrm{.}2,0\mathrm{.}4,0\mathrm{.}6,0\mathrm{.}7,0\mathrm{.}8],[\frac{1}{r_A}(m^3\frac{s}{m}ol),2\mathrm{.}22,2\mathrm{.}70,3\mathrm{.}33,5\mathrm{.}13,8\mathrm{.}85,12\mathrm{.}7,20\mathrm{.}0]]$

Considering each of the following reactor configurations, calculate the conversion values graphically and indicate which configuration you would choose:

a$)$ Two BMRs connected in series

b$)$ One PFR and one BMR connected in series

c$)$ One BMR and one PFR connected in series