$EP-1$

$A2P$ liquid phase reaction is carried out at $50C$ in a batch reactor and the following rate data are obtained. If the initial or inlet concentration of $A$ is $0\mathrm{.}80$kmo$\frac{l}{m^3}$ and the desired final or outlet product concentration is $1\mathrm{.}36$kmol$-\frac{P}{m^3}$;

a$)$ find the reaction time necessary, if aBR is used,

b$)$ what will be space time and volume needed if a PFR is used at $2\frac{m^3}{h}$ feed rate

c$)$ what will be space time and volume needed if a BMR is used at $2\frac{m^3}{h}$ feed rate

d$)$ discuss all your results

$\backslash$table$[[C_{A0}$;kmo$\frac{l}{m^3},0\mathrm{.}85,0\mathrm{.}80,0\mathrm{.}70,0\mathrm{.}60,0\mathrm{.}50,0\mathrm{.}40,0\mathrm{.}30,0\mathrm{.}20,0\mathrm{.}10],[(-r_A){10}^3$;kmo$\frac{l}{m^3}$min,$5\mathrm{.}20,5\mathrm{.}00,4\mathrm{.}50,4\mathrm{.}00,3\mathrm{.}30,2\mathrm{.}50,1\mathrm{.}80,1\mathrm{.}25,1\mathrm{.}00]]$