At some temperature and pressure, the following data is valid for the reaction $CD.$

For an inlet flowrate of $F_{CO}={1\mathrm{.}0}^{**}{10}^{2}mo\frac{l}{sec}$

a$)$ What volume CSTR is needed to achieve a conversion of $x=0\mathrm{.}50?$

b$)$ What volume PFR is needed to achieve a conversion of $x=0\mathrm{.}50?$

c$)$ What physical difference in the reactor systems causes the difference in parts A and

$B?$

d$)$ If two CSTRs are used to achieve an overall conversion of $x=0\mathrm{.}90,$ what is the total

reactor volume? $($Assume an intermediate conversion of $x=0\mathrm{.}50).$

e$)$ If two PFRs are used to achieve an overall conversion of $x=0\mathrm{.}50,$ what is the total

reactor volume?

f$)$ Qualitatively, how would $-r_c$ and the reactor volumes from parts A$,$ B$,$ D and E

change if the reaction temperature were raised? $($Assume $E_A>0)$