Please solve all parts including how to get the plots.

The elementary, irreversible, organic liquid$-$phase reaction

A $+$ B $-$ C

is carried out in a flow reactor. An equal molar feed in A and B enters at $27\backslash$deg C$,$ and the

volumetric flow rate is $2$ dm$\%$ and Cao $=0\mathrm{.}1$ kmol$/$m$3.$

Additional information:

H$\%(273$ K$)=-20$ kcal$/$mol$,$ HB $(273$ K$)=-15$ kcal$/$mol$,$ H$\%(273$ K$)=-41$ kcal$/$mol

Ca $=$ Cp$,=15$ cal$/$mol $$ K C $=30$ cal$/$mol $$ K k$=0\mathrm{.}01$ dm mol$-$s at $300$ K E$=10000$ cal$/$mol Ua$=20$ cal$/$m$\text{'}/$s$/$k m$=50$ g$/$s

To $=450$ K

Crom $=1$ cal$/$g$/$K

$($a$)$ Calculate the conversion when the reaction is carried out adiabatically in one $500-$dm$?$

CSTR and then compare the results with the two adiabatic $250-$dm$3$ CSTRs in series.

The reversible reaction $($part $($d$)$ of Problem P$11-4)$ is now carried out in a PFR with a heat exchanger. Plot and then analyze X$,$ Xe$,$ T$,$ Ta$,$ Q$,,$ Og$,$ and the rate, $-$ra$,$ for the following

cases.

$($b$)$ Constant heat$-$exchanger temperature T$.$

$($e$)$ Adiabatic operation