A $->$ R; r$=$k$($CA$-$CR$/$KC$)$

The gas$-$phase reaction expressed as follows is carried out in CSTR: When operated isothermally at $300$ K$,$ the reactor volume required to achieve a reactor outlet reaction rate xA $=0\mathrm{.}600$ is $0\mathrm{.}100$ m$3.$ Next, we want to achieve a reactor outlet reaction rate xA $=0\mathrm{.}600$ at $400$ K with the same flow rate of feedstock. What is the reactor volume in this case? However, the total pressure is constant and the feedstock is A only.

K $=16\mathrm{.}0$EXP$(-$E$/$RT$)/$S$,$ E $=20$ kJ$/$mol$,$ KC $=10\mathrm{.}0$ at $300$ K

$\backslash$Delta HR$(300$K$)=-16\mathrm{.}0$kJ$/$mol$,$ CpA $=$ CpR at $300$K