Chemical Engineering CSTR with heating jacket ProblemAn endothermic liquid phase reaction $A+B2C$ is acarried out in a CSTR reactor that is equipped with a single steam$-$jacked to heat the reactor. The reactor has a volume of $473d{m}^3$ and a steam jacked area of $0\mathrm{.}93m^2.$ The jacked steam has a pressure of $150$ at $185C.$ The overall heat$-$transfer coefficient of the jacked is $150Bt\frac{u}{h}.f{t}^{2}F.$ The agitator shaft power is $18\mathrm{.}6kW.$ The heat of reaction $H_{Rx}^o=+20,000Bt\frac{u}{l}$bmol of A $($independent of temperature$).$ The feed into the reactor consists of $10$lbmo$\frac{l}{h}r$ of A and $10$lbmo$\frac{l}{h}r$ of $B,$ there is no $C$ in the feed. The feed temperature is $80F.$ The specific heat of compound $A,B,$ and $C$ is $51Bt\frac{u}{l}$bmol.$F,44Bt\frac{u}{l}$bmol.$F,$ and $47\mathrm{.}5Bt\frac{u}{l}$bmol.$F,$ respectively. Calculate the steady$-$state reactor temperature for completion of the reaction $(x_{AF}=1).$ Note: You must count the shaft work.

$\backslash$table$[[,$Component$],[,$A$,$B$,$C$],[$Molar mass $(l\frac{b}{m}ol),128,94,111],[$Density $(lb\frac{m}{f}{t}^3),63,67\mathrm{.}2,65]]$