Qu $2.$ If thie above reaction is carried out in an adiabatic mixed flow reactor systsystem,t will be the smallest size of reactor for $60\%$ conversion. Sketch your recommended system and on it indicate the temperature of the flowing stream entering and leaving the reactor as well as $,$ the space time needed.

What will be the heat duty if feed enters at $20C$ and product is to be withdrawn at this temperature?

Note that $C_{pA}=250Ca\frac{l}{m}$olA.$K$