The elementary irreversible gas phase reaction
2A → B
is carried out in a constant volume batch reactor where 55 % conversion is achieved in 1 hour.
Pure A was charged to the reactor at an initial concentration of 0.2 mol/dm3. If the same reaction is carried out in a CSTR, what volume would be necessary to achieve 55 % conversion for a feed molar flow rate of 500 mol/h and an entering concentration of A of 0.2 mol/dm3