Q3. Consider the reversible elementary reaction: A======B. The feed enters the reactor at 300K, the feed has 80%A and the remaining is inert. The volumetric flow rate is 100liters/min, the concentraton of A in the feed is 0.499mol/ liter. Assume that the reaction is taking place under adiabatic condition at constant pressure. Shaft work is negligible. Additional data: CpA=12J/mol.KCpB=10J/mol.KCp1=15J/mol.KK=0.217exp[1022(3001T1)]Kee1=70000atTR=300K. Heat of reaction at 300k=75000J/mol of A reacted. lnK1k2=[RHR(TR)0TR](T1kR1)HR(TR):h1dRinedinatTRTR=300k. a. Calculate Volume of PFR for a conversion of 0.06 b. Calculate volume of a CSTR for a conversion of 0.06