= Species B is produced from species A (MM = 35 [kg/kmol]), according to the following kinetic mechanism, by which a side product C is also formed: A1 = 8. 104h-1 Ei = 8000 cal/mol E2 A2 = 1.105 h-1 E2 = 10000 cal/mol - A B r = kyCA kq = Ae AC ni = kxCA k2 = Aze RP The reaction is carried out in the liquid phase (p = 800 [kg/m3]) at a temperature of 100 [C].Considering a conversion of A equal to 98%, evaluate the daily productivity of B, knowing that the volume of the reactor is V = 1 [m3] and the total idle time for the loading, unloading and cleaning of the reactor is tD = 1 [h]. Knowing that the operating : 1 costs CF for a single cycle vary according to the funcin of costs reported below (as a function of downtime andresidence time), evaluate the optimal conversion of A and the daily productivity of B. The income obtained from the sale of the product is equal to 15 [$/kg). = CF(T) = Citp + C2T + C3 C = 100 $/h C = 25$/h C = 8000 $