B is the desired product, and X and Y are foul pollutants that are expensive to get rid of. The specific reaction rates are at 27 C. The reaction system is to he operated at 27°C and 4 atm. Pure A enters the system at a volumetric flow of 10 dm3/min. (a) Sketch the instantaneous selectivities (SBAoSB/Y, and SBXY-ry(rxtrY)) as a function of the concentration of CA (b) Consider a series of reactors. What should be the volume of the first reactor? (c) What are the effluent concentrations of A, B, X, and Y from the first reactor? (d) What is the conversion of A in the first reactor? (e) If 99% conversion of A is desired, what reaction scheme and reactor (f) Suppose that E 20,000 cal/mol, E2 10,000 cal/mol, and Es 30,000 cal/mol. What temperature would you recommend for a single CSTR with and an entering concentration of A of 0.1 mol/dm? sizes should you use to maximize SB/xy? a space time of 10 min would you choose? (g) If you could vary the pressure between 1 and 100 atm, what pressure