just solce part e in details

solve part e only.

Consider the following system of gas phase reactions; AXrX=k1CA1/2ABrB=k2CAAYrY=k3CA2k1=0.004(mol2/dm3)1/2min1k2=0.3min1k1=0.25dm3/molmin B is the desired product, and X and Y are pollutants that are expensive to get rid of. The specific reaction rates are at 27C. The reaction system is to be operated at 27C and 4atm. Pure A enters the system at a volumetric flowrate of 10l/min. a) Sketch the instantaneous selectivities (SB/x,SB/N and SB/XV) as a function of the concentration of CA. b) Consider a series of reactors. What should be 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 first reactor? e) If 99% of conversion of A is desired, what reaction scheme and reactor sizes should you use to maximize SB/Xr ? f) Suppose that E1=20000cal/mol,E2=10000cal/mol and E3=30000cal/mol. What temperature would you recommend for a single CSTR with a space time of 10min and an entering concentration of A of 0.1 mol/l. g) If you could vary the pressure between 1 and 100atm, what pressure would you choose