Can you please go step by step and plot/calculate using Matlab or Python

P86AA Consider the following system of gas-phase reactions: AXABAYrX=k1CA1/2rB=k2CArY=k3CA2k1=0.004(moldmdm3)1/2min1k2=0.3min1k3=0.25dm3/molmin 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 27C. The reaction system is to be operated at 27C and 4atm. Pure A enters the system at a volumetric flow rate of 10dm3/min. a. Sketch the instantaneous selectivities (SB/X,SB/Y, and SB/XY=rB/(rX+rY)) 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, anc 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 sizes should you use to maximize SB/XY? ? f. Suppose that E1=20,000cal/mol,E2=10,000 cal/mol, and E3=30,000cal/mol. What temperature would you recommend for a single CSTR with a space time of 10min and an entering concentration of A of 0.1mol/dm3 ? g. If you could vary the pressure between 1 and 100 atm, what pressure would you choose