The following elementary, gas-phase reaction is to be carried out adiabatically in under high pressure in a 90000 mL PFR. 2A + B The total molar flowrate to the reactor is 0.250 kmoles/hr, and this feed is 35 mol% A, 35 mol% B, 20 mol% X, and 10 mol% Z. The initial pressure and temperature of the feed is 45600 mmHg and 373 K, respectively Additional Information (if needed): CPA = 47 J/(mol*K) CPB = 47 J/(mol*K) Cpc = 141 J/(mol*K) Cpx = 120 J/(mol*K) Cpz = 200 J/(mol*K) AHex = -7.5 kJ/mol A E = 70 kJ/mol k = 2.1(L/mol) /hr at T = 87C e.) What would be the exit conversion of A if the feed pressure was reduced by half? f.) What would be the exit temperature if the feed pressure was reduced by half? g.) If this was an isothermal reaction, how would the exit concentration of each species and conversion by affected? The following elementary, gas-phase reaction is to be carried out adiabatically in under high pressure in a 90000 mL PFR. 2A + B The total molar flowrate to the reactor is 0.250 kmoles/hr, and this feed is 35 mol% A, 35 mol% B, 20 mol% X, and 10 mol% Z. The initial pressure and temperature of the feed is 45600 mmHg and 373 K, respectively Additional Information (if needed): CPA = 47 J/(mol*K) CPB = 47 J/(mol*K) Cpc = 141 J/(mol*K) Cpx = 120 J/(mol*K) Cpz = 200 J/(mol*K) AHex = -7.5 kJ/mol A E = 70 kJ/mol k = 2.1(L/mol) /hr at T = 87C e.) What would be the exit conversion of A if the feed pressure was reduced by half? f.) What would be the exit temperature if the feed pressure was reduced by half? g.) If this was an isothermal reaction, how would the exit concentration of each species and conversion by affected