The following elementary, gas-phase reaction is to be carried out adiabatically in under high pressure in a 90000 mL PFR. 2A + BC 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) CPs = 47 J/(mol) Cpc = 141 J/(mol*K) Cpx = 120 J/(mol*K) Cpz = 200 J/(mol*K) AHRX = -7.5 kJ/mol A E = 70 kJ/mol k = 2.1(L/mol) /hr at T = 87C b.) Calculate the exit concentrations of ALL species. c.) What is the exit conversion of species A? d.) Plot temperature as a function of reactor volume. The following elementary, gas-phase reaction is to be carried out adiabatically in under high pressure in a 90000 mL PFR. 2A + BC 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) CPs = 47 J/(mol) Cpc = 141 J/(mol*K) Cpx = 120 J/(mol*K) Cpz = 200 J/(mol*K) AHRX = -7.5 kJ/mol A E = 70 kJ/mol k = 2.1(L/mol) /hr at T = 87C b.) Calculate the exit concentrations of ALL species. c.) What is the exit conversion of species A? d.) Plot temperature as a function of reactor volume