using matlab

12. Plot Pxy diagram for a binary system of acetonitrile (1)itromethane (2) at 75C. The vapor pressure for pure species are calculated using Eqns. (5) and (6). Pp = exp (14.2724 - 2945.47 T + 224 2972.64 14.2043 - T + 209) where T is temperature. The vapor liquid equilibrium (VLE) coefficient is calculated as Ki = 1, and yi = Kixi where y; is the vapor mole fraction, and x; is the liquid mole fraction. At bubble point Iyi = K;x; = 1. Use total pressure, Pr, from 0.1 kPa to 100 kPa. Distinguish the liquid and vapor phase boundaries in your plot by using different colors. 12. Plot Pxy diagram for a binary system of acetonitrile (1)itromethane (2) at 75C. The vapor pressure for pure species are calculated using Eqns. (5) and (6). Pp = exp (14.2724 - 2945.47 T + 224 2972.64 14.2043 - T + 209) where T is temperature. The vapor liquid equilibrium (VLE) coefficient is calculated as Ki = 1, and yi = Kixi where y; is the vapor mole fraction, and x; is the liquid mole fraction. At bubble point Iyi = K;x; = 1. Use total pressure, Pr, from 0.1 kPa to 100 kPa. Distinguish the liquid and vapor phase boundaries in your plot by using different colors