Problem 1 Assuming a mixture of n-pentane (nC3) and n-heptane (nC;) is ideal, draw vapour-liquid r, x ys and P x rsy, equilibrium diagrams for this mixture at constant temperature of 50C. Given the Antoine expression for saturated pressure (i.e., vapour pressure: Pat = P;): B, In Pat = A, - RT with Anc, = 10.422, AnC, = 11.431, Bục, = 26799 J.mol and Bnc, = 35200 J.mol. Also R = 8.3145 J.K-.mol,P] = bar, [T] = K and [B;] = J. mol-". %3D %3D %3D %3D %3!
Problem 1 Assuming a mixture of n-pentane (nC3) and n-heptane (nC;) is ideal, draw vapour-liquid r, x ys and P x rsy, equilibrium diagrams for this mixture at constant temperature of 50C. Given the Antoine expression for saturated pressure (i.e., vapour pressure: Pat = P;): B, In Pat = A, - RT with Anc, = 10.422, AnC, = 11.431, Bục, = 26799 J.mol and Bnc, = 35200 J.mol. Also R = 8.3145 J.K-.mol,P] = bar, [T] = K and [B;] = J. mol-". %3D %3D %3D %3D %3!
Introduction to Chemical Engineering Thermodynamics
8th Edition
ISBN:9781259696527
Author:J.M. Smith Termodinamica en ingenieria quimica, Hendrick C Van Ness, Michael Abbott, Mark Swihart
Publisher:J.M. Smith Termodinamica en ingenieria quimica, Hendrick C Van Ness, Michael Abbott, Mark Swihart
Chapter1: Introduction
Section: Chapter Questions
Problem 1.1P
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