13.17. For the system ethyl ethanoate(1)/n-heptane(2) at 343.15 K, Iny1 =0.95.x3; Iny2=0.95xf; Pat = 79.80 kPa; and Pat = 40.50 kPa. Assuming the validity of Eq. (13.19), (a) Make a BUBL P calculation for T= 343.15 K, x1 = 0.05. (b) Make a DEW P calculation for T = 343.15 K, y1 = 0.05. (c) What are the azeotrope composition and pressure at T = 343.15 K? %3D %3D
13.17. For the system ethyl ethanoate(1)/n-heptane(2) at 343.15 K, Iny1 =0.95.x3; Iny2=0.95xf; Pat = 79.80 kPa; and Pat = 40.50 kPa. Assuming the validity of Eq. (13.19), (a) Make a BUBL P calculation for T= 343.15 K, x1 = 0.05. (b) Make a DEW P calculation for T = 343.15 K, y1 = 0.05. (c) What are the azeotrope composition and pressure at T = 343.15 K? %3D %3D
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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