Assume the validity of the De Priester charts, make the following VLE calculations for ethane (1)/ propane (2)/ isobutene (3)/ isopentane (4) systems: DEW P, given y1 = 0.40, y2 = 0.20, y3 = 0.10 and T = 75 degree Celsius BUBL T, given x1 = 0.27, x2 = 0.16, x3 = 0.25 and P = 35Bar
Assume the validity of the De Priester charts, make the following VLE calculations for ethane (1)/ propane (2)/ isobutene (3)/ isopentane (4) systems: DEW P, given y1 = 0.40, y2 = 0.20, y3 = 0.10 and T = 75 degree Celsius BUBL T, given x1 = 0.27, x2 = 0.16, x3 = 0.25 and P = 35Bar
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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Assume the validity of the De Priester charts, make the following VLE calculations for ethane
(1)/ propane (2)/ isobutene (3)/ isopentane (4) systems:
DEW P, given y1 = 0.40, y2 = 0.20, y3 = 0.10 and T = 75 degree Celsius
BUBL T, given x1 = 0.27, x2 = 0.16, x3 = 0.25 and P = 35Bar
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