The equation of the rectifying section operating line for distillation of a mixture of A and B in packed column is y = 0.6x + 0.376. The relative volatility of A with respect to B is 2. At a point in the rectifying section, x = 0.8, what are the concentrations of more volatile at the vapour liquid interface Given, kmoles kmoles = 400 Kx and ky = 170 m³.hr.Ay m³.hr.Ax

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
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The equation of the rectifying section operating line for distillation of a mixture of A and B in packed
column is y = 0.6x + 0.376. The relative volatility of A with respect to B is 2. At a point in the
rectifying section, x = 0.8, what are the concentrations of more volatile at the vapour liquid interface
Given ,
kтoles
ктoles
= 400-
Kx
and ky
= 170
m³.hr.Ay
m³.hr.Ax
Transcribed Image Text:The equation of the rectifying section operating line for distillation of a mixture of A and B in packed column is y = 0.6x + 0.376. The relative volatility of A with respect to B is 2. At a point in the rectifying section, x = 0.8, what are the concentrations of more volatile at the vapour liquid interface Given , kтoles ктoles = 400- Kx and ky = 170 m³.hr.Ay m³.hr.Ax
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