A continuous rectification column is used to separate a binary mixture of A and B. Distillate is produced at 100 kmol/hr containing 98 mole % A. The mole fractions of A in the liquid and in the vapor, z and y respectively, from two adjacent ideal plates in the enriching section are as follows: 0.65 0.82 0.56 0.76 If the latent heat of vaporization is the same for all mixtures and if the feed is a saturated liquid, calculate: (a) the reflux ratio (b) vapor rate in the stripping section in kmol/hr.

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
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A continuous rectification column is used to separate a binary mixture of A and B. Distillate
is produced at 100 kmol/hr containing 98 mole % A. The mole fractions of A in the liquid
and in the vapor, I and y respectively, from two adjacent ideal plates in the enriching section
are as follows:
0.65 0.82
0.56 0.76
If the latent heat of vaporization is the same for all mixtures and if the feed is a saturated
liquid, calculate:
(a) the reflux ratio
L(b) vapor rate in the stripping section in kmol/hr.
Transcribed Image Text:A continuous rectification column is used to separate a binary mixture of A and B. Distillate is produced at 100 kmol/hr containing 98 mole % A. The mole fractions of A in the liquid and in the vapor, I and y respectively, from two adjacent ideal plates in the enriching section are as follows: 0.65 0.82 0.56 0.76 If the latent heat of vaporization is the same for all mixtures and if the feed is a saturated liquid, calculate: (a) the reflux ratio L(b) vapor rate in the stripping section in kmol/hr.
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