A feed of component A and B containing 55 mole % of A is fed to a distillation tower at a rate of 40 kmol/h. and operating pressure of 1 atm. The feed is at bubble point. The top product A fraction is 0.975. Also not more than 2% of A in the feed should be allowed to leave at bottom. Determine: a) The minimum reflux ratio. b) The number of theoretical plates if actual reflux ratio is 1.4 times the minimum. c) The slopes of the two operating lines. Equilibrium data for component A X 0.02 0.04 0.05 0.07 0.09 0.14 0.22 0.43 0.60 0.78 0.85 0. y 0.04 0.09 0.12 0.15 0.23 0.32 0.45 0.68 0.80 0.91 0.95 0.

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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A feed of component A and B containing 55 mole % of
A is fed to a distillation tower at a rate of 40 kmol/h.
and operating pressure of 1 atm. The feed is at bubble
point. The top product A fraction is 0.975. Also not
more than 2% of A in the feed should be allowed to
leave at bottom.
Determine:
a) The minimum reflux ratio.
b) The number of theoretical plates if actual reflux ratio
is 1.4 times the minimum.
c) The slopes of the two operating lines.
Equilibrium data for component A
X
0.02 0.04 0.05 0.07 0.09 0.14 0.22 0.43 0.60 0.78 0.85 0.
y
0.04 0.09 0.12 0.15 0.23 0.32 0.45 0.68 0.80 0.91 0.95 0.
Transcribed Image Text:A feed of component A and B containing 55 mole % of A is fed to a distillation tower at a rate of 40 kmol/h. and operating pressure of 1 atm. The feed is at bubble point. The top product A fraction is 0.975. Also not more than 2% of A in the feed should be allowed to leave at bottom. Determine: a) The minimum reflux ratio. b) The number of theoretical plates if actual reflux ratio is 1.4 times the minimum. c) The slopes of the two operating lines. Equilibrium data for component A X 0.02 0.04 0.05 0.07 0.09 0.14 0.22 0.43 0.60 0.78 0.85 0. y 0.04 0.09 0.12 0.15 0.23 0.32 0.45 0.68 0.80 0.91 0.95 0.
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