Compositions and amounts of distillate and bottoms.

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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3. The liquid feed of 100 mol/h composed of 20% n-butane (A), 30% i-pentane (B), and 50%
n-pentane (C) is fed to a distillation column at 4 atm abs pressure and is to be fractioned so
that 95.0 mol% i-pentane (B) is recovered at the distillate and 95 mol% of the n-pentane
(C) in the bottoms. Calculate;
a. Compositions and amounts of distillate and bottoms.
b. Top and bottom temperatures.
c. Minimum stages for total reflux.
Hint: B is light key, C is heavy key.
Equilibrium K values for specified hydrocarbons at 4.0 atm
absolute.
10
n-butane
i-pentane
n-pentane
0.1
25
50
75
100
125
150
175
200
Temperature
Transcribed Image Text:3. The liquid feed of 100 mol/h composed of 20% n-butane (A), 30% i-pentane (B), and 50% n-pentane (C) is fed to a distillation column at 4 atm abs pressure and is to be fractioned so that 95.0 mol% i-pentane (B) is recovered at the distillate and 95 mol% of the n-pentane (C) in the bottoms. Calculate; a. Compositions and amounts of distillate and bottoms. b. Top and bottom temperatures. c. Minimum stages for total reflux. Hint: B is light key, C is heavy key. Equilibrium K values for specified hydrocarbons at 4.0 atm absolute. 10 n-butane i-pentane n-pentane 0.1 25 50 75 100 125 150 175 200 Temperature
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