A binary distillation is performed so that a distillate 94% and bottoms 8% in the more % volatile Component A. The column operates with a 600 kgmoles/hr of feed that is 60% Component A and 40% Component B. A reflux ratio of 1.34 is planned and the feed enters as a saturated liquid (as shown).

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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Answers:

A)362.79

B)5

C)3.60

1.00
y. Mole Fraction
0.80
0.73
0.60
€ 0.50
0.30
0.10
0.00
0.10
0.20
0.30
0.40
0.50
*, Mole Fraction
(a) What is the distillate flowrate (kgmoles/hr)? [a]
(b) How many stages are required? [b]
(c) What is the boilup ratio for this column? [c]
0.70
0.80
0.90
Transcribed Image Text:1.00 y. Mole Fraction 0.80 0.73 0.60 € 0.50 0.30 0.10 0.00 0.10 0.20 0.30 0.40 0.50 *, Mole Fraction (a) What is the distillate flowrate (kgmoles/hr)? [a] (b) How many stages are required? [b] (c) What is the boilup ratio for this column? [c] 0.70 0.80 0.90
A binary distillation is performed so that a distillate 94% and bottoms 8% in the more
% volatile Component A. The column operates with a 600 kgmoles/hr of feed that is
60% Component A and 40% Component B. A reflux ratio of 1.34 is planned and the
feed enters as a saturated liquid (as shown).
Transcribed Image Text:A binary distillation is performed so that a distillate 94% and bottoms 8% in the more % volatile Component A. The column operates with a 600 kgmoles/hr of feed that is 60% Component A and 40% Component B. A reflux ratio of 1.34 is planned and the feed enters as a saturated liquid (as shown).
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