4.10. Continuous, single-stage distillation. Saturated-liquid feed of F = 40 mol/h, containing 50 mol% A and B, is supplied to the apparatus in Figure 4.23. The condensate is split so that reflux/distillate = 1. (a) If heat is supplied such that W = 30 mol/h and α = 2, as defined below, what will be the composition of the overhead and the bot- toms product? PS απ Α = PB YAXB YBXA (b) If the operation is changed so that no condensate is returned to the still pot and W = 3D, compute the product compositions. Vapor V Condenser Still pot Feed F Distillate Reflux R D Heat Bottoms W

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
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4.10. Continuous, single-stage distillation.
Saturated-liquid feed of F = 40 mol/h, containing 50 mol% A
and B, is supplied to the apparatus in Figure 4.23. The condensate is
split so that reflux/distillate = 1.
(a) If heat is supplied such that W = 30 mol/h and α = 2, as defined
below, what will be the composition of the overhead and the bot-
toms product?
PS
απ Α =
PB
YAXB
YBXA
(b) If the operation is changed so that no condensate is returned to
the still pot and W = 3D, compute the product compositions.
Vapor
V
Condenser
Still pot
Feed
F
Distillate
Reflux
R
D
Heat
Bottoms
W
Transcribed Image Text:4.10. Continuous, single-stage distillation. Saturated-liquid feed of F = 40 mol/h, containing 50 mol% A and B, is supplied to the apparatus in Figure 4.23. The condensate is split so that reflux/distillate = 1. (a) If heat is supplied such that W = 30 mol/h and α = 2, as defined below, what will be the composition of the overhead and the bot- toms product? PS απ Α = PB YAXB YBXA (b) If the operation is changed so that no condensate is returned to the still pot and W = 3D, compute the product compositions. Vapor V Condenser Still pot Feed F Distillate Reflux R D Heat Bottoms W
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