A binary distillation is performed so that a distillate 94% and bottoms 8% in of the more volatile Component A results. The process shown below reflects one operating condition of a feed stream. Rectification, Stripping and the q-line are all provided on the x-y diagram below. Aling with expected stage for the distillation.. Solve a), b) c)
A binary distillation is performed so that a distillate 94% and bottoms 8% in of the more volatile Component A results. The process shown below reflects one operating condition of a feed stream. Rectification, Stripping and the q-line are all provided on the x-y diagram below. Aling with expected stage for the distillation.. Solve a), b) c)
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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A binary distillation is performed so that a distillate 94% and bottoms 8% in of the more volatile Component A results. The process shown below reflects one operating condition of a feed stream.
Rectification, Stripping and the q-line are all provided on the x-y diagram below. Aling with expected stage for the distillation..
Solve a), b) c)
![1M
1348
1.23
LINU
0.00 0.05 0.10 8.15
0.30 0.250.300.350.400.450.50 855 64 165 5 *
Volatile component mole fraction: x, y (perhaps x)
** 090 6.95
O
Answer the following -
(a) What is the y-mole fraction (vapor) leaving stage 27
(b) What is the y-mole fraction (vapor) leaving the feed stage?
(c) What is the feed stage tray number, e.g. 1, 2, 3 or?
What is temperature of the liquid stream leaving the reboiler?
(e) What is the temperature of the vapor stream leaving the feed stage?
(f) What is the temperature of the liquid stream leaving stage 2?
(g) What is the temperature of the liquid reflux returned to the column? Note: A total condensor is installed.
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Transcribed Image Text:1M
1348
1.23
LINU
0.00 0.05 0.10 8.15
0.30 0.250.300.350.400.450.50 855 64 165 5 *
Volatile component mole fraction: x, y (perhaps x)
** 090 6.95
O
Answer the following -
(a) What is the y-mole fraction (vapor) leaving stage 27
(b) What is the y-mole fraction (vapor) leaving the feed stage?
(c) What is the feed stage tray number, e.g. 1, 2, 3 or?
What is temperature of the liquid stream leaving the reboiler?
(e) What is the temperature of the vapor stream leaving the feed stage?
(f) What is the temperature of the liquid stream leaving stage 2?
(g) What is the temperature of the liquid reflux returned to the column? Note: A total condensor is installed.
Click Save and Submit to save and submit. Click Save All Answers to save all answers.
![andrammaron
y, Mole Fraction
1.00
0.95
0.90
085
0.80
0.75
0.70
065
0.60
0.55
0.50
0.45
0.40
0.35
0.30
0.75
0.20
015
010
DOS
DOD
0.00 0.05 0.10 0.15 0.20 3.25 0.30 0.35 0.40 0.45 0.500.55
. Mole Fraction
The following is a Tvy dinram for the custom
0.90 0.95 1.00
Sa 0.85
INING X 68 DU 0.75
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Transcribed Image Text:andrammaron
y, Mole Fraction
1.00
0.95
0.90
085
0.80
0.75
0.70
065
0.60
0.55
0.50
0.45
0.40
0.35
0.30
0.75
0.20
015
010
DOS
DOD
0.00 0.05 0.10 0.15 0.20 3.25 0.30 0.35 0.40 0.45 0.500.55
. Mole Fraction
The following is a Tvy dinram for the custom
0.90 0.95 1.00
Sa 0.85
INING X 68 DU 0.75
Click Save and Submit to save and submit. Click Save All Answers to save all answers.
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