Ternary Systems - Liquid Liquid Extraction: A liquid extractor is used to try to remove acetone from a water stream using methyl isobutyl ketone (MIBK). A flowchart of the process is shown (below). Phase behavior data is given in the ternary diagram (also below). Determine the following for this system: a. The overall composition (M) for the process. Plot its location as point M on the ternary diagram. b. The composition of the extract and raffinate streams. Plot their locations on the ternary diagram as points E and R, respectively. 195 g/ht 0.1g Adg 0.9g Wig 596 g/hr pure MIBK Liquid Extractor Mi g/hr xl g Ac/g x2 g W/g x3 g MIBK/g M2 g/hr x4 g Acfg x5 g W/g xó g MIBK/g MIBK 50 20 Acetic acid 30 40/ 20 90 80 70 60 50 9 40 X 20 Water
Ternary Systems - Liquid Liquid Extraction: A liquid extractor is used to try to remove acetone from a water stream using methyl isobutyl ketone (MIBK). A flowchart of the process is shown (below). Phase behavior data is given in the ternary diagram (also below). Determine the following for this system: a. The overall composition (M) for the process. Plot its location as point M on the ternary diagram. b. The composition of the extract and raffinate streams. Plot their locations on the ternary diagram as points E and R, respectively. 195 g/ht 0.1g Adg 0.9g Wig 596 g/hr pure MIBK Liquid Extractor Mi g/hr xl g Ac/g x2 g W/g x3 g MIBK/g M2 g/hr x4 g Acfg x5 g W/g xó g MIBK/g MIBK 50 20 Acetic acid 30 40/ 20 90 80 70 60 50 9 40 X 20 Water
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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Chemical engineering
Transcribed Image Text:Ternary Systems - Liquid Liquid Extraction:
A liquid extractor is used to try to remove acetone from a water stream using methyl isobutyl
ketone (MIBK). A flowchart of the process is shown (below). Phase behavior data is given in
the ternary diagram (also below). Determine the following for this system:
a. The overall composition (M) for the process. Plot its location as point M on the
ternary diagram.
b. The composition of the extract and raffinate streams. Plot their locations on the
ternary diagram as points E and R, respectively.
195 g/hr
0.1g Adg
0.9 g W/g
596 g/hr
pure MIBK
Liquid
Extractor
Mi g/hr
xl g Ac/g
x2 g W/g
x3 g MIBK/g
M2 g/hr
x4 g Aclg
x5 g W/g
x6 g MIBK/g
90
60
50
MIBK 10 20
40
Acetic acid
30
20
10
90
80
70
60
50
8
9
30
&
90
10
Water
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