A countercurrent extraction system uses 3 steps for acid extraction acetic acid/water/isopropyl ether at 20°C and 1 atm. The feed consists of 40% (by mass) of acetic acid and 60% (by mass) of water. The feed is 2000 kg/h. The solvent used contains 1% (by mass) of acetic acid. It is necessary that the raffinate at the exit of the extractor contains 5% of acetic acid (by mass). Determine: The amount of solvent, extract in MS and raffinate R1 Equilibrium data: Equilibrium diagrams of the ternary system: acetic acid/water/isopropyl ether (in mass fractions at 20°C and 1 atm).

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
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A countercurrent extraction system uses 3 steps for acid extraction acetic acid/water/isopropyl ether at 20°C and 1 atm. The feed consists of 40% (by mass) of acetic acid and 60% (by mass) of water. The feed is 2000 kg/h. The solvent used contains 1% (by mass) of acetic acid. It is necessary that the raffinate at the exit of the extractor contains 5% of acetic acid (by mass). 

Determine: The amount of solvent, extract in MS and raffinate R1 

Equilibrium data: Equilibrium diagrams of the ternary system: acetic acid/water/isopropyl ether
(in mass fractions at 20°C and 1 atm). 

Acetic Acid
1.0
isopropyl
ether
0.8
0.6
0.4
0.2
0
0
0.2
L
Fir
Fir
tir
0.4
PON
THE
IHE
IFT
1
1
1
H
14
14
0.6
T
ITT
I
11
T
In
TI
0.8
1.0
Water
Transcribed Image Text:Acetic Acid 1.0 isopropyl ether 0.8 0.6 0.4 0.2 0 0 0.2 L Fir Fir tir 0.4 PON THE IHE IFT 1 1 1 H 14 14 0.6 T ITT I 11 T In TI 0.8 1.0 Water
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