B) 100kg of a solution of acetic acid and H20 containing 30% acetic acid by weight is to be extracted three times with isopropyl ether using 40kg of isopropyl ether in each stage. Determine the weight of acetic acid extracted and the percentage recovery of acetic acid. The following data are available. Concentrations of acetic acid in the leaving streams are Isopropyl ether rich phase H2O rich phase Ist Stage 11.7% 25.8% Ilnd Stage 9.5% 22.7% IlIrd Stage 7.8% 20% BALU, K.; RAMALINGAM, S.; DEEBIKA, B. AND SATHYAMOORTHI, K. (2014)] 12 | Page

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
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B) 100kg of a solution of acetic acid and H20 containing 30% acetic acid by weight is to
be extracted three times with isopropyl ether using 40kg of isopropyl ether in each
stage. Determine the weight of acetic acid extracted and the percentage recovery of
acetic acid. The following data are available. Concentrations of acetic acid in the
leaving streams are
H2O rich phase
Isopropyl ether rich phase
11.7%
Ist Stage
25.8%
Ilnd Stage
9.5%
22.7%
IlIrd Stage
7.8%
20%
BALU, K.; RAMALINGAM, S.; DEEBIKA, B. AND SATHYAMOORTHI, K. (2014)|
12 | Page
Transcribed Image Text:B) 100kg of a solution of acetic acid and H20 containing 30% acetic acid by weight is to be extracted three times with isopropyl ether using 40kg of isopropyl ether in each stage. Determine the weight of acetic acid extracted and the percentage recovery of acetic acid. The following data are available. Concentrations of acetic acid in the leaving streams are H2O rich phase Isopropyl ether rich phase 11.7% Ist Stage 25.8% Ilnd Stage 9.5% 22.7% IlIrd Stage 7.8% 20% BALU, K.; RAMALINGAM, S.; DEEBIKA, B. AND SATHYAMOORTHI, K. (2014)| 12 | Page
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