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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

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

Introduction to Chemical Engineering Thermodynamics
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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B) 100kg of a solution of acetic acid and H2O containing 30% acetic acid by weight is to be extracted three times with isopropyl ether using 40kg of isopropyl ether in cach 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 25.8% Ist Stage 11.7% IInd Stage 9.5% 22.7% IIIrd Stage 7.8% 20% BALU, K.; RAMALINGAM, S.; DEEBIKA, B. AND SATHYAMOORTHI, K. (2014)|
Transcribed Image Text:B) 100kg of a solution of acetic acid and H2O containing 30% acetic acid by weight is to be extracted three times with isopropyl ether using 40kg of isopropyl ether in cach 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 25.8% Ist Stage 11.7% IInd Stage 9.5% 22.7% IIIrd Stage 7.8% 20% BALU, K.; RAMALINGAM, S.; DEEBIKA, B. AND SATHYAMOORTHI, K. (2014)|
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