Solvent вз Solvent F3=B2 : F2 D3 81 F1 D1 D2 Water Binary azeotrope Ethanol Water Ethanol Pure Pure ethanol water D1 D2 D3 Ethanol + water F1 F2 F3 B1 |вз Solvent recycle Pure water
Solvent вз Solvent F3=B2 : F2 D3 81 F1 D1 D2 Water Binary azeotrope Ethanol Water Ethanol Pure Pure ethanol water D1 D2 D3 Ethanol + water F1 F2 F3 B1 |вз Solvent recycle Pure 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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Forty mol/s of a bubble-point mixture of 75 mol% acetone and 25 mol% methanol at 1 atm is separated by extractive distillation, using ethanol as the solvent, to produce an acetone product of not less than 95 mol% acetone, a methanol product of not less than 98 mol% methanol, and a water stream for recycle of at least 99.9 mol% purity. Prepare a preliminary process design using the traditional three-column sequence consisting of ordinary distillation followed by extractive distillation, and then ordinary distillation to recover
the solvent, as shown for another system in Figure.
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