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EQUILIBRIUM DATA, MOLE- PERCENT ACETONE Liquid 0 11.7 20.7 11.7 29.7 34.1 44.0 52.0 68.7 74.3 2.6 5.4 8.9 17.4 31.5 45.6 55.7 60.1 Vapor o Liquid 63.9 81.5 74.6 87.0 80.3 90.2 86.5 92.5 95.7 100.0 100.0 Vapor 89.4 92.3 94.2 95.5 97.4

EQUILIBRIUM DATA, MOLE- PERCENT ACETONE Liquid 0 11.7 20.7 11.7 29.7 34.1 44.0 52.0 68.7 74.3 2.6 5.4 8.9 17.4 31.5 45.6 55.7 60.1 Vapor o Liquid 63.9 81.5 74.6 87.0 80.3 90.2 86.5 92.5 95.7 100.0 100.0 Vapor 89.4 92.3 94.2 95.5 97.4

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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A 50 mol% mixture of acetone in isopropanol is to be distilled to produce a distillate of 80 mol% acetone and a bottoms of 25 mol%. The feed is a saturated liquid, the column is operated with a reflux ratio of 0.5, and the Murphree vapor efficiency is 50%. How many trays are required? Assume a total condenser, partial reboiler, saturated- liquid reflux, and optimal feed stage. The vapor–liquid equilibrium data are:

EQUILIBRIUM DATA, MOLE- PERCENT ACETONE Liquid 0 11.7 20.7 11.7 29.7 34.1 44.0 52.0 68.7 74.3 2.6 5.4 8.9 17.4 31.5 45.6 55.7 60.1 Vapor o Liquid 63.9 81.5 74.6 87.0 80.3 90.2 86.5 92.5 95.7 100.0 100.0 Vapor 89.4 92.3 94.2 95.5 97.4
Transcribed Image Text:EQUILIBRIUM DATA, MOLE- PERCENT ACETONE Liquid 0 11.7 20.7 11.7 29.7 34.1 44.0 52.0 68.7 74.3 2.6 5.4 8.9 17.4 31.5 45.6 55.7 60.1 Vapor o Liquid 63.9 81.5 74.6 87.0 80.3 90.2 86.5 92.5 95.7 100.0 100.0 Vapor 89.4 92.3 94.2 95.5 97.4
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