Saturated liquid 189°F 33 psia 32 462,385 Ib/h 99.05 mole % methanol Feed 442,900,000 Btu/h 262.5°F, 40 psia 188,975 Ib/h 1.01 mol% methanol

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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Results of design calculations for a methanol–water distillation operation are given in Figure . (a) Calculate the column diameter at the top and at the bottom, assuming sieve trays. Should the column be swaged? (b) Calculate the length and diameter of the horizontal reflux drum.

Saturated
liquid
189°F
33 psia
32
462,385 Ib/h
99.05 mole % methanol
Feed
442,900,000 Btu/h
262.5°F, 40 psia
188,975 Ib/h
1.01 mol% methanol
Transcribed Image Text:Saturated liquid 189°F 33 psia 32 462,385 Ib/h 99.05 mole % methanol Feed 442,900,000 Btu/h 262.5°F, 40 psia 188,975 Ib/h 1.01 mol% methanol
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