pr0cess plant needs tw0 ethyl-alc0h0l-water s0luti0ns, 0ne c0ntaining 89% ethan0l and the 0ther 60% ethan0l. A dilute mixture c0ntaining 35% ethan0l is available. The 60% s0luti0n is withdrawn at the rate of 1000 kg/h. If the b0tt0ms is t0 c0ntain n0 m0re than 3% ethan0l and 0nly 5% 0f the alc0h0l in the feed sh0uld be l0st in this stream, calculate the fl0w rates 0f all the unkn0wn streams.....
pr0cess plant needs tw0 ethyl-alc0h0l-water s0luti0ns, 0ne c0ntaining 89% ethan0l and the 0ther 60% ethan0l. A dilute mixture c0ntaining 35% ethan0l is available. The 60% s0luti0n is withdrawn at the rate of 1000 kg/h. If the b0tt0ms is t0 c0ntain n0 m0re than 3% ethan0l and 0nly 5% 0f the alc0h0l in the feed sh0uld be l0st in this stream, calculate the fl0w rates 0f all the unkn0wn streams.....
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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.....pr0cess plant needs tw0 ethyl-alc0h0l-water s0luti0ns, 0ne c0ntaining 89% ethan0l and the 0ther 60% ethan0l. A dilute mixture c0ntaining 35% ethan0l is available. The 60% s0luti0n is withdrawn at the rate of 1000 kg/h. If the b0tt0ms is t0 c0ntain n0 m0re than 3% ethan0l and 0nly 5% 0f the alc0h0l in the feed sh0uld be l0st in this stream, calculate the fl0w rates 0f all the unkn0wn streams.....
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