In a continuously operating distillation column, 5000 kg/h equimolar mixture of CCl4 and CS2 will be distilled, and the top product with 90% CS2 in moles and a lower product whose amount does not exceed CS2 in moles will be separated. The reflux ratio is 3 and the feed stream is the liquid at its boiling point. Calculate the required theoretical number of shelves and top and bottom product flow rates. CCl4=154, CS2=76
In a continuously operating distillation column, 5000 kg/h equimolar mixture of CCl4 and CS2 will be distilled, and the top product with 90% CS2 in moles and a lower product whose amount does not exceed CS2 in moles will be separated. The reflux ratio is 3 and the feed stream is the liquid at its boiling point. Calculate the required theoretical number of shelves and top and bottom product flow rates. CCl4=154, CS2=76
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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In a continuously operating distillation column, 5000 kg/h equimolar mixture of CCl4 and CS2 will be distilled, and the top product with 90% CS2 in moles and a lower product whose amount does not exceed CS2 in moles will be separated. The reflux ratio is 3 and the feed stream is the liquid at its boiling point. Calculate the required theoretical number of shelves and top and bottom product flow rates. CCl4=154, CS2=76
Transcribed Image Text:X 0 0.025 0.123 0.225 0.362 0.538 0.775
y 0 0.088 0.275 0.450 0.612 0.763 0.900
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