A liquid has the following composition in mol%: Propane 1.36%, i-Butane 14.33%, n-Butane 16.37%, i-pentane 15.66%, n-Pentane 17.88% and n-Hexane 34.4%. The mixture must be separated into a column, with 95% of the n-butane that enters the feed must leave in the distillate and 98% of the isopentane that enters must come out at the bottom. The Column has a pressure at 30 psia and uses a condenser that operates at 10.78 ºC and a cooler that operates at 63.33 ºC. Making the pertinent considerations, Calculate the minimum number of theoretical stages required. Determine the distribution of components in the distillate and in the background.
A liquid has the following composition in mol%: Propane 1.36%, i-Butane 14.33%, n-Butane 16.37%, i-pentane 15.66%, n-Pentane 17.88% and n-Hexane 34.4%. The mixture must be separated into a column, with 95% of the n-butane that enters the feed must leave in the distillate and 98% of the isopentane that enters must come out at the bottom. The Column has a pressure at 30 psia and uses a condenser that operates at 10.78 ºC and a cooler that operates at 63.33 ºC. Making the pertinent considerations, Calculate the minimum number of theoretical stages required. Determine the distribution of components in the distillate and in the background.
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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Question
A liquid has the following composition in mol%: Propane 1.36%, i-Butane 14.33%, n-Butane 16.37%, i-pentane 15.66%, n-Pentane 17.88% and n-Hexane 34.4%.
The mixture must be separated into a column, with 95% of the n-butane that enters the feed must leave in the distillate and 98% of the isopentane that enters must come out at the bottom. The Column has a pressure at 30 psia and uses a condenser that operates at 10.78 ºC and a cooler that operates at 63.33 ºC. Making the pertinent considerations, Calculate the minimum number of theoretical stages required. Determine the distribution of components in the distillate and in the background.
Transcribed Image Text:T.
pr = P, exp -5,4(@+1\÷-1) atm),
P
%3D
|Comp
3| PROPΑΝΟ
Tc
Pc
369,8
425,2
408,1
4,249
3,797
3,648
3,369
0,152
0,193
4 n-BUTANO
5 ISOBUTANO
0,177
0,249
0,228
7 n-PENTANO
469,7
460,4
507,4
3,381
3,012
8 ISOPENTANO
11 n-HEXANO
0,305
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