Write three balances and use one constraint for the performance of Still 2 to solve for the following quantities for a process feed (₁) of 300.0 mol/h. Overhead from second still (ing) = i mol/h Bottoms from second still (4) = mol/h Benzene mole fraction in bottoms from second still (X4B) = Toluene mole fraction in bottoms from second still (47) = i
Write three balances and use one constraint for the performance of Still 2 to solve for the following quantities for a process feed (₁) of 300.0 mol/h. Overhead from second still (ing) = i mol/h Bottoms from second still (4) = mol/h Benzene mole fraction in bottoms from second still (X4B) = Toluene mole fraction in bottoms from second still (47) = i
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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![Write three balances and use one constraint for the performance of Still 2
to solve for the following quantities for a process feed (₁) of 300.0 mol/h.
Overhead from second still (n) = i
mol/h
Bottoms from second still (4) =
mol/h
Benzene mole fraction in bottoms from second still (X4B)
i
Toluene mole fraction in bottoms from second still (x4T) = i](/v2/_next/image?url=https%3A%2F%2Fcontent.bartleby.com%2Fqna-images%2Fquestion%2F3eaf4e8e-342a-49df-ae3c-b5b0f02158f6%2Fb2f57111-41d4-4362-8179-fd7fee26aa68%2Fjzb07fc_processed.jpeg&w=3840&q=75)
Transcribed Image Text:Write three balances and use one constraint for the performance of Still 2
to solve for the following quantities for a process feed (₁) of 300.0 mol/h.
Overhead from second still (n) = i
mol/h
Bottoms from second still (4) =
mol/h
Benzene mole fraction in bottoms from second still (X4B)
i
Toluene mole fraction in bottoms from second still (x4T) = i
![A liquid mixture containing 30.0 mole% benzene
(B), 25.0% toluene (T), and the balance xylene (X)
is fed to a distillation column.
The bottoms product contains 98.0 mole% X and
no B, and 81.0% of the X in the feed is recovered in
this stream.
The overhead product is fed to a second column.
The overhead product from the second column
contains 95.5% of the B in the feed to this column.
The composition of this stream is 94.0 mole% B
and the balance T.](/v2/_next/image?url=https%3A%2F%2Fcontent.bartleby.com%2Fqna-images%2Fquestion%2F3eaf4e8e-342a-49df-ae3c-b5b0f02158f6%2Fb2f57111-41d4-4362-8179-fd7fee26aa68%2F14jlnp6_processed.jpeg&w=3840&q=75)
Transcribed Image Text:A liquid mixture containing 30.0 mole% benzene
(B), 25.0% toluene (T), and the balance xylene (X)
is fed to a distillation column.
The bottoms product contains 98.0 mole% X and
no B, and 81.0% of the X in the feed is recovered in
this stream.
The overhead product is fed to a second column.
The overhead product from the second column
contains 95.5% of the B in the feed to this column.
The composition of this stream is 94.0 mole% B
and the balance T.
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