MODULE 6 11. Toluene reacts with H₂ to form benzene (B), but a side reaction occurs in which a by-product, diphenyl (D), is formed: C7H8 + H₂ -> C6H6 + CHA Toluene Hydrogen Benzene Methane C7H8 + H₂ C12H10 Diphenyl The process is shown below. Hydrogen is added to the gas recycle stream to make the ratio of H₂ to CH4 1 to 1 before the gas enters the mixer. The ratio of H₂ to toluene entering the reactor at G is 4 to 1. The conversion of toluene to benzene on one pass through the reactor is 80%, and the conversion of toluene to the by-product diphenyl is 8% on the same pass. Calculate the moles of Ra and moles of R₁ per hour. F Feed 100% toiuono 3450 lb/hr + CHA Makeup M 100% H₂ Mixer Gross feed G Reactor Liquid recycle R 100% toluene Gas recycle Ro Separator P Purge He only B Benzene 100% D Diphenyl 100%

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
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Problem 1.1P
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MODULE 6
11. Toluene reacts with H₂ to form benzene (B), but a side reaction occurs in which a by-product, diphenyl (D), is formed:
C7H8 + H₂ -> C6H6 + CH4
Toluene
Hydrogen
Benzene
Methane
C7H8 + H₂
The process is shown below. Hydrogen is added to the gas recycle stream to make the ratio of H₂ to CH4 1 to 1 before
the gas enters the mixer. The ratio of H₂ to toluene entering the reactor at G is 4 to 1. The conversion of toluene to
benzene on one pass through the reactor is 80%, and the conversion of toluene to the by-product diphenyl is 8% on
the same pass. Calculate the moles of RG and moles of R₁ per hour.
F
Feed
C12H10 + CH4
Diphenyl
100% toluene
3450 lb/hr
Mixer
Makeup
M 100% H₂
Gross
feed
G
Reactor
Liquid recycle R
100% toluene
Gas recycle
Ro
Separator
P Purge
H₂
CH₂
- only
B
Benzene
100%
D
Diphenyl
100%
Transcribed Image Text:MODULE 6 11. Toluene reacts with H₂ to form benzene (B), but a side reaction occurs in which a by-product, diphenyl (D), is formed: C7H8 + H₂ -> C6H6 + CH4 Toluene Hydrogen Benzene Methane C7H8 + H₂ The process is shown below. Hydrogen is added to the gas recycle stream to make the ratio of H₂ to CH4 1 to 1 before the gas enters the mixer. The ratio of H₂ to toluene entering the reactor at G is 4 to 1. The conversion of toluene to benzene on one pass through the reactor is 80%, and the conversion of toluene to the by-product diphenyl is 8% on the same pass. Calculate the moles of RG and moles of R₁ per hour. F Feed C12H10 + CH4 Diphenyl 100% toluene 3450 lb/hr Mixer Makeup M 100% H₂ Gross feed G Reactor Liquid recycle R 100% toluene Gas recycle Ro Separator P Purge H₂ CH₂ - only B Benzene 100% D Diphenyl 100%
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