9.12. The reversible first-order gas reaction = 1 = A R is to be carried out in a mixed flow reactor. For operations at 300 K the volume of reactor required is 100 liters for 60% conversion of A. What should be the volume of the reactor for the same feed rate and conversion but with operations at 400 K? 10³ exp [-2416/T] Data: k₁ AC₂ CPR CPA = 0 AH, = -8000 cal/mol at 300 K K = 10 at 300 K Feed consists of pure A Total pressure stays constant 2
9.12. The reversible first-order gas reaction = 1 = A R is to be carried out in a mixed flow reactor. For operations at 300 K the volume of reactor required is 100 liters for 60% conversion of A. What should be the volume of the reactor for the same feed rate and conversion but with operations at 400 K? 10³ exp [-2416/T] Data: k₁ AC₂ CPR CPA = 0 AH, = -8000 cal/mol at 300 K K = 10 at 300 K Feed consists of pure A Total pressure stays constant 2
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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![9.12. The reversible first-order gas reaction
-
1
=
A R
is to be carried out in a mixed flow reactor. For operations at 300 K the
volume of reactor required is 100 liters for 60% conversion of A. What
should be the volume of the reactor for the same feed rate and conversion
but with operations at 400 K?
Data: k₁
10³ exp [-2416/T]
CpA = 0
ACp CpR
AH, = -8000 cal/mol at 300 K
K 10 at 300 K
Feed consists of pure A
Total pressure stays constant
2](/v2/_next/image?url=https%3A%2F%2Fcontent.bartleby.com%2Fqna-images%2Fquestion%2Fcc848ade-4f38-45df-b422-a4c468d5fa68%2Fb2fec555-7243-40e5-b2fe-a440bd48b314%2F62ab6a_processed.jpeg&w=3840&q=75)
Transcribed Image Text:9.12. The reversible first-order gas reaction
-
1
=
A R
is to be carried out in a mixed flow reactor. For operations at 300 K the
volume of reactor required is 100 liters for 60% conversion of A. What
should be the volume of the reactor for the same feed rate and conversion
but with operations at 400 K?
Data: k₁
10³ exp [-2416/T]
CpA = 0
ACp CpR
AH, = -8000 cal/mol at 300 K
K 10 at 300 K
Feed consists of pure A
Total pressure stays constant
2
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