Consider the continuous stirred tank reactor configurations with a first-order decay reaction coefficient k, Q, C. (a) V, k Q. Çut (b) a, C. 0.5V, k Q, C* 0.5V, k a. Cut Q. C. (c) (1/n)V, (1/n)V, Q. Caut (1/n)V, Q. Cu a, c2 k k n tanks in series (1) Based on the mass balance concept, derive the concentration Cae for configuration (a) (2) Derive an expression for Ceur for configuration (b) (3) Derive an expression for Cout for configuration (c). Is this configuration more or less efficient than a plug flow reactor with the same hydraulic retention time and reaction rate coefficient?
Consider the continuous stirred tank reactor configurations with a first-order decay reaction coefficient k, Q, C. (a) V, k Q. Çut (b) a, C. 0.5V, k Q, C* 0.5V, k a. Cut Q. C. (c) (1/n)V, (1/n)V, Q. Caut (1/n)V, Q. Cu a, c2 k k n tanks in series (1) Based on the mass balance concept, derive the concentration Cae for configuration (a) (2) Derive an expression for Ceur for configuration (b) (3) Derive an expression for Cout for configuration (c). Is this configuration more or less efficient than a plug flow reactor with the same hydraulic retention time and reaction rate coefficient?
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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Transcribed Image Text:Consider the continuous stirred tank reactor configurations with a first-order decay
reaction coefficient k,
Q, C.
(a)
V, k
Q. Çut
(b)
a, C.
0.5V, k Q, C*
0.5V, k
a. Cut
Q. C.
(c)
(1/n)V,
(1/n)V,
Q. Caut
(1/n)V,
Q. Cu
a, c2
k
k
n tanks in series
(1) Based on the mass balance concept, derive the concentration Cae for configuration (a)
(2) Derive an expression for Ceur for configuration (b)
(3) Derive an expression for Cout for configuration (c). Is this configuration more or less efficient than
a plug flow reactor with the same hydraulic retention time and reaction rate coefficient?
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