A desired liquid-phase reaction: R_FR = k₁ C03 CB A+B- is accompanied by a parallel reaction: k₂ A+B- S rs = K₂ C15 C0.5 A number of reactor configurations are possible. Ideal batch, semi-batch, plug-flow and stirred tank could all be used. In the case of the semi-batch reactor, the order of addition of A and B can be changed. Order the reactor configurations from the least desirable to the most desirable to maximize production of the desired product. Explain your reasoning.

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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A desired liquid-phase reaction:
k₁
R_FR = k₁ C³ CB
A+ B
is accompanied by a parallel reaction:
k₂
A+B
S rs = K₂ C15 C0.5
A number of reactor configurations are possible. Ideal batch, semi-batch, plug-flow and stirred
tank could all be used. In the case of the semi-batch reactor, the order of addition of A and B can
be changed. Order the reactor configurations from the least desirable to the most desirable to
maximize production of the desired product. Explain your reasoning.
Transcribed Image Text:A desired liquid-phase reaction: k₁ R_FR = k₁ C³ CB A+ B is accompanied by a parallel reaction: k₂ A+B S rs = K₂ C15 C0.5 A number of reactor configurations are possible. Ideal batch, semi-batch, plug-flow and stirred tank could all be used. In the case of the semi-batch reactor, the order of addition of A and B can be changed. Order the reactor configurations from the least desirable to the most desirable to maximize production of the desired product. Explain your reasoning.
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