A CSTR reactor is designed for the irreversible conversion of A into B and C. The reactor is operated with an inlet volumetric flow of Qo = 50 L/hr with a concentration of compound A, [A]o = 100 g/L. The first order conversion can be described by the rate equation: -TA = k[A] where k = 1.2 hr* is the rate constant. F. Why does the required reactor volume increase with X? Why does it not increase linearly?

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
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Problem 3
A CSTR reactor is designed for the irreversible conversion of A into B and C. The reactor is operated with an
inlet volumetric flow of Qo = 50 L/hr with a concentration of compound A, [A]o = 100 g/L. The first order
conversion can be described by the rate equation:
-Ta = k[A]
where k = 1.2 hr' is the rate constant.
F. Why does the required reactor volume increase with X? Why does it not increase linearly?
Transcribed Image Text:Problem 3 A CSTR reactor is designed for the irreversible conversion of A into B and C. The reactor is operated with an inlet volumetric flow of Qo = 50 L/hr with a concentration of compound A, [A]o = 100 g/L. The first order conversion can be described by the rate equation: -Ta = k[A] where k = 1.2 hr' is the rate constant. F. Why does the required reactor volume increase with X? Why does it not increase linearly?
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