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: -rA = k[A] where k = 1.2 hr* is the rate constant. G. How can two or more reactors be installed in series to reduce the requirements for total reactor volume to reach X = 0.75?
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: -rA = k[A] where k = 1.2 hr* is the rate constant. G. How can two or more reactors be installed in series to reduce the requirements for total reactor volume to reach X = 0.75?
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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![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.
G. How can two or more reactors be installed in series to reduce the requirements for total reactor
volume to reach X = 0.75?](/v2/_next/image?url=https%3A%2F%2Fcontent.bartleby.com%2Fqna-images%2Fquestion%2F93b23145-5ee0-47ce-8764-c1aacd8763c3%2Fdf25f7bd-ebe7-4e31-a41d-05f19e1e2af2%2F0o5x8nq_processed.png&w=3840&q=75)
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.
G. How can two or more reactors be installed in series to reduce the requirements for total reactor
volume to reach X = 0.75?
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