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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? 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: -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? 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
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. F. Why does the required reactor volume increase with X? Why does it not increase linearly? G. How can two or more reactors be installed in series to reduce the requirements for total reactor volume to reach X = 0.75?
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. F. Why does the required reactor volume increase with X? Why does it not increase linearly? 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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