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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 Q = 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. D. Plot Fao /-TA VS. degree of conversion, in the range 0

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 Q = 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. D. Plot Fao /-TA VS. degree of conversion, in the range 0

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
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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. D. Plot Fa,0 /-ra vs. degree of conversion, in the range 0 <x < 0.9. Which reactor volume is needed for X = 0.75?. E. What are the retention times for each of the reactor volumes calculated in question D?
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. D. Plot Fa,0 /-ra vs. degree of conversion, in the range 0 <x < 0.9. Which reactor volume is needed for X = 0.75?. E. What are the retention times for each of the reactor volumes calculated in question D?
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