A fluidized bed CSTR is used to perform the following homogenous gas-phase reaction: A + B → C The reaction is elementary and is first-order in both A and B. Equimolar feed is used in the reactor with vo = 100- min’ Po = 2 atm, T = 400 K, and k = 15; . The reactor is kg mol min' operated at constant temperature and pressure. Moreover, the system behaves as an ideal gas. Calculate the weight of the catalyst required to achieve 95% conversion of A.

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
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A fluidized bed CSTR is used to perform the following homogenous gas-phase
reaction:
A + B → C
The reaction is elementary and is first-order in both A and B. Equimolar feed is used in the
L2
reactor with vo
100-
Po = 2 atm, T = 400 K, and k = 15-
min
The reactor is
kg mol min
operated at constant temperature and pressure. Moreover, the system behaves as an ideal
gas. Calculate the weight of the catalyst required to achieve 95% conversion of A.
Transcribed Image Text:A fluidized bed CSTR is used to perform the following homogenous gas-phase reaction: A + B → C The reaction is elementary and is first-order in both A and B. Equimolar feed is used in the L2 reactor with vo 100- Po = 2 atm, T = 400 K, and k = 15- min The reactor is kg mol min operated at constant temperature and pressure. Moreover, the system behaves as an ideal gas. Calculate the weight of the catalyst required to achieve 95% conversion of A.
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