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 L min' mol kg cat min atm² Vo= 100- Po 3 atm, T = 500 K, The reactor is operated at constant temperature and pressure. Moreover, the system behaves as an ideal gas. Calculate the weight of the catalyst required to achieve 90% conversion of A. and k= 0.15;

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 reactor with
L
Vo = 100-
'min'
Po = 3 atm, T = 500 K,
mol
kg cat - min atm²
and k = 0.15;
The reactor is operated at constant temperature and pressure. Moreover, the
system behaves as an ideal gas. Calculate the weight of the catalyst required
to achieve 90% 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 reactor with L Vo = 100- 'min' Po = 3 atm, T = 500 K, mol kg cat - min atm² and k = 0.15; The reactor is operated at constant temperature and pressure. Moreover, the system behaves as an ideal gas. Calculate the weight of the catalyst required to achieve 90% conversion of A.
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