The homogeneous reaction in gas phase A → 3R follows 2nd order kinetics. For a feed rate of 4 m3/h of pure A at 5 atm and 350°C, an experimental reactor consisting of a tube 2.5 cm in diameter by 2 m in length allows 60% conversion. An industrial facility should treat 320 m3/h of feed with 50% A and 50% inert at 350°C and 25 atm, to obtain 80% conversion. a) How many tubes like the ones mentioned will be needed? b) Should they be placed in series or parallel?
The homogeneous reaction in gas phase A → 3R follows 2nd order kinetics. For a feed rate of 4 m3/h of pure A at 5 atm and 350°C, an experimental reactor consisting of a tube 2.5 cm in diameter by 2 m in length allows 60% conversion. An industrial facility should treat 320 m3/h of feed with 50% A and 50% inert at 350°C and 25 atm, to obtain 80% conversion. a) How many tubes like the ones mentioned will be needed? b) Should they be placed in series or parallel?
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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The homogeneous reaction in gas phase A → 3R follows 2nd order kinetics. For a feed rate of 4 m3/h of pure A at 5 atm and 350°C, an experimental reactor consisting of a tube 2.5 cm in diameter by 2 m in length allows 60% conversion. An industrial facility should treat 320 m3/h of feed with 50% A and 50% inert at 350°C and 25 atm, to obtain 80% conversion.
a) How many tubes like the ones mentioned will be needed?
b) Should they be placed in series or parallel?
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