1. The Homogeneous gas phase reaction A-→ 3R, satisfactorily follows second order kinetics. For feed rate of 4 m3/h of pure A at 350 °C and 5 ATM, an experimental reactor (size 25 mm ID pipe x 2 m length) gives 60% conversion of A. Commercial plant is to handle 320 m3/h of feed containing 50% A and 50% mole % inserts at 350 deg C and 25 atm for the obtaining 80% conversion of A. i) ii) How many 2 m lengths of 25 mm ID pipe are needed for 80% Conversion. Should they (pipe lengths) be arranged in series or parallel. Solve for ideal Batch reactor and plug flow reactor.
1. The Homogeneous gas phase reaction A-→ 3R, satisfactorily follows second order kinetics. For feed rate of 4 m3/h of pure A at 350 °C and 5 ATM, an experimental reactor (size 25 mm ID pipe x 2 m length) gives 60% conversion of A. Commercial plant is to handle 320 m3/h of feed containing 50% A and 50% mole % inserts at 350 deg C and 25 atm for the obtaining 80% conversion of A. i) ii) How many 2 m lengths of 25 mm ID pipe are needed for 80% Conversion. Should they (pipe lengths) be arranged in series or parallel. Solve for ideal Batch reactor and plug flow reactor.
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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Transcribed Image Text:1. The Homogeneous gas phase reaction A-→ 3R, satisfactorily follows second order
kinetics. For feed rate of 4 m3/h of pure A at 350 °C and 5 ATM, an experimental reactor
(size 25 mm ID pipe x 2 m length) gives 60% conversion of A. Commercial plant is to
handle 320 m3/h of feed containing 50% A and 50% mole % inserts at 350 deg C and 25
atm for the obtaining 80% conversion of A.
i)
ii)
How many 2 m lengths of 25 mm ID pipe are needed for 80% Conversion.
Should they (pipe lengths) be arranged in series or parallel.
Solve for ideal Batch reactor and plug flow reactor.
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