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A gas phase consistent system has a reaction of A → 3R satisfactorily follows second order kinetics. For a feed rate of 6 m3/h of pure A at 350°C and 5 atm, an experimental reactor ( ID pipe x 2.5 m length) gives 60% conversion of feed. A commercial plant is to handel 325 m³/h of feed with 50 mole % of A with inerts as remaining at 3500C and 25 atm for A to remain at 20%. a) How many 25 mm ID pipe are required? b) What is the best arrangement, parallel or in series. ( 25 mm Assume that the plug flow in pipe is in ideal gas behavior.

A gas phase consistent system has a reaction of A → 3R satisfactorily follows second order kinetics. For a feed rate of 6 m3/h of pure A at 350°C and 5 atm, an experimental reactor ( ID pipe x 2.5 m length) gives 60% conversion of feed. A commercial plant is to handel 325 m³/h of feed with 50 mole % of A with inerts as remaining at 3500C and 25 atm for A to remain at 20%. a) How many 25 mm ID pipe are required? b) What is the best arrangement, parallel or in series. ( 25 mm Assume that the plug flow in pipe is in ideal gas behavior.

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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A gas phase consistent system has a reaction of A → 3R satisfactorily follows second order kinetics. For a feed rate of 6 m3/h of pure A at 350°C and 5 atm, an experimental reactor ( ID pipe x 2.5 m length) gives 60% conversion of feed. A commercial plant is to handel 325 m³/h of feed with 50 mole % of A with inerts as remaining at 3500C and 25 atm for A to remain at 20%. a) How many 25 mm ID pipe are required? b) What is the best arrangement, parallel or in series. ( 25 mm Assume that the plug flow in pipe is in ideal gas behavior.
Transcribed Image Text:A gas phase consistent system has a reaction of A → 3R satisfactorily follows second order kinetics. For a feed rate of 6 m3/h of pure A at 350°C and 5 atm, an experimental reactor ( ID pipe x 2.5 m length) gives 60% conversion of feed. A commercial plant is to handel 325 m³/h of feed with 50 mole % of A with inerts as remaining at 3500C and 25 atm for A to remain at 20%. a) How many 25 mm ID pipe are required? b) What is the best arrangement, parallel or in series. ( 25 mm Assume that the plug flow in pipe is in ideal gas behavior.
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