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The elementary gas-phase reaction 2A → B is carried out in a constant-volume batch reactor where 50% conversion is achieved in I hour. Pure A is charged to the reactor at an initial concentration of 0.2 mol/dm³. If the same reaction is carried out in a CSTR, what volume would be necessary to achieve 50% conversion for a feed molar flow rate of 500 mol/h and an entering concentration of A of 0.2 mol/dm?? (Ans.: V = 5,000 dm)

The elementary gas-phase reaction 2A → B is carried out in a constant-volume batch reactor where 50% conversion is achieved in I hour. Pure A is charged to the reactor at an initial concentration of 0.2 mol/dm³. If the same reaction is carried out in a CSTR, what volume would be necessary to achieve 50% conversion for a feed molar flow rate of 500 mol/h and an entering concentration of A of 0.2 mol/dm?? (Ans.: V = 5,000 dm)

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
Problem 1.1P
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P5-5, The elementary gas-phase reaction 2A → B is carried out in a constant-volume batch reactor where 50% conversion is achieved in 1 hour. Pure A is charged to the reactor at an initial concentration of 0.2 mol/dm. If the same reaction is carried out in a CSTR, what volume would be necessary to achieve 50% conversion for a feed molar flow rate of 500 mol/h and an entering concentration of A of 0.2 mol/dm? (Ans.: V = 5,000 dm³)
Transcribed Image Text:P5-5, The elementary gas-phase reaction 2A → B is carried out in a constant-volume batch reactor where 50% conversion is achieved in 1 hour. Pure A is charged to the reactor at an initial concentration of 0.2 mol/dm. If the same reaction is carried out in a CSTR, what volume would be necessary to achieve 50% conversion for a feed molar flow rate of 500 mol/h and an entering concentration of A of 0.2 mol/dm? (Ans.: V = 5,000 dm³)
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