4) We are planning to operate a batch reactor to convert A into R. This is a liquid reaction, the stoichiometry is A →R, and the rate of reaction is given in Table. How long must we react each batch for the concentration to drop from CAO 1.3 mol/liter to CAf = 0.3 mol/liter? = CA, mol/liter 0.1 0.2 0.3 0.4 0.5 0.6 0.7 0.8 1.0 1.3 - ra, mol/liter min 0.1 0.3 0.5 0.6 0.5 0.25 0.10 0.06 0.05 0.045 0.042 a size of plug flow reactor would be needed for 80% conversion of a feed stream of 1000 mol A/hr at CAO = 1.5 mol/liter?
4) We are planning to operate a batch reactor to convert A into R. This is a liquid reaction, the stoichiometry is A →R, and the rate of reaction is given in Table. How long must we react each batch for the concentration to drop from CAO 1.3 mol/liter to CAf = 0.3 mol/liter? = CA, mol/liter 0.1 0.2 0.3 0.4 0.5 0.6 0.7 0.8 1.0 1.3 - ra, mol/liter min 0.1 0.3 0.5 0.6 0.5 0.25 0.10 0.06 0.05 0.045 0.042 a size of plug flow reactor would be needed for 80% conversion of a feed stream of 1000 mol A/hr at CAO = 1.5 mol/liter?
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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