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The elementary liquid-phase reaction k A + 2B R k2 with rate equation mol -B = (12.5 liter²/mol?- min)C,C - (1.5 min-1)CR, %3D -TA = liter min

The elementary liquid-phase reaction k A + 2B R k2 with rate equation mol -B = (12.5 liter²/mol?- min)C,C - (1.5 min-1)CR, %3D -TA = liter min

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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The elementary liquid-phase reaction A + 2B R k2 with rate equation mol -TA = TB (12.5 liter/mol? min)CAC - (1.5 min-1)CR, liter min is to take place in a 6-liter steady-state mixed flow reactor. Two feed streams, one containing 2.8 mol A/liter and the other containing 1.6 mol B/liter, are to be introduced at equal volumetric flow rates into the reactor, and 75% conversion of limiting component is desired (see Fig. E5.3). What should be the flow rate of each stream? Assume a constant density throughout. CÁo = 2.8 mol A/liter C30 = 1.6 mol B/liter VA = UB = U 75% conversion of B V = 6 liter Figure E5.3
Transcribed Image Text:The elementary liquid-phase reaction A + 2B R k2 with rate equation mol -TA = TB (12.5 liter/mol? min)CAC - (1.5 min-1)CR, liter min is to take place in a 6-liter steady-state mixed flow reactor. Two feed streams, one containing 2.8 mol A/liter and the other containing 1.6 mol B/liter, are to be introduced at equal volumetric flow rates into the reactor, and 75% conversion of limiting component is desired (see Fig. E5.3). What should be the flow rate of each stream? Assume a constant density throughout. CÁo = 2.8 mol A/liter C30 = 1.6 mol B/liter VA = UB = U 75% conversion of B V = 6 liter Figure E5.3
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