T (s) 14 25 29 30 27 24 25 12 CA0, mol/dm³ 200 190 180 170 150 140 120 110 CA. mol/dm³ 100 90 80 70 50 40 20 10
T (s) 14 25 29 30 27 24 25 12 CA0, mol/dm³ 200 190 180 170 150 140 120 110 CA. mol/dm³ 100 90 80 70 50 40 20 10
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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question a) already being answered as in the picture. i want to understand how to get answered for question b)
a) Using data from Table 2, suggest the best single flow reactor (either CSTR or PFR) for 85% conversion when the feed rate consists of 100 mol/dm3 of n-pentane. Justify your answer (answer in pic)
b) If two-reactor scheme to be installed in the system, proposed the best reactorarrangement for the same conversion in (a) that give optimum condition. Justifyyour answer. Hint: Determine the concentration of reactant between stages at minimum reaction rate (please explain how to answer b)
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