EFFLUENT TRACER CONCENTRATION AS A FUNCTION OF TIME 0 1 2 3 4 5 6 7 8 9 10 12 TABLE E18-1.1 t (min) 14 E (mg/L) 8 6 4 3 2.2 1.5 0.6 8. 10
EFFLUENT TRACER CONCENTRATION AS A FUNCTION OF TIME 0 1 2 3 4 5 6 7 8 9 10 12 TABLE E18-1.1 t (min) 14 E (mg/L) 8 6 4 3 2.2 1.5 0.6 8. 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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Conversion Using Dispersion and Tanks-in-Series Models
The first-order reaction
A ⎯⎯→B
is carried out in a 10-cm-diameter tubular reactor 6.36 m in length. The specific reaction rate is 0.25 min-1. The results of a tracer test carried out on this reactor are shown in Table E18-1.1.Calculate the conversion using (a) the closed vessel dispersion model, (b) PFR,(c) the tanks-in-series model, and (d) a single CSTR.
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