1.0 TCSTR ,==1 min Tk = 1 m/kmol and C =1 kmol/m TPFR TPFR (1) (1)3

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
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Comparing Second-Order Reaction Systems
Consider a second-order reaction being carried out in a real CSTR that can be modeled as two different reactor systems: In the first system an ideal CSTR is followed by an ideal PFR (Figure E16-3.1); in the second system the PFR precedes the CSTR (Figure E16-3.2). To simplify the calculations, let τs and τp each equal 1 min, let the reaction rate constant equal 1.0 m3/kmol
min, and let the initial concentration of liquid reactant, CA0, equal 1.0 kmol/m3. Find the conversion in each system.
For the parameters given, we note that in these two arrangements (see Figures E16-3.1 and E16-3.2), the RTD function, E(t), is the same

1.0
TCSTR
,==1 min
Tk = 1 m/kmol and
C =1 kmol/m
TPFR
TPFR
(1)
(1)3
Transcribed Image Text:1.0 TCSTR ,==1 min Tk = 1 m/kmol and C =1 kmol/m TPFR TPFR (1) (1)3
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