27.4. Carbohydrate A decomposes in the presence of enzyme E. We also suspect that carbohydrate B in some way influences this decomposition. To study this phenomenon various concentrations of A, B, and E flow into and out of a mixed flow reactor (V = 240 cm³). (a) From the following data find a rate equation for the decomposition. (b) What can you say about the role of B in the decomposition? (c) Can you suggest a mechanism for this reaction? %3D CA0, mol/m3 CA, mol/m³ CB0, mol/m CE0, mol/m³ v, cm³/min 200 50 12.5 80 5 24 900 1200 300 800 5 48 700 33.3 33.3 33.3 24 200 80 33.3 10 80 900 500 33.3 20 120
27.4. Carbohydrate A decomposes in the presence of enzyme E. We also suspect that carbohydrate B in some way influences this decomposition. To study this phenomenon various concentrations of A, B, and E flow into and out of a mixed flow reactor (V = 240 cm³). (a) From the following data find a rate equation for the decomposition. (b) What can you say about the role of B in the decomposition? (c) Can you suggest a mechanism for this reaction? %3D CA0, mol/m3 CA, mol/m³ CB0, mol/m CE0, mol/m³ v, cm³/min 200 50 12.5 80 5 24 900 1200 300 800 5 48 700 33.3 33.3 33.3 24 200 80 33.3 10 80 900 500 33.3 20 120
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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Transcribed Image Text:27.4. Carbohydrate A decomposes in the presence of enzyme E. We also suspect
that carbohydrate B in some way influences this decomposition. To study
this phenomenon various concentrations of A, B, and E flow into and out
of a mixed flow reactor (V = 240 cm³).
(a) From the following data find a rate equation for the decomposition.
(b) What can you say about the role of B in the decomposition?
(c) Can you suggest a mechanism for this reaction?
CA0, mol/m³ CA, mol/m³ CBo, mol/m³ CE0, mol/m³
v,
cm³/min
200
50
12.5
80
900
300
5
24
1200
800
5
48
700
33.3
33.3
33.3
24
200
80
33.3
10
80
900
500
33.3
20
120
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