C. 1.74 L/min d. 0.87 L/min e. 0.44 L/min f. 0.21 L/min 8. A 0.5 mol/L glyceride-ester solution in MeOH is fed at 0.07 L/s into a 250 L CSTR in the pilot plant. The catalyst is charged in a separate stream at 0.03 L/s. The generic reaction rate is independent of the concentration of MeOH and can be described by: (-REster) kcat CEster mol/L.S Product stream analysis shows that 37% of the glyceride-ester has reacted. For this system the rate constant kcat is: W a. 2.35E-4 (1/min) b. 0.014 (1/min) V C. 0.019 (1/min) d. 0.027 (1/min) e. 0.055 (1/min) f. 1.1 (1/min)
C. 1.74 L/min d. 0.87 L/min e. 0.44 L/min f. 0.21 L/min 8. A 0.5 mol/L glyceride-ester solution in MeOH is fed at 0.07 L/s into a 250 L CSTR in the pilot plant. The catalyst is charged in a separate stream at 0.03 L/s. The generic reaction rate is independent of the concentration of MeOH and can be described by: (-REster) kcat CEster mol/L.S Product stream analysis shows that 37% of the glyceride-ester has reacted. For this system the rate constant kcat is: W a. 2.35E-4 (1/min) b. 0.014 (1/min) V C. 0.019 (1/min) d. 0.027 (1/min) e. 0.055 (1/min) f. 1.1 (1/min)
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
Related questions
Question
Transcribed Image Text:C.
1.74
L/min
d. 0.87
L/min
e. 0.44
L/min
f.
0.21
L/min
8.
A 0.5 mol/L glyceride-ester solution in MeOH is fed at 0.07 L/s into a 250 L CSTR in the pilot
plant. The catalyst is charged in a separate stream at 0.03 L/s. The generic reaction rate is
independent of the concentration of MeOH and can be described by:
(-REster) kcat CEster mol/L.S
Product stream analysis shows that 37% of the glyceride-ester has reacted. For this system
the rate constant kcat is:
W
a.
2.35E-4
(1/min)
b. 0.014
(1/min)
V
C.
0.019
(1/min)
d. 0.027
(1/min)
e.
0.055
(1/min)
f.
1.1
(1/min)
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