7. The hydrolysis of propylene oxide ('po' Mw 58) to propylene glycol ('pg' Mw 76) is scaled up to a 10 m³ agitated reactor. The proposed process is to charge 2100kg of 30wt% PO in to 6000 kg of a water and catalyst mixture in the vessel. The density of all fluids is 1000 the reaction rate is given by: kg m ། po+water →pg (-Rpo) = 0.7 [po] mol/L.s To limit the temperature in the vessel, the reaction rate may exceed 0.0001 mol/L.s; The maximum addition rate for the process is: a. 6.96 L/min v b. 3.48 L/min C. 1.74 L/min d. 0.87 L/min e. 0.44 L/min f. 0.21 L/min
7. The hydrolysis of propylene oxide ('po' Mw 58) to propylene glycol ('pg' Mw 76) is scaled up to a 10 m³ agitated reactor. The proposed process is to charge 2100kg of 30wt% PO in to 6000 kg of a water and catalyst mixture in the vessel. The density of all fluids is 1000 the reaction rate is given by: kg m ། po+water →pg (-Rpo) = 0.7 [po] mol/L.s To limit the temperature in the vessel, the reaction rate may exceed 0.0001 mol/L.s; The maximum addition rate for the process is: a. 6.96 L/min v b. 3.48 L/min C. 1.74 L/min d. 0.87 L/min e. 0.44 L/min f. 0.21 L/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
![7.
The hydrolysis of propylene oxide ('po' Mw 58) to propylene glycol ('pg' Mw 76) is scaled up
to a 10 m³ agitated reactor. The proposed process is to charge 2100kg of 30wt% PO in to
6000 kg of a water and catalyst mixture in the vessel. The density of all fluids is 1000
the reaction rate is given by:
kg
m
།
po+water →pg (-Rpo) = 0.7 [po] mol/L.s
To limit the temperature in the vessel, the reaction rate may exceed 0.0001 mol/L.s;
The maximum addition rate for the process is:
a. 6.96
L/min v
b. 3.48
L/min
C.
1.74
L/min
d. 0.87
L/min
e. 0.44
L/min
f. 0.21
L/min](/v2/_next/image?url=https%3A%2F%2Fcontent.bartleby.com%2Fqna-images%2Fquestion%2Fbc5a7f44-f883-4cf2-8c1e-fbb6272dba60%2F1db378a9-d222-4934-a9f0-f8e58c1e9078%2Frbv2zu_processed.jpeg&w=3840&q=75)
Transcribed Image Text:7.
The hydrolysis of propylene oxide ('po' Mw 58) to propylene glycol ('pg' Mw 76) is scaled up
to a 10 m³ agitated reactor. The proposed process is to charge 2100kg of 30wt% PO in to
6000 kg of a water and catalyst mixture in the vessel. The density of all fluids is 1000
the reaction rate is given by:
kg
m
།
po+water →pg (-Rpo) = 0.7 [po] mol/L.s
To limit the temperature in the vessel, the reaction rate may exceed 0.0001 mol/L.s;
The maximum addition rate for the process is:
a. 6.96
L/min v
b. 3.48
L/min
C.
1.74
L/min
d. 0.87
L/min
e. 0.44
L/min
f. 0.21
L/min
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