An existing stirred-tank reactor is to be used for a 2nd-order liquid phase reaction. A tracer injection led to the following data below: Where C is concentration in moles/L and t is the time in seconds. If the reaction has been found to give 90% conversion in 600 seconds in a batch reactor with CAo=0.5 mol/L, estimate the conversion that can be achieved in the stirred-tank reactor that gave the tracer data shown above using the complete segregation model. Assume the same inlet concentration as in the batch reactor.
An existing stirred-tank reactor is to be used for a 2nd-order liquid phase reaction. A tracer injection led to the following data below: Where C is concentration in moles/L and t is the time in seconds. If the reaction has been found to give 90% conversion in 600 seconds in a batch reactor with CAo=0.5 mol/L, estimate the conversion that can be achieved in the stirred-tank reactor that gave the tracer data shown above using the complete segregation model. Assume the same inlet concentration as in the batch reactor.
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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An existing stirred-tank reactor is to be used for a 2nd-order liquid phase reaction. A tracer injection led to the following data below:
Where C is concentration in moles/L and t is the time in seconds. If the reaction has been found to give 90% conversion in 600 seconds in a batch reactor with CAo=0.5 mol/L, estimate the conversion that can be achieved in the stirred-tank reactor that gave the tracer data shown above using the complete segregation model. Assume the same inlet concentration as in the batch reactor.
Transcribed Image Text:A tracer injection led to the following data:
T
0
300
360
60 120 180 240
8
5
10
8
6
4
420 480 540 600 720 840
C 0 1
3 2.2 1.5 0.6 0
Where C is concentration in moles/L and t is the time in seconds. If the reaction has been found
to give 90% conversion in 600 seconds in a batch reactor with CAO=0.5 mol/L, estimate the
conversion that can be achieved in the stirred-tank reactor that gave the tracer data shown above
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