A liquid phase rxn A → 2.5 B occurred in a one-hundred liter constant temperature Continuously Stirred Tank Reactor and obeys the rate law given below. At first, it is charged with 1.75 mM reactant A that is pure with a rate of 2 liters/minute. -r₁=kC k - "A A Note that the "k" constant depends on temperature based on Arrhenius Law: 1.25 L0.25 molo.25 min -1.525 1,000e T The temperature operation of the reactor is 52°C. Determine the concentration at steady-state of both A and B.

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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Topic: Conversion and Reactor Sizing

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A liquid phase rxn A → 2.5 B occurred in a one-hundred liter constant temperature Continuously
Stirred Tank Reactor and obeys the rate law given below. At first, it is charged with 1.75 mM
reactant A that is pure with a rate of 2 liters/minute.
r
k
=kC
=
A
A
Note that the "k" constant depends on temperature based on Arrhenius Law:
1.25
10.25
molo.25 min
-1,525
1,000e T
The temperature operation of the reactor is 52°C. Determine the concentration at steady-state of
both A and B.
Transcribed Image Text:A liquid phase rxn A → 2.5 B occurred in a one-hundred liter constant temperature Continuously Stirred Tank Reactor and obeys the rate law given below. At first, it is charged with 1.75 mM reactant A that is pure with a rate of 2 liters/minute. r k =kC = A A Note that the "k" constant depends on temperature based on Arrhenius Law: 1.25 10.25 molo.25 min -1,525 1,000e T The temperature operation of the reactor is 52°C. Determine the concentration at steady-state of both A and B.
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