The off gas from a boiling water nuclear power reactor contains a whole variety of radioactive trash, one of the most troublesome being Xe-133 (half life = 5.2 days). This off gas flows continuously through a large holdup tank in which its mean residence time is 30 days, and where we can assume that the contents are well mixed. Find the fraction of activity removed in the tank.

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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The off gas from a boiling water nuclear power reactor contains a whole
variety of radioactive trash, one of the most troublesome being Xe-133
(half life = 5.2 days). This off gas flows continuously through a large holdup
tank in which its mean residence time is 30 days, and where we can assume
that the contents are well mixed. Find the fraction of activity removed in
the tank.
A specific enzyme acts as catalyst in the fermentation of reactant A. At a
given enzyme concentration in the aqueous feed stream (25 liter/min) find
the volume of plug flow reactor needed for 95% conversion of reactant
A (CA02 mol/liter). The kinetics of the fermentation at this enzyme
concentration is given by
A
enzyme
R,
-A=
0.1 CA
1+0.5 CA
mol
liter.min
Transcribed Image Text:The off gas from a boiling water nuclear power reactor contains a whole variety of radioactive trash, one of the most troublesome being Xe-133 (half life = 5.2 days). This off gas flows continuously through a large holdup tank in which its mean residence time is 30 days, and where we can assume that the contents are well mixed. Find the fraction of activity removed in the tank. A specific enzyme acts as catalyst in the fermentation of reactant A. At a given enzyme concentration in the aqueous feed stream (25 liter/min) find the volume of plug flow reactor needed for 95% conversion of reactant A (CA02 mol/liter). The kinetics of the fermentation at this enzyme concentration is given by A enzyme R, -A= 0.1 CA 1+0.5 CA mol liter.min
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