Abstract
In any form of continuous reactor the different reagent molecules spend different
residence times in the reacting zone. The degree to which a reaction advances after
a lapse of nominal residence time may be somewhat different from that expected from
classical (micro) kinetics and the known order of the reaction.
If the reaction mixture passes laminarly through a reasonably large cylindrical
reactor-one in which intermolecular diffusion is negligible-the effective measure
of the advancement of the reaction in terms of the residual concentration of the reagent - measured (i) as an actual distributed system C and (ii) as an idealized system in which
all molecules spend an equal tlme of residence Cm. may be expressed by the equation:
Equation (29)
where n is order of reaction, S=knC0n-1τ0, and τ0 is the minimal time of residence (time
for the central core).
Equation (29) becomes meaningless when n=1 and is replaced by
Equation (30)
The ratio C/Cm increases as S increases; the increase, however, is the less pronounced
the higher the value of n.
If the mixture passes through a mixed tank reactor advancement of the degree of
the reaction is measured by a function given by Metzner and Pigford. For a second
order of reaction a correct treatment can only be carried out if a distinction is made
between the square on the mean concentration and the mean of the square concentration.
Cited by
2 articles.
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