In semi-batch or continuously stirred reactors, often a feed containing one
or more reactants has to be mixed with the contents of the vessel. For fas
t competitive or consecutive reactions the mixing rate of the feed stream w
ith the vessel contents has a large influence on the product quality. The m
ixing rate is often controlled by the turbulent dispersion process. Therefo
re, it has been suggested in the literature to keep the turbulent dispersio
n time constant upon scale-up to obtain a constant product quality. In this
study, based on a combination of a theoretical model, Planar Laser Induced
Fluorescence experiments and Laser Doppler Velocimetry experiments, the tu
rbulent dispersion coefficient is determined. This has been done for the ca
se that a feed stream is mixed in a stirred vessel by a combination of feed
stream and stirrer generated turbulence. The turbulent dispersion coeffici
ent is used to derive an equation for the turbulent dispersion time as func
tion of several design and process variables.