A kinetic model for the prediction of the performance of a froth flota
tion cell is proposed. The model is based on the assumption of a free-
flowing concentrate froth. The flux of bubble surface is estimated fro
m the cell aeration rate and the specific surface of the bubbles in th
e froth. The specific surface in the froth is based on the mean bubble
size which is estimated by off-line image processing of photographs t
aken of the froth during laboratory scale batch tests. A sequence of b
atch flotation tests in which a low-rank UK coal was demineralized, by
varying the initial addition of Sodium Dodecyl Sulphate (SDS), was us
ed to test the consistency of the model predictions with experimental
data. Although all the model parameters have a physical reality, not a
ll were able to be measured at this stage. Nevertheless, the consisten
cy of the predictions with the experimental data was encouraging, and
the potential value of extended on-line image processing as a tool for
improved experimentation was apparent.