Abstract
A three-phase model of froth flotation, consisting of a pulp and two distinct froth phases, is developed for describing mass transport in flotation cells. Methods are proposed for estimating the various rate coefficients contained in the model. A comparison of predictions with experimental data for china clay demonstrates that the model can successfully predict the pulp phase kinetics, as well as kinetics of solid drainage from froth and product recovery, over a wide range of froth depth, 0.12 m to 0.46 m.
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