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Improving the recovery of coarse coal particles in a Jameson cell
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Minerals Engineering 19 (2006) 609–618Improving the recovery of coarse coal particles in a Jameson cell
J. Cowburn a,*, G. Harbort b, E. Manlapig b, Z. Pokrajcic a
a Xstrata Technology, Level 2, 87 Wickham Terrace Spring Hill, Brisbane, QLD 4000, Australia
b Julius Kruttschnitt Mineral Research Centre, Isles Road, Indooroopilly, OLD 4069, Australia
Received 11 July 2005; accepted 6 September 2005
Available online 24 October 2005Abstract
It has been observed in several Jameson cell installation where the source for flotation feed is deslime screens, that the recovery of coal
particles greater than 0.5 mm is not as great as that of finer material. Consequently, a research project was undertaken at a CHPP in the
Bowen Basin Queensland to assess the possibility of increasing the recovery of coarser particles (+0.5 mm) within the downcomer of the
Jameson cell. The effect of decreasing turbulence and agitation in a commercial-scale downcomer was investigated to assess the effect on
the recovery of both coarse and fine coal particles.
This paper details the findings of the test work, summarising the results relating to differences in the operating parameters within the
downcomer.
2005 Elsevier Ltd. All rights reserved.
Keywords: Coal; Froth flotation and particle size1. Introduction
Coal flotation has been active in Australia since 1970
when there were 16 mechanically agitated cells in operation
(Post, 1975). However, it was not until 1990 that it became
widely accepted as an economical method of treating fine
coal. The first Jameson cell was installed at Newlands Coal
Handling and Preparation Plant (CHPP) in 1990 treating
coal slimes. Since that time the Jameson cell flotation
machine has become the recognised technology in Austra-
lia for fine coal flotation with 90 cells installed in Australia
and 115 worldwide (Xstrata Technology Website). The
Jameson cell is a high intensity flotation device, which uti-
lises
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