Title of article
Optimization of operating parameters for coarse sphalerite flotation in the HydroFloat fluidised-bed separator
Author/Authors
Awatey، نويسنده , , Bellson and Thanasekaran، نويسنده , , Homie and Kohmuench، نويسنده , , Jaisen N. and Skinner، نويسنده , , William and Zanin، نويسنده , , Massimiliano، نويسنده ,
Issue Information
روزنامه با شماره پیاپی سال 2013
Pages
7
From page
99
To page
105
Abstract
Increasing the upper size limit of coarse particle flotation has been a long-standing challenge in the minerals processing industry. The HydroFloat separator, an air-assisted fluidised-bed separator, has been used in this study to float 250–1180 μm sphalerite particles in batch flotation tests and compared to results achieved utilizing a laboratory-scale conventional Denver cell. The quiescent environment within the HydroFloat cell significantly reduces the turbulent energy dissipation within the collection zone, hence decreasing the detachment of particles from bubbles during flotation. Three operating parameters including bed-level, superficial water and gas rates have been studied, and their effect on the flotation of coarse sphalerite particles is reported. It is shown that coarse sphalerite recovery increases with increasing bed-level, superficial water and gas flow rates. However, there are thresholds for each operating parameter above which recovery starts to decrease. A comparison of recovery with a conventional Denver flotation cell indicates that the HydroFloat separator vastly outperforms the conventional flotation machine for the very coarse particles (+425 μm), and this is mainly attributable to the absence of turbulence and the minimization of a froth zone, both of which are detrimental to coarse particle flotation.
Keywords
Flotation , Fluidised bed , Coarse Particles , HydroFloat , Teeter bed
Journal title
Minerals Engineering
Serial Year
2013
Journal title
Minerals Engineering
Record number
2277098
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