Case Studies on the Performance and Characterisation of the Froth Phase in Industrial Flotation Circuits

The Australasian Institute of Mining and Metallurgy
S R. Grano M Vera
Organization:
The Australasian Institute of Mining and Metallurgy
Pages:
8
File Size:
214 KB
Publication Date:
Jan 1, 2005

Abstract

This paper deals with two separate case studies investigating the froth phase performance and characterisation of two industrial rougher/ scavenger flotation circuits. Froth phase performance was quantified using a mass balance approach to estimate froth zone recovery. Measured characteristics of the froth phase included frother solution concentration determined by gas chromatography, and the time taken for an equilibrium froth sample to decay to one-half of its original froth height. The latter measurement is referred to as the æfroth half-lifeÆ and is strongly linked to froth stability. Special methods and techniques developed to preserve frother in solution and to measure froth half-life are briefly described. The frother type in the first case study was a mixture of straight and branched alcohols, whilst the frother type in the second case study was a mixture of alcohols, aldehydes and triethoxybutane. The first case study focussed on a flotation circuit treating a low-grade ore containing only a small fraction of floatable copper sulfide minerals, while the second case study focussed on a flotation circuit treating a higher grade complex sulfide ore containing significant quantities of chalcopyrite, galena, sphalerite and pyrite. It was found that froth zone recovery of valuable mineral generally decreased down-the-bank of the two industrial rougher/scavenger circuits. Moreover, decreases in froth zone recovery significantly limit the overall cell recovery of valuable mineral achievable from the plant scavenger cells. However, the decrease in froth zone recovery could not be linked to the removal of frother from the pulp solution to the concentrate product in the preceding rougher flotation stages. Measurements of residual frother in solution suggested that, approximately, only five to ten per cent of the added frother was removed into the rougher/scavenger concentrate, with the remainder appearing in the scavenger tailings. This finding suggested there was apparently adequate frother in solution in the scavenger stages.
Citation

APA: S R. Grano M Vera  (2005)  Case Studies on the Performance and Characterisation of the Froth Phase in Industrial Flotation Circuits

MLA: S R. Grano M Vera Case Studies on the Performance and Characterisation of the Froth Phase in Industrial Flotation Circuits. The Australasian Institute of Mining and Metallurgy, 2005.

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