Studies on impeller type, impeller speed and air flow rate in an industrial scale flotation cell — Part 1: Effect on bubble size distribution

• Published in: Minerals engineering Vol. 8; no. 6; pp. 615 - 635
• Main Authors: Gorain, B.K, Franzidis, J.-P, Manlapig, E.V
• Format: Journal Article
• Language: English
• Published: Elsevier Ltd 1995
• Subjects: aeration rate; Agitair Chile-X impeller; Agitair Pipsa impeller; Bubble size distribution; Dorr-Oliver impeller; impeller speed; Industrial flotation cell; Outokumpu impeller; Industrial flotation cell; Outokumpu impeller; Agitair Chile-X impeller; Bubble size distribution; Agitair Pipsa impeller; aeration rate; impeller speed; Dorr-Oliver impeller
• ISSN: 0892-6875; 1872-9444
• DOI: 10.1016/0892-6875(95)00025-L

Bubble size distributions were measured at different locations in a 2.8 m 3 portable industrial scale sub-aeration flotation cell, treating zinc cleaner feed in the Hellyer Concentrator in Tasmania, Australia. The cell was fitted in turn with four different impeller-stator systems, and operated over a range of air flow rates and impeller speeds. The mean bubble size was found to increase with increase in air flow rate at different locations in the cell, for all four impellers, and to decrease with increase in impeller speed. The mean bubble size was largest close to the impeller shaft and smallest at the impeller discharge point, for all the impellers. The shape of the bubble size distribution also changed with location in the cell. The “global mean” bubble size calculated by simple arithmetic average of the values at six locations in the cell coincided remarkably well with the mean bubble size measured halfway between the impeller shaft and the side of the cell, at the top of the pulp. In general, the impellers produced “global mean” values of 1.0 mm or less at the manufacturer's recommended impeller speed.