Studies on impeller type, impeller speed and air flow rate in an industrial scale flotation cell. Part 3: Effect on superficial gas velocity

Superficial gas velocity was measured at different locations in a 2.8 m 3 portable industrial scale sub-aeration flotation cell, treating zinc cleaner feed at Hellyer Concentrator in Tasmania, Australia. The cell was fitted in turn with four different impeller-stator systems, and operated over a ran...

Full description

Saved in:
Bibliographic Details
Published inMinerals engineering Vol. 9; no. 6; pp. 639 - 654
Main Authors Gorain, B.K., Franzidis, J.-P., Manlapig, E.V.
Format Journal Article
LanguageEnglish
Published Oxford Elsevier Ltd 1996
Elsevier Science
Subjects
agitation
Applied sciences
Chemical engineering
Exact sciences and technology
Flotation
flotation bubbles
Froth flotation
Solid-solid systems
agitation
Froth flotation
flotation bubbles
Aeration
Flow velocity
Flow rate
Flotation machine
Online AccessGet full text

Cover

More Information
Summary:Superficial gas velocity was measured at different locations in a 2.8 m 3 portable industrial scale sub-aeration flotation cell, treating zinc cleaner feed at 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. Superficial gas velocity values ranged from 0.29 cm/sec to 6.4 cm/sec at the air flow rates employed. The distribution of air in the cell was very dependent on the impeller type, as well as on the operating conditions in the cell. For a well dispersed condition, the value of superficial gas velocity was uniform at different locations, whereas for flooding conditions the superficial gas velocity was very high near to the impeller and much lower away from the impeller.
ISSN:0892-6875
1872-9444
DOI:10.1016/0892-6875(96)00052-0