Column Flotation Operation at Mines Gaspé Molybdenum Circuit

Canadian Institute of Mining, Metallurgy and Petroleum
T. Cienski V. Coffin
Organization:
Canadian Institute of Mining, Metallurgy and Petroleum
Pages:
23
File Size:
547 KB
Publication Date:
Jan 1, 1981

Abstract

"(Figure 1) Reagentized pulp enters into the column at about 1/4 of the distance from the top. Inside the column it meets with a downward flowing stream of water and with an upward flowing mass of air bubbles. Flotation takes place in this counter current system while at the same time fine gangue particles are washed off the froth before it reaches the overflow lip at the top of the column. The main operating features of the column flotation are as follows:a) No moving parts. Solids are kept in suspention not by an agitating action of a propeller but by settling down against the rising air bubbles.b) Wash water. Spray pipes are installed a few inches below the froth surface and deliver required volume of water. The purpose of this water is twofold:(i) it keeps in balance the flow of material through the column and(ii) it washes rising froth in the froth layer as well as removes unwanted fines attached to the bubbles at the lower flotation section. As a result the concentrate produced is of higher purity than in the conventional flotation. Column is characterized by very high up-grading. However, even temporary disruption of wash water supply results in a drastic drop of concentrate grate.c) Flow balance. (Figure 2) For the correct operation volume of the underflow (tail) is larger than that of the feed. The difference is made up by the wash water. This difference called bias is predetermined and ranges from some 4 to 15 USGPM depending on the size of the unit and process requirements."
Citation

APA: T. Cienski V. Coffin  (1981)  Column Flotation Operation at Mines Gaspé Molybdenum Circuit

MLA: T. Cienski V. Coffin Column Flotation Operation at Mines Gaspé Molybdenum Circuit. Canadian Institute of Mining, Metallurgy and Petroleum, 1981.

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