Conditioning In Oleic Acid Flotation

The American Institute of Mining, Metallurgical, and Petroleum Engineers
Nathaniel Arbiter E. K. C. Williams
Organization:
The American Institute of Mining, Metallurgical, and Petroleum Engineers
Pages:
30
File Size:
787 KB
Publication Date:
Jan 1, 1980

Abstract

INTRODUCTION The surface processes involved in preparing ores for flotation and for operations depending on their flocculation/dispersion characteristics * vary widely in agitation dependence. Most of the reagents used for these purposes are added to grinding circuits, pump sumps, launders, or directly to flotation cells with the turbulent flow conditions usually adequate both for mixing reagents and for surface reactions without special conditioners. However, some reagent systems do require specific control of agitation intensities and reaction times, the more important of these being the following: 1. Activation of ZnS with CuSO4. With the usual conditions pH about 10, with collector added with the CuSO4, Cu 2+ is almost completely precipitated as basic compounds and as collector salt. As a result the levels of reagent in solution are extremely low which probably accounts for the need for separate conditioning. The agitation intensities are at about the 0.01 HP/ton level.** 2. Flocculation with natural or synthetic polymers. In this case the agitation problem is two-fold; first, to insure adequate initial mixing of the viscous stock solution of the
Citation

APA: Nathaniel Arbiter E. K. C. Williams  (1980)  Conditioning In Oleic Acid Flotation

MLA: Nathaniel Arbiter E. K. C. Williams Conditioning In Oleic Acid Flotation. The American Institute of Mining, Metallurgical, and Petroleum Engineers, 1980.

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