Minerals Beneficiation - Effects of Rod Mill Feed Size Reduction

The American Institute of Mining, Metallurgical, and Petroleum Engineers
J. J. Strohl H. J. Schwellenbach
Organization:
The American Institute of Mining, Metallurgical, and Petroleum Engineers
Pages:
2
File Size:
107 KB
Publication Date:
Jan 1, 1951

Abstract

This paper relates the results obtained by decreasing the size of feed to a rod mill screen circuit. As would be expected, added production was gained and a finer grind with no tonnage loss was made possible. THE MacIntyre mill of the National Lead Co. has four parallel sections in which magnetic and gravity separations are made. Ore from a 5000-ton bin is fed by Hardinge constant weight feeders to a 6x12-ft open-end Marcy rod mill in each section. Rod mill discharge is bucket elevated to two 4x10-ft Tyrock screens whose oversize is returned to the rod mill. Screen undersize is pumped to Crockett separators for magnetite removal, and the Crockett tailings are sized and tabled to make an ilmenite concentrate. Minus 200-mesh material, overflowed by the Crockett and Dorrco sizers is thickened, de-slimed, and concentrated by flotation.' By 1948, the development of a successful slime flotation process and numerous improvements in the gravity circuit of the mill had increased the capacity of the available concentrating equipment. At the same time, improvements in the operating techniques of the dry crushing plant and improved feeding of the crusher by the mining department had appreciably increased the production rate per operating hour in that plant. Therefore, it was decided to take advantage of the added crusher capacity to produce a finer rod mill feed and in that way increase grinding capacity. At approximately the same time, finer screens were installed in the rod mill circuits to give finer grind and thus improve liberation of the magnetite and ilmenite from the gangue and from one another. Prior to the first part of 1948, a 3/4-in. limiting screen was used for sizing rod mill feed. The first reduction in crushing plant screen size was to 1/2 in. With this screen, the circulating load in the tertiary crushing circuit was too high and plant capacity dropped below a practical hourly rate. A 9/16-in.-sq opening screen, installed next, proved satisfac-
Citation

APA: J. J. Strohl H. J. Schwellenbach  (1951)  Minerals Beneficiation - Effects of Rod Mill Feed Size Reduction

MLA: J. J. Strohl H. J. Schwellenbach Minerals Beneficiation - Effects of Rod Mill Feed Size Reduction. The American Institute of Mining, Metallurgical, and Petroleum Engineers, 1951.

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