Filtration And Control Of Moisture Content On Taconite Concentrates

The American Institute of Mining, Metallurgical, and Petroleum Engineers
Henderson C. F. Cornell A. F. Dunyon D. A. Dahlstrom
Organization:
The American Institute of Mining, Metallurgical, and Petroleum Engineers
Pages:
7
File Size:
573 KB
Publication Date:
Jan 3, 1957

Abstract

IN processing magnetic taconites several steps of crushing, grinding, classification, and magnetic separation are required to produce a 60+ pct Fe concentrate. Usually the final concentrate is in a slurry form of 55 to 70 pct solids by weight and is further characterized by a particle size of 60+ pct -325 mesh. In taconite plants already completed or under construction the conventional method used to obtain pellets suitable for blast furnaces is to filter the concentrate slurry, ball the filter cake, and then harden the green pellets in a traveling grate or in a vertical shaft furnace. Large tonnages must be handled in minimum floor space, with reduced maintenance and lowest possible operating cost. Filtration must therefore achieve two objectives: 1) high filtration rate-in terms of pounds of dry solids per hour per square foot of filtration area-at a low filtrate solids concentration, and 2) a filter cake moisture that will always permit efficient balling within the normal fluctuations of plant operating conditions. If moisture contents are too high, balling may be impossible or result in a mushy ball without enough green strength for the firing operation.
Citation

APA: Henderson C. F. Cornell A. F. Dunyon D. A. Dahlstrom  (1957)  Filtration And Control Of Moisture Content On Taconite Concentrates

MLA: Henderson C. F. Cornell A. F. Dunyon D. A. Dahlstrom Filtration And Control Of Moisture Content On Taconite Concentrates. The American Institute of Mining, Metallurgical, and Petroleum Engineers, 1957.

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