Optimizing Performance at the David Bell Mine Concentrator

Canadian Institute of Mining, Metallurgy and Petroleum
K. Meyer
Organization:
Canadian Institute of Mining, Metallurgy and Petroleum
Pages:
19
File Size:
529 KB
Publication Date:
Jan 1, 1991

Abstract

"The largest cost centres of the David Bell Mine concentrator are grinding, leaching and effluent treatment. Optimizing results during the 6th year of operation are listed below: o SAG mill slurry density control and operating strategies improved liner life and media consumption by 10 and 25%, respectively.o Poly-met liners clad the SAG mill except for the feed end. Lower noise levels and reduced mill downtime have resulted in an improved and more efficient workplace (time required for liner changes is 2 to 3%).o A comparative grinding media study using seven different marked media at the same time showed media wear rates range 120 to 198 mg/kWh and ball mill charge replacement frequencies of 8.3 to 13.1 per year, and that a meaningful wear test must include all media to be tested at the same time in the same mill. High quality carbon steel cylinders had the best economics.o Pre-aeration, using pure gaseous oxygen is accomplished in pipe reactors. Small bubble generators provide oxygen in the first three leach tanks. 1500 to 3000 kg of oxygen is consumed per day. Leach kinetics have improved and trends indicate increases in gold recovery of three to seven ounces per day at reduced costs. Effects of reduced cyanidation of accessory metals on the effluent treatment plant will be discussed in a separate paper."
Citation

APA: K. Meyer  (1991)  Optimizing Performance at the David Bell Mine Concentrator

MLA: K. Meyer Optimizing Performance at the David Bell Mine Concentrator. Canadian Institute of Mining, Metallurgy and Petroleum, 1991.

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