Controlling CaCO Scale on Activated Carbon Improves Gold Recovery and Operating Costs

Society for Mining, Metallurgy & Exploration
Terry Mattioli Larry G. Nisle Terry Fagg Buck Bradshaw
Organization:
Society for Mining, Metallurgy & Exploration
Pages:
6
File Size:
894 KB
Publication Date:
Jan 1, 1990

Abstract

Deposition of calcium carbonate scale on activated carbon in the Pinson Mining mill carbon column circuit was causing erratic gold recovery rate, long acid wash time, high carbon attrition and long strip times. Continuous addition of a blended antiscalant into the mill thickener overflow at 8 ppm reduced the average carbon acid wash weight loss from approximately 10% to < 2%. Cleaner carbon improved the gold loading rate in the mill column. The loading on Column I was increased to 175-225 oz/ton carbon from 125-150 oz/ton for a two-day carbon advance cycle. The higher loading capability has given Pinson more flexibility and better control of gold flow through their carbon adsorption, stripping and electrowin­ning processes. Preventing calcium carbonate build-up on activated carbon with this antiscalant reduced acid wash batch time. This enabled Pinson to acid wash and regenerate every batch of stripped carbon for all the adsorption circuits. Shorter strip times have also resulted from the lowering of the calcium carbonate scale level in the loaded carbon. Carbon consumption has been reduced and is now averaging 0.046 lb/ton ore for the first six months of 1990 compared to 0.072 and 0.083 lb/ton respectively in 1989 and 1988.
Citation

APA: Terry Mattioli Larry G. Nisle Terry Fagg Buck Bradshaw  (1990)  Controlling CaCO Scale on Activated Carbon Improves Gold Recovery and Operating Costs

MLA: Terry Mattioli Larry G. Nisle Terry Fagg Buck Bradshaw Controlling CaCO Scale on Activated Carbon Improves Gold Recovery and Operating Costs . Society for Mining, Metallurgy & Exploration, 1990.

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