Recent Development In Processing Of Oxide And Refractory Gold Ores

- Organization:
- Society for Mining, Metallurgy & Exploration
- Pages:
- 6
- File Size:
- 1252 KB
- Publication Date:
- Jan 1, 2000
Abstract
After more than 100 years, alkaline cyanide leaching of gold and silver ores, either directly in the case of oxidized ores, or after pretreatment of refractory ores by roasting, pressure leaching or bacterial leaching, remains the dominant
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leaching method to extract the precious metals f om ores.
Leaching with halides (chlorine, bromine and iodine) and with thiourea and thiosulfates is less common but practiced in some cases to dissolve the precious metals both from ores and jewelry and electronic scrap.
Cyanide solutions can contain from 1 ppm Au to 30,000 ppm Au. According to the source, i.e., agitated tank leaching, heap leaching, eluates from stripping activated carbon or waste electroplating solutions. Similar variations occur with silver which can have a profound influence on the recovery method. The presence of other elements in the leach solutions, particularly mercury and copper, likewise play an important role in the procedures required to recover the gold
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and silver values f om solution.
The same circumstances are found when lixivants other than cyanide are used to dissolve the precious metals.
For decades, the preferred method of recovering gold and silver values from alkaline cyanide leach solutions was by zinc dust precipitation according to the Merrill Crowe process developed in the late 19th century. Finely ground gold and silver ores or concentrates were either leached directly or after roasting, in agitated tanks or Pachucas and subjected to solid/liquid separation by filtering or by treatment in counter-current-decantation washing thickeners (CCD). This solid/liquid separation step was often very difficult especially when ores containing high quantities of clay were treated which caused filtration or thickening problems.
Following testing and development by the U.S. Bureau of Mines (USBM) in the late 60s, the introduction of carbonin-leach (CIL) or carbon-in-pulp (CIP) plants to recover gold and silver from leach pulps was one of the greatest operational and cost saving improvements made in the industry in South Dakota and quickly spread around the world to be the most common process to recover gold and silver from cyanide solutions.
Citation
APA:
(2000) Recent Development In Processing Of Oxide And Refractory Gold OresMLA: Recent Development In Processing Of Oxide And Refractory Gold Ores . Society for Mining, Metallurgy & Exploration, 2000.