Thermophilic microbial treatment of precious metal ores
AssigneeAdvanced Mineral Technologies, Inc.
InventorsStephen R. Hutchins, Michael S. Davidson, James A. Brierley, Corale L. Brierley
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Abstract
A method is provided for the recovery of precious metals, such as gold and silver, from refractory sulfidic material and refractory carbonaceous sulfidic material. The sulfidic material is pulped and bioleached using either facultative or obligate thermophiles at temperatures in excess of about 45.degree. C. and ranging up to about 90.degree. C. The residue remaining from the bioleach is neutralized and washed and the precious metals therein recovered by dissolution.
Claims19
A method for recovering precious metals from particulate refractory mineral sulfides in which at least one precious metal is occluded within the sulfide particulate which impedes the recovery of precious metals therefrom by direct leaching which comprises:
- bioleaching a mineral sulfide containing said occluded precious metal with an aqueous solution containing at least one facultative or obligate thermophile capable of promoting the oxidation of said mineral sulfide,
- said bioleaching being carried out at a temperature of at least about 45.degree. C. but not exceeding that temperature above which the thermophile is degraded,
- said bioleaching being carried out in the presence of nutrients specific to the growth of said thermophile for a time at least sufficient to oxidize said sulfide mineral and liberate said precious metal and provide a residue containing said liberated precious metal in recoverable form,
- separating said precious-metal-containing residue from said bioleach solution,
- washing said residue, and then leaching said precious-metal-containing residue with an aqueous leach solution selective to the dissolution of said liberated precious metal and provide a residue impoverished in said precious metal.
A method for recovering precious metals from particulate refractory mineral sulfides in which at least one precious metal is occluded within the sulfide particulate which impedes the recovery of precious metals therefrom by direct leaching which comprises:
- providing said mineral sulfide in the finely ground state,
- forming a slurry of said sulfide with acid, nutrient nitrogen salts and phosphorus salts to which an acidophilic thermophile has been added,
- the pH of said slurry ranging from about 0.5 to 3, feeding said slurry into a series of biological reactors ranging from a first reactor to an Nth reactor,
- the rate of feed through the reactors being at least sufficient to provide a residence time to effect partial to complete oxidation of the mineral sulfide sufficient to liberate the precious metals therein,
- adding air and carbon dioxide to said reactors during said residence period while allowing for oxidation of said sulfide by said thermophile at a temperature in excess of about 45.degree. C. but not exceeding that temperature above which the thermophile is degraded,
- passing said slurry in the reacted form from said Nth reactor to a solid/liquid separator to provide a residue containing liberated precious metals and a filtered acid leach liquor which is cycled to a series of neutralization tanks,
- neutralizing acid in said residue, subjecting said neutralized residue to cyanidation with a cyanide solution to dissolve selectively precious metals therein that form soluble complexes with said cyanide solution,
- neutralizing said filtered acid leach liquor using limestone whereby CO.sub.2 is formed and recycled to the biological reactors,
- adding make-up acid and nutrients to said acid leach liquor,
- recyling said leach liquor with said nutrients to said biological reactors, and
- recovering said precious metals from said cyanide solution.
Dependencies are inferred from the claim text.