Process for the recovery of gold from carbonaceous ores
AssigneeFreeport Minerals Corporation
InventorsRaphael F. Matson, Bernard M. Fisher
Life of this patent
Estimating the term…
Abstract
The recovery of gold from refractory carbonaceous gold-containing ores by cyanidation techniques is improved by subjecting an oxidized slurry of this type of ores to simultaneous cyanidation and countercurrent granular activated carbon adsorption in two or more stages. The gold transfers to the carbon and may be separated from it by conventional methods.
Claims6
In a process for the recovery of gold values from carbonaceous gold-containing ores by contacting an aqueous slurry of said ores with a cyanide complexing agent for the gold values, the improvement which comprises:
- (a) forming said aqueous slurry of said ores in the presence of a soluble alkaline material;
- (b) subjecting said aqueous slurry to oxidation comprising an oxygenation step, wherein said formed aqueous slurry is intimately contacted with an oxygen-containing gas for at least one hour, and a chlorination step, wherein the oxygenated slurry is intimately contacted with a source of hypochlorite ions for at least one hour;
- (c) simultaneously contacting the oxidized aqueous slurry, in a plurality of stages, with said cyanide complexing agent and granular activated carbon, the carbon flowing in countercurrent fashion with said slurry, wherein the temperatures of the slurry is maintained between about 40.degree. and 100.degree. F., whereby said gold values are transferred to said granular activated carbon;
- and
- (d) separating said granular activated carbon from said aqueous slurry.
A process for recovering gold values from carbonaceous gold-containing ores which comprises:
- (a) forming an aqueous slurry of said ores having a solids content between about 30 and 60% by weight;
- (b) adding a soluble alkaline material to raise the pH of said aqueous slurry to between about 8 and 13;
- (c) contacting said aqueous slurry with an oxygen-containing gas at a temperature between about 120.degree. and 210.degree. F.;
- (d) thereafter adjusting the temperature of said aqueous slurry to between about 70.degree. and 140.degree. F.;
- (e) thereafter subjecting the slurry to a chlorination step, wherein the slurry is contacted with a material capable of providing hypochlorite ions in solution;
- (f) allowing any excess hypochlorite ions to be consumed;
- (g) further adjusting the temperature of said slurry to between about 40.degree. and 100.degree. F.;
- (h) thereafter feeding the slurry to a plurality of solid-liquid extraction stages wherein it contacts a cyanide complexing agent for the gold values and granular activated carbon flowing countercurrent with said flow of said slurry, whereby said gold values are transferred to said granular activated carbon;
- and
- (i) separating said granular activated carbon and transferred gold values contained in said granular activated carbon from said slurry by means of interstage screening.
Dependencies are inferred from the claim text.