Process for the recovery of gold from carbonaceous ores

Claim 2

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° and 100° F., whereby said gold values are transferred to said granular activated carbon; and (d) separating said granular activated carbon from said aqueous slurry.

Claim 3

The process of claim 1, wherein said oxygenation step is carried out at a temperature between about 120° and 210° F. and said chlorination step is carried out at a temperature between about 70° and 140° F.

Claim 4

The process of claim 2, wherein said oxygenation step is carried out at a pH between about 8 and 13 for 4-8 hours, the temperature of the slurry is thereafter adjusted to between about 70° and 140° F., and the chlorination step carried out at a pH between about 5 and 11 for 1-6 hours, at about 70°-140° F.

Claim 5

The process of claim 3, further comprising holding the chlorinated slurry at 70°-140° F. in a vessel separate from that in which said chlorination step takes place for a period of time sufficient to allow excess hypochlorite ions to be consumed.

Claim 6

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° and 210° F.; (d) thereafter adjusting the temperature of said aqueous slurry to between about 70° and 140° 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° and 100° 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.

Claim 7

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° and 210° F.; (d) thereafter adjusting the temperature of said aqueous slurry to between about 70° and 140° 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° and 100° 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.

Claim 8

The process of claim 5 further comprising separating said transferred gold values in step (i) from said granular activated carbon and recycling said granular activated carbon to said plurality of solid-liquid extraction stages.