Non-polluting process for recovery of precious metal values from ores including those containing carbonate materials

Claim 2

A cyclical hydrometallurgical process for production of a precious metal from a precious metal-containing solid material which consists essentially of: (A) contacting the precious metal-containing material with an effective volume of a caustic leaching solution whose leachants consist essentially of an effective concentration of a hypochlorite salt and an effective concentration of a chloride salt ion for a sufficient time to solubilize the precious metal; (B) depositing the precious metal by displacement of the precious metal with a more electropositive metal to produce a stripped solution; (C) adding sufficient hypochlorite to the stripped solution to maintain an effective concentration of hypochlorite salt therein; and (D) recycling the stripped caustic solution to contact additional precious metal-containing material.

Claim 3

The hydrometallurgical process of claim 1 wherein the metal-containing solid material is passed through a plurality of such metal solubilization contacting steps (A).

Claim 4

The hydrometallurgical process of claim 1 for solubilization of silver, gold or a mixture thereof from solid material containing the same, wherein the contacting of the solid material is performed with an effective volume of a caustic aqueous solution consisting essentially of water; an effective concentration of sodium hypochlorite, potassium hypochlorite, lithium hypochlorite, magnesium hypochlorite, calcium hypochlorite or a mixture thereof; and an effective concentration of sodium chloride, potassium chloride, lithium chloride, magnesium chloride, calcium chloride or a mixture thereof.

Claim 5

The process of claim 3 wherein the aqueous solution contains sodium hypochlorite and sodium chloride.

Claim 6

A hydrometallurgical process for production of metallic silver from a silver-containing material which consists essentially of: (A) contacting the silver-containing material with a volume of a caustic leaching solution whose leachants consist essentially of an effective concentration of a hypochlorite salt and an effective concentration of a chloride salt in a volume of water sufficient to produce a final solution concentration of 5 to 20 parts per million of solubilized silver contained therein; (B) agitating the silver-containing material with the caustic solution for a period of time sufficient to allow substantially complete solubilization of the silver; (C) separating a solubilized silver-containing solution from a residual material resulting from step (B); (D) contacting the solubilized silver-containing solution with iron, zinc or a mixture thereof, in a sufficient quantity to cause deposition of the solubilized silver leaving a stripped solution; (E) separating the stripped solution from the deposited silver; (F) passing a portion of the stripped solution to an electrolysis cell to regenerate the hypochlorite ion concentration in the caustic solution; (G) recycling the remainder of the caustic stripped solution to again contact silver-containing material; and (H) passing the regenerated portion of the stripped caustic solution to contact additional silver-containing material.

Claim 7

A hydrometallurgical process for production of metallic silver from a silver-containing material which consists essentially of: (A) contacting the silver-containing material with a volume of a caustic leaching solution whose leachants consist essentially of an effective concentration of a hypochlorite salt and an effective concentration of a chloride salt in a volume of water sufficient to produce a final solution concentration of 5 to 20 parts per million of solubilized silver contained therein; (B) agitating the silver-containing material with the caustic solution for a period of time sufficient to allow substantially complete solubilization of the silver; (C) separating a solubilized silver-containing solution from a residual material resulting from step (B); (D) contacting the solubilized silver-containing solution with iron, zinc or a mixture thereof, in a sufficient quantity to cause deposition of the solubilized silver leaving a stripped solution; (E) separating the stripped solution from the deposited silver; (F) passing a portion of the stripped solution to an electrolysis cell to regenerate the hypochlorite ion concentration in the caustic solution; (G) recycling the remainder of the caustic stripped solution to again contact silver-containing material; and (H) passing the regenerated portion of the stripped caustic solution to contact additional silver-containing material.

Claim 8

The process of claim 5 wherein the residual material from step (C) is again contacted with a caustic solution whose leachants consist essentially of an effective concentration of a hypochlorite salt and an effective concentration of a chloride salt in a volume of water sufficient to effect additional recovery of silver contained therein.

Claim 9

The process of claim 5 or 6 wherein additional chloride salt is added to the portion of the stripped caustic solution passed to the electrolysis cell in step (F) whereby the electrolysis is rendered more efficient.

Claim 10

The process of claim 1, 2, 3, 4, 5 or 6 wherein the hypochlorite salt concentration is in the range of 0.25 to 2.00 percent by weight.

Claim 11

The process of claim 1, 2, 3, 4, 5 or 6 wherein the chloride salt concentration is in the range of about 5 to 20%.

Claim 12

The process of claim 1, 2, 3, 4, 5 or 6 wherein the hypochlorite salt concentration is in the range of 0.40 to 1.6 percent by weight and the chloride salt concentration is in the range of 10 to 15 percent by weight.

Claim 13

The process of claim 1, 2, 3, 4, 5 or 6 wherein the pH of the caustic leaching solution during the leaching step is 8-13.

Claim 14

The process of claim 7 wherein the pH of the caustic leaching solution during the leaching step is 8-13.

Claim 15

The process of claim 8 wherein the pH of the caustic leaching solution during the leaching step is 8-13.

Claim 16

The process of claim 9 wherein the pH of the caustic leaching solution during the leaching step is 8-13.

Claim 17

The process of claim 10 wherein the pH of the caustic leaching solution during the leaching step is 8-13.