Method for recovering cyanide from a barren solution

Patent metadata

Field	Value
Publication number	US-2017081202-A1
Application number	US-201615268731-A
Country	US
Kind code	A1
Filing date	Sep 19, 2016
Priority date	Sep 21, 2015
Publication date	Mar 23, 2017
Grant date	—

Abstract

A process is disclosed for recovering cyanide used to leach gold or silver from ore. In the course of leaching gold or silver from ore, a barren solution is generated. A portion of the barren solution containing sodium cyanide is recycled to the cyanidation process while blowdown from the barren solution is subjected to pre-treatment, UV photodissociation and pH adjustment. Ultimately, a volatile hydrocyanic acid is formed and is absorbed into a sodium hydroxide solution through the employment of a gas-filled membrane. This forms sodium cyanide that can be recycled and used in the cyanidation process to leach gold or silver from ore.

First claim

What is claimed is:

1 . A method of recovering cyanide from a barren solution containing sodium cyanide, metals and metal-cyanide complexes, comprising:
pre-treating the barren solution and removing metals therefrom by precipitation and or co-precipitation and adsorption; after pre-treatment, directing the barren solution to a ultraviolet irradiation unit; irradiating the barren solution with ultraviolet light at a pH greater than 8 . 0 and, through photodissociation, causing the metal-cyanide complexes to form free cyanide; after irradiating the barren solution, adding an acid to the barren solution and adjusting the pH of the barren solution downwardly to approximately 6.0-6.5 to form hydrocyanic acid gas in the barren solution; after forming the hydrocyanic acid gas in the barren solution, directing the barren solution to a gas-filled membrane; and directing a sodium hydroxide solution through a stripping side of the gas-filled membrane and diffusing the hydrocyanic acid gas through pores in the gas-filled membrane where the hydrocyanic acid gas is absorbed by the sodium hydroxide on the stripping side of the gas-filled membrane to form a sodium cyanide solution.

2 . The method of claim 1 wherein pre-treating the barren solution includes mixing sodium hydroxide, hydrated lime, quick lime, or magnesium hydroxide with the barren solution.

3 . The method of claim 2 wherein pre-treating the barren solution further includes mixing a coagulant with the barren solution.

4 . The method of claim 1 wherein removing metals from the barren solution includes clarifying the barren solution prior to directing the barren solution to the ultraviolet irradiation unit.

5 . The method of claim 4 wherein prior to directing the barren solution to the irradiation unit but after the barren solution has been clarified, the method includes filtering the barren solution.

6 . The method of claim 1 including mixing an anti-scalant with the barren solution in the irradiation unit or at a point upstream of the irradiation unit.

7 . The method of claim 1 including irradiating the barren solution with ultraviolet light having a wave length in the region from 200 to 300 nm which causes the metal-cyanide complexes in the barren solution to undergo photo disassociation.

8 . The method of claim 1 including irradiating the barren solution with ultraviolet light at a pH of 10.0 to 10.5.

9 . The method of claim 1 wherein after irradiating the barren solution with ultraviolet light, filtering the barren solution and removing fine particles of metal hydroxide.

10 . The method of claim 1 including mixing the sodium cyanide solution with ore containing gold or silver and leaching the gold or silver from the ore into the sodium cyanide solution.

11 . The method of claim 10 including precipitating gold or silver from the sodium cyanide solution and filtering the gold or silver from the sodium cyanide solution.

12 . A method of recovering gold or silver from ore contained in an ore slurry and recovering sodium cyanide used to leach gold or silver from the ore, the method comprising:
directing the ore slurry containing gold or silver to a leaching tank; mixing sodium cyanide with the ore to form a sodium cyanide solution; leaching gold or silver from the ore into the sodium cyanide solution; adding a reagent to the sodium cyanide solution and precipitating gold or silver from the sodium cyanide solution; filtering the gold or silver from the sodium cyanide solution which yields a barren solution containing sodium cyanide; pre-treating the barren solution and removing metals therefrom by precipitation, and or co-precipitation and adsorption; after pre-treatment, directing the barren solution to a ultraviolet irradiation unit; irradiating the barren solution with ultraviolet light at a pH greater than 8 . 0 and, through photodissociation, causing the metal-cyanide complexes to form free cyanide; after irradiating the barren solution, adding an acid to the barren solution and adjusting the pH of the barren solution downwardly to approximately 6.0-6.5 to form hydrocyanic acid gas in the barren solution; after forming the hydrocyanic acid gas in the barren solution, directing the barren solution to a gas-filled membrane; directing a sodium hydroxide solution through a stripping side of the gas-filled membrane and diffusing the hydrocyanic acid gas through pores in the gas-filled membrane where the hydrocyanic acid gas is absorbed by the sodium hydroxide on the stripping side of the gas-filled membrane to yield sodium cyanide; and recycling at least a portion of the sodium cyanide produced by the gas-filled membrane to the leaching tank such that the sodium cyanide can be reused to leach gold or silver from the ore.

13 . The method of claim 12 wherein pre-treating the barren solution includes mixing sodium hydroxide, hydrated lime, quick lime, or magnesium hydroxide with the barren solution.

14 . The method of claim 13 wherein pre-treating the barren solution further includes mixing a coagulant with the barren solution.

15 . The method of claim 12 wherein removing metals from the barren solution includes clarifying the barren solution prior to directing the barren solution to the ultraviolet irradiation unit.

16 . The method of claim 15 wherein prior to directing the barren solution to the irradiation unit but after the barren solution has been clarified, the method includes filtering the barren solution.

17 . The method of claim 12 including mixing an anti-scalant with the barren solution in the irradiation unit or at a point upstream of the irradiation unit.

18 . The method of claim 12 including irradiating the barren solution with ultraviolet light having a wave length in the region from 200 to 300 nm which causes the metal-cyanide complexes in the barren solution to undergo photo disassociation.

19 . The method of claim 12 including irradiating the barren solution with ultraviolet light at a pH of 10.0 to 10.5.

20 . The method of claim 12 wherein after irradiating the barren solution with ultraviolet light, filtering the barren solution and removing fine particles of metal hydroxide.

Assignees

• Veolia Water Solutions & Tech

Inventors

• Banerjee Kashi
• Buisson Herve

Classifications

• C22B11/08

  by cyaniding · CPC title

• C01C3/10 Primary

  Simple alkali metal cyanides · CPC title

• C22B3/22

  by physical processes, e.g. by filtration, by magnetic means {, or by thermal decomposition} (treatment or purification of solutions by liquid-liquid extraction C22B3/26) · CPC title

• C22B3/44

  by chemical processes (treatment or purification of solutions by liquid-liquid extraction C22B3/26, by ion-exchange extraction C22B3/42) · CPC title

• C22B3/04

  by leaching (C22B3/18 takes precedence) · CPC title