Gold recovery from refractory carbonaceous ores by pressure oxidation, thiosulfate leaching and resin-in-pulp adsorption

• US 5,785,736 A
• Filed: 07/16/1996
• Issued: 07/28/1998
• Est. Priority Date: 02/10/1995
• Status: Expired due to Term

• Current Assignee: Barrick Gold Corporation
• Original Assignee: Barrick Gold Corporation
• Inventors: Fleming, Christopher, Marchbank, Andrew R., Dreisinger, David, Thomas, Kenneth G.
• Primary Examiner(s): ANDREWS, MELVYN J
• Application Number:
  US08/680,906
• Time in Patent Office: 742 Days
• Field of Search: 75/736, 75/744, 204/109
• US Class Current: 75/736
• CPC Class Codes: C22B 11/04 by wet processes extraction of metal compounds by leaching in organic solutions C22B3/16; treatment or purification of solutions by liquid-liquid extraction C22B3/26
• CPC Class Codes: C22B 3/08 Sulfuric acid , other sulfurated acids or salts thereof
• CPC Class Codes: C22B 3/42 by ion-exchange extraction
• CPC Class Codes: Y02P 10/20 Recycling

Abstract

A process for treatment of precious metal ores in which gold is leached from an oxidized ore slurry using a thiosulfate salt lixiviant and copper catalyst. Gold and copper are subsequently loaded onto an ion exchange resin. Copper is recovered from the resin by elution with a thiosulfate solution; gold is recovered from the resin by elution with a thiocyanate colution. Gold is recovered from the eluate by precipitation, electrowinning, or cementation.

Claims

1. A process for recovering gold from a slurry comprising a solid ore residue and a gold-bearing thiosulfate lixiviant comprising:

contacting the slurry with an ion exchange resin having affinity for gold to adsorb gold from the gold-bearing thiosulfate lixiviant onto said resin;

eluting gold from said resin to produce a gold-bearing eluate; and

recovering gold from the gold-bearing eluate.

2. The process of claim 1 wherein gold is recovered from the gold-bearing eluate by electrowinning.

3. The process of claim 1 wherein said ion exchange resin is a strong-base resin.

4. The process of claim 1 wherein said ion exchange resin is a weak-base resin.

5. The process of claim 1 comprising eluting the gold from said resin with a thiocyanate solution eluant.

6. The process of claim 1 wherein gold is recovered from the gold-bearing eluate by raising the pH of the eluate to between about 9.5 and about 11.5 to cause gold to precipitate.

11. The process of claim 1 wherein the slurry comprises a solid ore residue and a gold-bearing and copper-bearing thiosulfate lixiviant and the ion exchange resin has an affinity for gold and copper, the process comprising contacting the slurry with the ion exchange resin to adsorb gold and copper from the lixiviant onto said resin;

eluting copper from said resin to produce a copper-bearing eluate; and

eluting gold from said resin to produce a gold-bearing eluate.

12. The process of claim 11 wherein said copper is eluted from the resin with an eluant containing between about 100 g/L and 200 g/L ammonium thiosulfate.

13. The process of claim 11 wherein said copper-bearing eluate is recycled for use as a catalyst in leaching gold with thiosulfate lixiviant.

7. A process for recovering gold from a gold-bearing thiosulfate lixiviant comprising:

contacting the gold-bearing thiosulfate lixiviant with an ion exchange resin having affinity for gold to adsorb gold from the gold-bearing thiosulfate lixiviant onto said resin;

eluting gold from said resin to produce a gold-bearing eluate; and

recovering gold from the gold-bearing eluate.

8. The process of claim 7 wherein said ion exchange resin is a strong-base resin.

9. The process of claim 7 comprising eluting the gold from said resin with a thiocyanate solution eluant.

10. The process of claim 7 wherein gold is recovered from the gold-bearing eluate by raising the pH of the eluate to between about 9.5 to about 11.5 to cause gold to precipitate.

14. The process of claim 7 wherein the lixiviant is a gold-bearing and copper-bearing thiosulfate lixiviant and the ion exchange resin has an affinity for gold and copper, the process comprising contacting the lixiviant with the ion exchange resin to adsorb gold and copper from the lixiviant onto said resin;

eluting copper from said resin to produce a copper-bearing eluate; and

eluting gold from said resin to produce a gold-bearing eluate.

15. The process of claim 14 wherein said copper is eluted from the resin with an eluant containing between about 100 g/L and 200 g/L ammonium thiosulfate.

16. The process of claim 14 wherein said copper-bearing eluate is recycled for use as a catalyst in leaching gold with thiosulfate lixiviant.

26. The process of claim 7 wherein the gold-bearing thiosulfate lixiviant is prepared by:

forming an aqueous ore slurry comprising an auriferous ore;

subjecting the ore slurry to pressure oxidation in an autoclave to produce an oxidized ore slurry;

leaching gold from the oxidized slurry by mixing the oxidized ore slurry with a lixiviant comprising a thiosulfate salt to produce a leached slurry comprising a solid residue and a gold-bearing thiosulfate lixiviant.

17. A process for recovering gold from a gold-bearing oxidized ore slurry comprising:

contacting the oxidized ore slurry with a thiosulfate lixiviant in the presence of an ion exchange resin having affinity for gold to leach gold from the ore and adsorb gold onto said resin;

eluting gold from said resin to produce a gold-bearing eluate; and

recovering gold from the gold-bearing eluate.

18. The process of claim 17 wherein a system pH in the range of between 7 and 8.7 is maintained during said contacting of the oxidized slurry with lixiviant.

27. The process of claim 17 wherein the gold-bearing oxidized ore slurry is prepared by:

forming an aqueous ore slurry comprising an auriferous ore; and

subjecting the ore slurry to pressure oxidation in an autoclave to produce a gold-bearing oxidized ore slurry.

19. A process for recovering gold from an auriferous ore comprising the steps of:

forming an aqueous ore slurry comprising an auriferous ore;

subjecting the ore slurry to pressure oxidation in an autoclave under neutral or alkaline conditions to produce an oxidized ore slurry;

leaching gold from the oxidized slurry by mixing the oxidized ore slurry with a lixiviant comprising a thiosulfate salt to produce a leached slurry comprising a solid residue and a gold-bearing leachate;

contacting the leached slurry with an ion exchange resin having affinity for gold to adsorb gold from the gold-bearing thiosulfate leachate onto said resin;

eluting gold from said resin to produce a gold-bearing eluate; and

recovering gold from the gold-bearing eluate.

20. A process for recovering gold from an auriferous ore comprising the steps of:

forming an aqueous ore slurry comprising an auriferous ore;

subjecting the ore slurry to pressure oxidation in an autoclave to produce an oxidized ore slurry;

mixing the oxidized ore slurry with a lixiviant comprising a thiosulfate salt to form a mixture of oxidized ore slurry and lixiviant;

leaching gold from the oxidized slurry by maintaining the mixture at a pH between 7 and 8.7 while agitating the mixture to produce a leached slurry comprising a solid residue and a gold-bearing leachate; and

recovering gold from the gold-bearing leachate by contacting the leachate with an ion exchange resin having affinity for gold to adsorb gold onto said resin.

21. The process of claim 20 comprising contacting the leachate with said resin in the presence of said solid residue.

22. A process for recovering gold from a refractory sulfidic and refractory carbonaceous auriferous ore having preg-robbing characteristics due to the presence of organic carbon comprising the steps of:

forming an aqueous ore slurry comprising a refractory sulfidic and refractory carbonaceous ore having preg-robbing characteristics due to the presence of organic carbon;

subjecting the ore slurry to pressure oxidation in an autoclave under neutral or alkaline conditions to produce an oxidized ore slurry having a pH in the range of between about 6 and 8;

mixing the oxidized ore slurry with a lixiviant comprising a thiosulfate salt;

leaching gold from the oxidized slurry by maintaining the mixture at a pH between 7 and 8.7 to produce a leached slurry comprising a solid residue and a gold-bearing leachate; and

recovering gold from the gold-bearing leachate by contacting the leached slurry with an ion exchange resin having affinity for gold to adsorb gold from the gold-bearing thiosulfate lixiviant onto said resin;

eluting gold from said resin to produce a gold-bearing eluate; and

recovering gold from the gold-bearing eluate.

23. A process for recovering gold from a gold-bearing eluate resulting from the elution of gold-thiosulfate complex from an ion exchange resin with a thiocyanate solution, the eluate containing thiosulfate ions and thiocyanate ions, the process comprising adding a basic compound to the eluate to increase the pH of the eluate to between about 9.5 to about 11.5 to cause gold to precipitate.

24. The process of claim 23 wherein said basic compound is selected from the group consisting of lime and caustic soda.

25. The process of claim 23 further comprising adding a reductant to the eluate to increase gold precipitation.

28. A process for recovering gold from an auriferous ore slurry comprising:

contacting the auriferous ore slurry with a thiosulfate lixiviant in the presence of an ion exchange resin having affinity for gold to leach gold from the ore and adsorb gold onto said resin;

eluting gold from said resin to produce a gold-bearing eluate; and

recovering gold from the gold-bearing eluate.

29. The process of claim 28 wherein a system pH in the range of between 7 and 8.7 is maintained during said contacting of the slurry with lixiviant.

30. A process for recovering gold from an auriferous ore comprising the steps of:

contacting the ore with a lixiviant comprising a thiosulfate salt solution at a pH of between 7 and 8.7 to produce a leached slurry comprising a solid residue and a gold-bearing leachate; and

recovering gold from the gold-bearing leachate by contacting the leached slurry with an ion exchange resin having affinity for gold to adsorb gold from the gold-bearing thiosulfate lixiviant onto said resin;

eluting gold from said resin to produce a gold-bearing eluate; and

recovering gold from the gold-bearing eluate.

31. A process for recovering gold from an auriferous ore comprising the steps of:

forming an aqueous ore slurry comprising an auriferous ore;

mixing the ore slurry with a lixiviant comprising a quantity of thiosulfate salt in a stirred tank reactor system comprising several agitated leach tanks by progressively transferring the ore slurry from the first of said leach tanks to the last of said leach tanks while introducing a portion of said thiosulfate salt separately into a plurality of said agitated leach tanks to produce a leached slurry comprising a solid residue and a gold-bearing leachate; and

recovering gold from the gold-bearing leachate by contacting the leached slurry with an ion exchange resin having affinity for gold to adsorb gold from the gold-bearing thiosulfate lixiviant onto said resin;

eluting gold from said resin to produce a gold-bearing eluate; and

recovering gold from the gold-bearing eluate.

32. A process for recovering gold from a refractory sulfidic and refractory carbonaceous auriferous ore having preg-robbing characteristics due to the presence of organic carbon comprising the steps of:

forming an aqueous ore slurry comprising a refractory sulfidic and refractory carbonaceous ore having preg-robbing characteristics due to the presence of organic carbon;

subjecting the ore slurry to pressure oxidation in an autoclave to produce an oxidized ore slurry;

mixing the oxidized ore slurry with a lixiviant comprising a thiosulfate salt;

leaching gold from the oxidized slurry by maintaining the mixture at a pH between 7 and 8.7 to produce a leached slurry comprising a solid residue and a gold-bearing leachate; and

recovering gold from the gold-bearing leachate by contacting the leached slurry with an ion exchange resin having affinity for gold to adsorb gold from the gold-bearing thiosulfate lixiviant onto said resin;

eluting gold from said resin to produce a gold-bearing eluate; and

recovering gold from the gold-bearing eluate.