Precious metal recovery using thiocyanate lixiviant

• US 7,285,256 B2
• Filed: 08/28/2003
• Issued: 10/23/2007
• Est. Priority Date: 04/04/2003
• Status: Active Grant

• Current Assignee: Newmont USA Limited (Newmont Corp.)
• Original Assignee: Newmont USA Limited (Newmont Corp.)
• Inventors: Wan, Rong Yu, LeVier, K. Marc
• Primary Examiner(s): Langel; Wayne A.
• Assistant Examiner(s): Fiorito; James
• Application Number:
  US10/651,184
• Publication Number:
  US 20040197249A1
• Time in Patent Office: 1,517 Days
• Field of Search: 423/27, 423/29, 423/22
• US Class Current: 423/22
• CPC Class Codes: C22B 11/08 by cyaniding
• CPC Class Codes: C22B 15/0076 Cyanide groups
• CPC Class Codes: C22B 3/24 by adsorption on solid substances, e.g. by extraction with solid resins
• CPC Class Codes: C22B 3/42 by ion-exchange extraction
• CPC Class Codes: Y02P 10/20 Recycling

Abstract

Precious metal-containing mineral material is subjected to an acidic thiocyanate leach to dissolve the precious metal as a precious metal-thiocyanate complex. A feed of the thiocyanate leach solution may include a large molar ratio of ferric iron to thiocyanate. Precious metal may be removed from pregnant thiocyanate leach solution, such as by transferring precious metal from precious metal-thiocyanate complex to precious metal-cyanide complex and then loading the precious metal-cyanide complex onto an adsorbent material. Remaining cyanide in the thiocyanate leach solution may be converted to thiocyanate for additional leaching of precious metal.

Claims

1. A method for processing precious metal-containing mineral material to recover precious metal from the mineral material using a circulating thiocyanate leach solution, the method comprising:

thiocyanate leaching the mineral material with the thiocyanate leach solution, the thiocyanate leach solution comprising dissolved thiocyanate and dissolved ferric iron and during the thiocyanate leaching at least a portion of the precious metal from the mineral material is dissolved into the thiocyanate leach solution in the form of precious metal-thiocyanate complex;

supplying feed of the thiocyanate leach solution to the thiocyanate leaching, the feed of the thiocyanate leach solution comprising a pH in a range of from pH 1 to pH 3 and comprising a molar ratio of the dissolved ferric iron to the dissolved thiocyanate of at least 2, and during the thiocyanate leaching at least a portion of the dissolved ferric iron in the feed of the thiocyanate leach solution is reduced to dissolved ferrous iron;

recovering at least a portion of the precious metal from the thiocyanate leach solution, after the recovering barren effluent of the thiocyanate leach solution comprises a concentration of the dissolved ferric iron that is smaller than a concentration of the dissolved ferric iron in the feed of the thiocyanate leach solution;

conditioning the thiocyanate leach solution to prepare the feed of the thiocyanate leach solution, at least a portion of the barren effluent of the thiocyanate leach solution being supplied to the conditioning for use to prepare the feed of the thiocyanate leach solution, and the conditioning comprising increasing a concentration of the dissolved ferric iron in the thiocyanate leach solution relative to the concentration of the dissolved ferric iron in the barren effluent of the thiocyanate leach solution supplied to the conditioning.

2. The method of claim 1, wherein a concentration of the dissolved thiocyanate in the feed of the thiocyanate leach solution is no larger than 0.03 mole per liter.

3. The method of claim 2, wherein the concentration of the dissolved thiocyanate in the feed of the thiocyanate leach solution is in a range of from 0.0001 mole per liter to 0.03 mole per liter.

4. The method of claim 2, wherein the concentration of the dissolved thiocyanate in the feed of the thiocyanate leach solution is in a range of from 0.001 mole per liter to 0.02 mole per liter.

5. The method of claim 1, wherein the concentration of the dissolved ferric iron in the feed of the thiocyanate leach solution is at least 0.05 mole per liter.

6. The method of claim 1, wherein the concentration of the dissolved ferric iron in the feed of the thiocyanate leach solution is at least 0.1 mole per liter.

7. The method of claim 1, wherein the molar ratio of the dissolved ferric iron to the dissolved thiocyanate in the feed of the thiocyanate leach solution is at least 4.

8. The method of claim 1, wherein a concentration of the dissolved thiocyanate in the feed of the thiocyanate leach solution is in a range of from 0.0001 mole per liter to 0.03 mole per liter, the concentration of the dissolved ferric iron in the feed of the thiocyanate leach solution is at least 0.05 mole per liter, and the molar ratio of the dissolved ferric iron to the dissolved thiocyanate in the feed of the thiocyanate leach solution is at least 7.

9. The method of claim 1, wherein the precious metal comprises gold and at least a majority of the gold in the mineral material is leached into the thiocyanate leach solution during the thiocyanate leaching.

10. The method of claim 1, wherein the recovering comprises solvent extraction of the precious metal from the thiocyanate leach solution after the thiocyanate leaching, the solvent extraction comprising contacting the thiocyanate leach solution with an organic extractant phase and transferring at least a portion of the dissolved precious metal from the thiocyanate leach solution into the organic extractant phase.

11. The method of claim 10, wherein the organic extractant phase comprises a phosphorous-containing extractant.

12. The method of claim 10, wherein the organic extractant phase comprises an amine extractant.

13. The method of claim 1, wherein:

the recovering comprises contacting the thiocyanate leach solution with ion exchange resin after the thiocyanate leaching; and

during the contacting at least a portion of the precious metal is removed from the thiocyanate leach solution and loaded onto the ion exchange resin.

14. The method of claim 1, wherein the thiocyanate leach solution is maintained at an acidic pH during the thiocyanate leaching, the recovering and the conditioning.

15. The method of claim 1, wherein the thiocyanate leach solution is maintained at a pH in a range of from pH 1 to pH 3 during the thiocyanate leaching, the recovering and the conditioning.

16. The method of claim 1, wherein the thiocyanate leaching comprises:

applying the feed of the thiocyanate leach solution to a heap comprising the mineral material; and

percolating the thiocyanate leach solution through the heap.

17. The method of claim 16, comprising, prior to the thiocyanate leaching, preparing the mineral material, the preparing comprising:

forming the heap initially comprising particulate feed material, the particulate feed material comprising sulfide minerals; and

bio-oxidizing the feed material in the heap to decompose at least a portion of the sulfide minerals.

18. The method of claim 1, wherein the conditioning comprises adding acidic bio-oxidation effluent liquid to the thiocyanate leach solution, the acidic bio-oxidation effluent liquid comprising a concentration of ferric iron that is larger than the concentration of the dissolved ferric iron in the feed of the thiocyanate leach solution.

19. The method of claim 1, comprising, prior to the thiocyanate leaching, preparing the mineral material, the preparing comprising pressure oxidizing under acidic conditions feed material, the feed material comprising sulfide minerals that are decomposed during the pressure oxidizing.

20. The method of claim 19, wherein the feed material comprises at least 2 weight percent sulfide sulfur.

21. The method of claim 20, wherein the feed material comprises at least one of (i) an ore comprising at least 2 weight percent sulfide sulfur and (ii) a sulfide concentrate made from the ore.

22. The method of claim 1, comprising, prior to the thiocyanate leaching, preparing the mineral material, the preparing comprising acid leaching feed material with an acidic leach solution, the feed material comprising copper and during the acid leaching at least a portion of the copper is dissolved into the acidic leach solution, thereby removing soluble copper from the feed material prior to the thiocyanate leaching.

23. The method of claim 22, wherein the copper-containing feed material comprises at least 200 parts per million by weight of the copper that is dissolved into the acidic leach solution during the acid leaching.

24. The method of claim 1, wherein the mineral material comprises at least one of(i) an ore comprising at least 0.5 weight percent sulfide sulfur and less than 2 weight percent sulfide sulfur and (ii) a concentrate prepared from the ore.

25. The method of claim 24, wherein the ore comprises no more than 1.5 weight percent sulfide sulfur.

26. The method of claim 1, wherein the increasing a concentration of the dissolved ferric iron in the thiocyanate leach solution comprises adding dissolved ferric iron to the thiocyanate leach solution.

27. The method of claim 26, wherein the adding dissolved ferric iron comprises adding acidic bio-oxidation effluent liquid to the thiocyanate leach solution.

28. The method of claim 1, wherein the increasing a concentration of the dissolved ferric iron in the thiocyanate leach solution comprises oxidizing to ferric form at least a portion of the dissolved ferrous iron in the thiocyanate leach solution.

29. The method of claim 28, wherein the oxidizing comprises introducing an oxidant into the thiocyanate leach solution.

30. The method of claim 29, wherein the oxidant comprises a persulphate.

31. The method of claim 29, wherein the oxidant comprises a component selected from the group consisting of persulfuric acid, peroxide, manganese dioxide, ozone, a halogen and a hypochiorite.

32. The method of claim 28, wherein the oxidizing comprises contacting the thiocyanate leach solution with oxidizing gas.

33. The method of claim 32, wherein the oxidizing comprises contacting the thiocyanate leach solution with oxygen gas and a component selected from the group consisting of sulfur dioxide gas, a bisulfite and a metabisulfite.

34. The method of claim 1, wherein the mineral material comprises sulfide sulfur;

and

during the thiocyanate leaching at least a portion of the sulfide sulfur in the mineral material is oxidized.

35. The method of claim 34, wherein:

the mineral material comprises residue remaining following acidic oxidative pretreatment of a particulate feed material comprising sulfide sulfur, during the oxidative pretreatment a portion of the sulfide sulfur of the particulate feed material having been oxidized; and

the at least a portion of the sulfide sulfur of the mineral material oxidized during the thiocyanate leaching comprises sulfide sulfur of the particulate feed material remaining unoxidized upon completion of the oxidative pretreatment.

36. The method of claim 35, wherein during the thiocyanate leaching, the mineral material is in a heap that has been substantially structurally undisturbed between completion of the oxidative treatment and commencement of the thiocyanate leaching.

37. The method of claim 34, wherein:

at commencement of the thiocyanate leaching, the mineral material comprises a sulfide sulfur content of at least 0.5 weight percent sulfide sulfur; and

solid residue of the mineral material remaining at the completion of the thiocyanate leaching comprises a sulfide sulfur content that is smaller than the sulfide sulfur content of the mineral material at the commencement of the thiocyanate leaching.

38. The method of claim 5, wherein a concentration of the dissolved thiocyanate in the feed of the thiocyanate leach solution is no larger than 0.05 mole per liter.

39. The method of claim 38, wherein the molar ratio of the dissolved ferric iron to the dissolved thiocyanate is no larger than 20.

40. The method of claim 24, comprising during the thiocyanate leaching, oxidizing at least a portion of the sulfide sulfur and decomposing at least a portion of sulfide minerals contained in the feed of the mineral material.