Precious metal recovery using thiocyanate lixiviant

• US 7,559,973 B2
• Filed: 10/05/2007
• Issued: 07/14/2009
• 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): Wyszomierski; George
• Assistant Examiner(s): MCGUTHRY BANKS, TIMA MICHELE
• Application Number:
  US11/868,378
• Publication Number:
  US 20080066578A1
• Time in Patent Office: 648 Days
• Field of Search: 757/44, 423/29
• US Class Current: 75/744
• 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

For removal of precious metal from thiocyanate leach solution, precious metal is transferred from precious metal-thiocyanate complex to precious metal-cyanide complex. Preparation of thiocyanate leach solution includes dissolving cyanide in an aqueous liquid and converting the cyanide to dissolved thiocyanate.

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, wherein the molar ratio of the dissolved ferric iron to the dissolved thiocyanate is determined by dividing molar concentration of the dissolved ferric iron by molar concentration of the dissolved thiocyanate, and wherein 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, to produce a barren effluent of the thiocyanate leach solution comprising 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;

wherein the recovering comprises introducing dissolved cyanide into the thiocyanate leach solution and transferring at least a portion of the precious metal in the thiocyanate leach solution from the precious metal-thiocyanate complex to precious metal-cyanide complex.

2. The method of claim 1, wherein the recovering comprises adding cyanide to the thiocyanate leach solution at a molar ratio of the added cyanide to the dissolved thiocyanate in the thiocyanate leach solution that is no larger than 1:

4.

3. The method of claim 2 wherein the precious metal comprises gold, and the transferring comprises transferring at least 80 percent of the gold dissolved in the thiocyanate solution from gold-thiocyanate complex to gold-cyanide complex.

4. The method of claim 3, wherein the recovering comprises removing at least a portion of the gold-cyanide complex from the thiocyanate leach solution.

5. 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, wherein the molar ratio of the dissolved ferric iron to the dissolved thiocyanate is determined by dividing molar concentration of the dissolved ferric iron by molar concentration of the dissolved thiocyanate, and wherein 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, to produce barren effluent of the thiocyanate leach solution comprising 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;

wherein the conditioning comprises introducing dissolved cyanide into the thiocyanate leach solution and converting at least a portion of the dissolved cyanide to thiocyanate prior to supplying the feed of the thiocyanate leach solution to the thiocyanate leaching.

6. The method of claim 5, wherein the conditioning comprises introducing dissolved cyanide into the thiocyanate leach solution and converting substantially all of the dissolved cyanide to thiocyanate prior to supplying the feed of the thiocyanate leach solution to the thiocyanate leaching.

7. A method for recovering precious metal from mineral material containing the precious metal, the method comprising:

thiocyanate leaching the mineral material with a thiocyanate leach solution to dissolve at least a portion of the precious metal from the mineral material into the leach solution in the form of precious metal-thiocyanate complex;

introducing dissolved cyanide into the thiocyanate leach solution and transferring at least a portion of the precious metal from the precious metal-thiocyanate complex to precious metal-cyanide complex;

removing from the thiocyanate leach solution at least a portion of the precious metal transferred to the precious metal-cyanide complex.

8. The method of claim 7, wherein the thiocyanate leach solution is at an acidic pH during the thiocyanate leaching, the introducing, the transferring and the removing.

9. The method of claim 8, wherein, during the introducing and the transferring, the thiocyanate leach solution comprises a molar ratio of dissolved cyanide to dissolved thiocyanate that does not exceed 1:

4.

10. The method of claim 9, wherein the introducing comprises adding the cyanide to the thiocyanate leach solution at a molar ratio of the cyanide to precious metal in the thiocyanate leach solution that is no larger than 20:

1.

11. The method of claim 10, wherein:

the precious metal in the thiocyanate leach solution comprises gold; and

the introducing comprises adding the cyanide to the thiocyanate leach solution at a molar ratio of the added cyanide to the gold in the thiocyanate leach solution that is no larger than 20;

1.

12. The method of claim 11, wherein the molar ratio of the cyanide to the gold in the thiocyanate leach solution is in a range of from 2:

1 to 20;

1.

13. A method for recovering precious metal from a thiocyanate leach solution in which precious metal is dissolved in the form of precious metal-thiocyanate complex, the method comprising:

introducing cyanide into the thiocyanate leach solution;

transferring at least a portion of the precious metal from the precious metal-thiocyanate complex in the thiocyanate leach solution to precious metal-cyanide complex in the thiocyanate leach solution; and

removing from the thiocyanate leach solution at least a portion of the precious metal transferred to the precious metal-cyanide complex.

14. The method of claim 13, wherein the transferring comprises introducing dissolved cyanide into the thiocyanate leach solution at a molar ratio of the dissolved cyanide to dissolved thiocyanate in the thiocyanate leach solution that does not exceed 1:

4.

15. The method of claim 14, wherein the precious metal comprises gold, and the transferring comprises transferring at least 80 percent of the gold dissolved in the thiocyanate leach solution from the gold-thiocyanate complex to the gold-cyanide complex.

18. The method of claim 13, wherein the removing comprises separating from the thiocyanate leach solution at least a portion of the precious metal in the form of the precious metal-cyanide complex.

19. The method of claim 18, wherein the removing comprises loading at least a portion of the precious metal-cyanide complex onto an adsorbent material.

20. The method of claim 19, wherein the adsorbent material comprises activated carbon.

21. The method of claim 19, wherein the adsorbent material comprises ion exchange resin.

16. The method of claim, wherein the transferring comprises adding the cyanide to the thiocyanate leach solution at a molar ratio of the cyanide to the gold in the thiocyanate leach solution that is no larger than 20:

1.

17. The method of claim 16, wherein during the transferring, the thiocyanate leach solution has a pH in a range from pH 1 to pH 3.