Gold recovery from refractory carbonaceous ores by pressure oxidation and thiosulfate leaching

• US 5,536,297 A
• Filed: 02/10/1995
• Issued: 07/16/1996
• Est. Priority Date: 02/10/1995
• Status: Expired due to Term

• Current Assignee: Barrick Gold Corporation
• Original Assignee: Barrick Gold Corporation
• Inventors: Fleming, Christopher, Dreisinger, David, Thomas, Kenneth G., Marchbank, Andrew R.
• Primary Examiner(s): ANDREWS, MELVYN J
• Application Number:
  US08/389,016
• Time in Patent Office: 522 Days
• Field of Search: 75/736, 75/744
• 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 3/24 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

A process for recovering gold in which an ore slurry of refractory sulfidic and refractory carbonaceous ore having preg-robbing characteristics due to the presence of organic carbon is subjected to pressure oxidation in an autoclave. The oxidized ore slurry is mixed with a thiosulfate salt lixiviant, which mixture is maintained at a pH between 7 and 8.7 while the slurry is agitated in a stirred tank reactor system having agitated leach tanks. Gold is recovered from the gold-bearing leachate by cementation, adsorption on an adsorbent, or cyanidation.

Claims

1. 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 to form a mixture of oxidized ore slurry and lixiviant;

leaching gold from the oxidized slurry in a stirred tank reactor system comprising between two and six agitated leach tanks by maintaining the mixture at a pH between 7 and 8.7 while agitating the mixture with a slurry residence time in each of said tanks of between about 30 and about 120 minutes to produce a leached slurry comprising a solid residue and a gold-bearing leachate; and

recovering gold from the gold-bearing leachate.

2. The process of claim 1 wherein said gold is recovered from the gold-bearing leachate by zinc, copper, or iron cementation.

3. The process of claim 1 further comprising recovering ammonia from the leached slurry by adding a basic compound and aerating to drive off ammonia in an off-gas, scrubbing said off-gas to remove ammonia therefrom, and recycling ammonia to said leaching step.

4. The process of claim 1 comprising contacting the gold-bearing leachate with an adsorbent in order to load gold-thiosulfate complex from the leachate onto the adsorbent;

and

recovering gold from the gold-thiosulfate complex adsorbed onto the adsorbent.

5. The process of claim 1 comprising contacting the gold-bearing leachate with cyanide ion and an adsorbent in the presence of the solid residue to produce an aurocyanide complex which is loaded onto the adsorbent;

and

recovering gold from the aurocyanide complex adsorbed onto the adsorbent.

6. The process of claim 1 comprising separating the gold-bearing leachate from the solid residue;

contacting the gold-bearing leachate with cyanide ion to produce an aurocyanide complex in solution;

contacting the aurocyanide complex in solution with an adsorbent to load the aurocyanide complex onto the adsorbent; and

recovering gold from the aurocyanide complex adsorbed onto the adsorbent.

7. The process of claim 1 comprising separating the gold-bearing leachate from the solid residue;

contacting the gold-bearing leachate with cyanide ion and an adsorbent simultaneously to produce an aurocyanide complex which is loaded onto the adsorbent; and

recovering gold from the aurocyanide complex adsorbed onto the adsorbent.

8. The process of claim 1 wherein said pressure oxidation occurs under acidic conditions to produce a pressure oxidized slurry having a pH of less than about 1 and raising said pH of the oxidized slurry to between 7 and 8.7 prior to mixing the oxidized ore slurry with the lixiviant.

9. The process of claim 1 comprising the addition of between about 50 and about 200 ppm chloride to the ore slurry prior to pressure oxidation.

10. 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 in a stirred tank reactor system comprising between two and six agitated leach tanks by maintaining the mixture at a pH between 7 and 8.7 while agitating the mixture with a slurry residence time in each of said tanks of between about 30 and about 120 minutes to produce a leached slurry comprising a solid residue and a gold-bearing leachate; and

recovering gold from the gold-bearing leachate.

11. The process of claim 10 wherein said gold is recovered from the gold-bearing leachate by cementation with zinc, copper, or iron.

12. The process of claim 10 comprising contacting the gold-bearing leachate with an adsorbent in order to load gold-thiosulfate complex from the leachate onto the adsorbent;

and

recovering gold from the gold-thiosulfate complex adsorbed onto the adsorbent.

13. The process of claim 10 comprising contacting the gold-bearing leachate with cyanide ion and an adsorbent in the presence of the solid residue to produce an aurocyanide complex which is loaded onto the adsorbent;

and

recovering gold from the aurocyanide complex adsorbed onto the adsorbent.

14. The process of claim 10 comprising separating the gold-bearing leachate from the solid residue;

contacting the gold-bearing leachate with cyanide ion to produce an aurocyanide complex in solution;

contacting the aurocyanide complex in solution with an adsorbent to load the aurocyanide complex onto the adsorbent; and

recovering gold from the aurocyanide complex adsorbed onto the adsorbent.

15. The process of claim 10 comprising separating the gold-bearing leachate from the solid residue;

contacting the gold-bearing leachate with cyanide ion and an adsorbent simultaneously to produce an aurocyanide complex which is loaded onto the adsorbent; and

recovering gold from the aurocyanide complex adsorbed onto the adsorbent.

16. The process of claim 10 comprising adding between about 5 and 40 kg sodium hydroxide per ton of ore to the ore slurry to be subjected to pressure oxidation.

17. 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 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 for between about 30 and about 100 minutes in an autoclave at a temperature in the range of between about 185° and

235°

C. and an oxygen overpressure of at least about 20 psi to produce an oxidized ore slurry;

cooling the oxidized ore slurry to a temperature between about 40°

C. and about 55°

C.;

adjusting the pH of the oxidized slurry to between 7 and 8.7;

mixing the oxidized slurry with a lixiviant comprising a thiosulfate salt in a proportion of between about 0.025M and 0.1M thiosulfate ion, copper in a proportion of between about 50 and 100 ppm, and sulfite in a proportion of at least about 0.001M, while maintaining the pH between 7 and 8.7;

maintaining the oxidized slurry and lixiviant at a temperature in the range of between 40°

C. and 55°

C. while agitating the slurry in a stirred tank reactor system comprising between two and six mechanically agitated leach tanks with a residence time of the slurry in each tank of between about 30 and 120 minutes to produce a leached slurry comprising a solid residue and a gold-bearing leachate; and

recovering gold from the gold-bearing leachate.

18. The process of claim 17 wherein said gold is recovered from the gold-bearing leachate by cementation with zinc, copper, or iron.

19. The process of claim 17 comprising contacting the gold-bearing leachate with an adsorbent in order to load gold-thiosulfate complex from the leachate onto the adsorbent;

and

recovering gold from the gold-thiosulfate complex adsorbed onto the adsorbent.

20. The process of claim 17 comprising contacting the gold-bearing leachate with cyanide ion and an adsorbent in the presence of the solid residue to produce an aurocyanide complex which is loaded onto the adsorbent;

and

recovering gold from the aurocyanide complex adsorbed onto the adsorbent.

21. The process of claim 17 comprising separating the gold-bearing leachate from the solid residue;

contacting the gold-bearing leachate with cyanide ion to produce an aurocyanide complex in solution;

contacting the aurocyanide complex in solution with an adsorbent to load the aurocyanide complex onto the adsorbent; and

recovering gold from the aurocyanide complex adsorbed onto the adsorbent.

22. The process of claim 17 comprising separating the gold-bearing leachate from the solid residue;

contacting the gold-bearing leachate with cyanide ion and an adsorbent simultaneously to produce an aurocyanide complex which is loaded onto the adsorbent; and

recovering gold from the aurocyanide complex adsorbed onto the adsorbent.