Method to improve recovery of gold from double refractory gold ores

• US 8,262,768 B2
• Filed: 09/11/2008
• Issued: 09/11/2012
• Est. Priority Date: 09/17/2007
• Status: Active Grant

• Current Assignee: Barrick Gold Corporation
• Original Assignee: Barrick Gold Corporation
• Inventors: Gorain, Barun, Kondos, Peter
• Primary Examiner(s): Yang, Jie
• Application Number:
  US12/208,985
• Publication Number:
  US 20090071295A1
• Time in Patent Office: 1,461 Days
• Field of Search: 757/44, 757/10, 423/26
• US Class Current: 75/710
• CPC Class Codes: B03D 1/02 Froth-flotation processes
• 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 11/08 by cyaniding
• CPC Class Codes: C22B 3/04 by leaching C22B3/18 takes precedence
• CPC Class Codes: C22B 3/24 by adsorption on solid substances, e.g. by extraction with solid resins
• CPC Class Codes: Y02P 10/20 Recycling

Abstract

The present invention is directed to a precious metal recovery process in which carbonaceous material, such as preg robbing carbon, is floated after sulfide oxidation to separate the carbonaceous material from the precious metal.

Claims

1. A method, comprising:

(a) providing a feed material comprising a precious metal, at least about 0.1 wt. % sulfide sulfur, and 0.3 to about 10 wt. % carbonaceous materials;

(b) oxidizing at least a portion of the sulfide sulfur in the feed material to provide an oxidized material, wherein at least most of the gold and/or silver and carbonaceous materials remain in the oxidized feed material;

(c) comminuting the oxidized material to remove, at least partially, an oxidative film on at least some particles of the oxidized feed material;

(d) after step (b), floating the comminuted and oxidized feed material to separate the material into a first fraction comprising at least most of the gold and/or silver and a second fraction comprising at least about 25 wt. % of the carbonaceous materials in the feed material, wherein the comminuted and oxidized feed material is free of precious metal leaching prior to the floating step;

(e) comminuting the second fraction to provide a comminuted second fraction;

(f) floating the comminuted second fraction to form cleaner tails comprising most of the gold and/or silver in the comminuted second fraction and a cleaner concentrate comprising most of the carbonaceous material in the comminuted second fraction; and

(g) after floating is completed, thereafter recovering the gold and/or silver from the first fraction and the cleaner tails, wherein the first fraction and the cleaner tails comprise at least about 90% of the gold and/or silver in the oxidized material.

2. The method of claim 1, further comprising:

(f) conditioning the comminuted and oxidized material by contacting the comminuted and oxidized material with a collector that renders the carbonaceous material more hydrophobic, wherein the conditioned comminuted and oxidized material is subjected to flotation in step (d).

3. The method of claim 2, wherein at least one of a sulfide depressant and carbonaceous material activator is contacted with the comminuted and oxidized material during conditioning.

4. The method of claim 2, further comprising:

conditioning the comminuted second fraction by contacting the comminuted second fraction with the collector that renders the carbonaceous material more hydrophobic.

5. A method, comprising:

(a) providing a feed material comprising a precious metal, at least about 0.1 wt. % sulfide sulfur, and 0.3 to about 10 wt. % carbonaceous materials;

(b) pressure oxidizing at least a portion of the sulfide sulfur in the feed material to provide an oxidized material, wherein at least most of the gold and/or silver and carbonaceous materials remain in the oxidized feed material; and

(c) after step (b) floating the oxidized feed material to separate the material into a first fraction comprising at least about 70 wt. % of the gold and/or silver in the oxidized feed material and a second fraction comprising no less than about 40 wt. % of the carbonaceous materials in the feed material;

(d) comminuting the second fraction to provide a comminuted second fraction; and

(e) floating the comminuted second fraction to form cleaner tails comprising most of the gold and/or silver in the comminuted second fraction and a cleaner concentrate comprising most of the carbonaceous material in the comminuted second fraction, wherein the first fraction and the cleaner tails comprise at least about 90% of the gold and/or silver in the oxidized material.

6. The method of claim 5, further comprising:

after step (c) comminuting the oxidized material to remove, at least partially, an oxidative film on at least some particles of the oxidized material, wherein the comminuted and oxidized material is subjected to flotation in step (c).

7. The method of claim 6, further comprising:

after comminuting the oxidized material, conditioning the comminuted and oxidized material by contacting the comminuted and oxidized material with a collector that renders the carbonaceous material more hydrophobic, wherein the conditioned comminuted and oxidized material is subjected to flotation in step (c).

8. The method of claim 7, wherein at least one of a sulfide depressant and carbonaceous material activator is contacted with the comminuted and oxidized material during conditioning.

9. The method of claim 7, wherein the first fraction is a rougher concentrate and the second fraction is a rougher tails and further comprising:

(f) comminuting the second fraction to provide a comminuted second fraction;

(g) conditioning the comminuted second fraction by contacting the comminuted second fraction with the collector; and

(h) floating the comminuted second fraction to form a third fraction comprising most of the gold and/or silver in the second fraction and a fourth fraction comprising most of the carbonaceous material in the second fraction.

10. The method of claim 9, wherein the oxidized feed material, prior to the floating step, is free of precious metal leaching and further comprising:

recovering gold and/or silver from the first and third fractions.

11. The method of claim 5, wherein the oxidized feed material is free of precious metal leaching before the floating step.

12. A method, comprising:

(a) providing a feed material comprising a precious metal, at least about 0.1 wt. % sulfide sulfur, and 0.3 to about 10 wt. % carbonaceous materials;

(b) pressure oxidizing at least a portion of the sulfide sulfur in the feed material to provide an oxidized material, wherein at least most of the gold and/or silver and carbonaceous materials remain in the oxidized feed material; and

(c) thereafter floating the oxidized feed material to separate the material into a first fraction comprising at least most of the gold and/or silver and a second fraction comprising at least about 25 wt. % of the carbonaceous materials in the feed material;

(d) comminuting the second fraction to provide a comminuted second fraction; and

(e) floating the comminuted second fraction to form cleaner concentrate comprising most of the gold and/or silver in the comminuted second fraction and a cleaner tails comprising most of the carbonaceous material in the comminuted second fraction, wherein the first fraction and the cleaner concentrate comprise at least about 90% of the gold and/or silver in the oxidized material.

13. The method of claim 12, further comprising:

comminuting the oxidized material to remove, at least partially, an oxidative film on at least some particles of the oxidized material, wherein the comminuted and oxidized material is subjected to flotation in step (c).

14. The method of claim 13, further comprising:

after the comminuting the oxidized material, conditioning the comminuted and oxidized material by contacting the comminuted and oxidized material with a collector that renders the carbonaceous material more hydrophilic, wherein the conditioned comminuted and oxidized material is subjected to flotation in step (c).

15. The method of claim 14, wherein at least one of a carbon depressant and sulfide activator is contacted with the comminuted and oxidized material during conditioning.

16. The method of claim 14, further comprising:

(f) comminuting the second fraction to provide a comminuted second fraction;

(g) conditioning the comminuted second fraction by contacting the comminuted second fraction with the collector; and

(h) floating the comminuted second fraction to form a fourth fraction comprising most of the gold and/or silver in the second fraction and a third fraction comprising most of the carbonaceous material in the second fraction.

17. The method of claim 16, further comprising:

recovering gold and/or silver from the first fraction and the fourth fractions.