Leaching copper-containing ores

Patent metadata

Field	Value
Publication number	US-10563287-B2
Application number	US-201816230150-A
Country	US
Kind code	B2
Filing date	Dec 21, 2018
Priority date	Apr 6, 2017
Publication date	Feb 18, 2020
Grant date	Feb 18, 2020

Abstract

A method of leaching copper-containing ores, such as chalcopyrite ores, with a leach liquor in the presence of silver and an activation agent that activates silver whereby the silver enhances copper extraction from copper ores.

First claim

The invention claimed is:

1. A method of leaching copper-containing ores with a leach liquor including:
(a) forming agglomerates by a step selected from (i) mixing together ore fragments and silver in an agglomeration step, (ii) adding silver to ore fragments and then mixing together ore fragments in an agglomeration step, or (iii) forming agglomerates in an agglomeration step and then adding silver to the agglomerates, with the agglomerates having a low added silver concentration of less than 5 g silver per kg copper in the ore in agglomerates, and
(b) leaching agglomerates in the presence of an activation agent that activates silver whereby the silver enhances copper extraction from copper ores, with the activation agent being in the form of any one or more than one of chlorides, iodides, bromides, and thiourea.

2. The method defined in claim 1 wherein the leaching is selected from the group consisting of heap, vat, and tank leaching.

3. The method defined in claim 1 includes providing a selected concentration or concentration range of the activation agent in the leach liquor.

4. The method defined in claim 3 wherein the selected concentration or concentration range of the activation agent in the leach liquor results from any one or more of the following positive steps:
(a) addition of the activation agent to the leach liquor;
(b) removal of the activation agent from the leach liquor;
(c) addition of the activation agent in the agglomeration step;
(d) mixing different ore types having regard to the activation agent in the ores;
(e) selection and mixing/blending of water source/type regard to the activation agent in the ores; and
(f) other human-intervention into one or more inputs to the method of leaching that can affect the activation agent concentrations in the method of leaching.

5. The method defined in claim 1 wherein the leaching is carried out in the presence of a low concentration or concentration range of the activation agent.

6. The method defined in claim 5 wherein the leaching is carried out in the presence of a low concentration of chlorides, iodides, and bromides of up to 5 g/L in the leach liquor.

7. The method defined in claim 6 wherein the low concentration of chlorides is greater than 0.8 g/L.

8. The method defined in claim 5 wherein the leaching is carried out in the presence of a low concentration of chlorides of greater than 0.2 g/L.

9. The method defined in claim 5 wherein the leaching is carried out in the presence of a low concentration of thiourea of less than 10 g/L in the leach liquor.

10. The method defined in claim 5 wherein the low concentration of chlorides, iodides and bromides is up to 4 g/L in the leach liquor.

11. The method defined in claim 1 includes adding the activation agent to the leach liquor during the method to maintain a required concentration.

12. The method defined in claim 1 includes leaching a heap of agglomerates with the leach liquor.

13. The method defined in claim 12 wherein heap leaching includes bioleaching with microorganisms to assist leaching of copper.

14. The method defined in claim 12 wherein heap leaching includes controlling heap temperature to be less than 85° C.

15. The method defined in claim 12 includes controlling oxidation potential of the leach liquor during an active leaching phase of heap leaching to be less than 900 mV versus a standard hydrogen electrode.

16. The method defined in claim 12 includes recovering copper from the leach liquor in downstream copper recovery steps.

17. The method defined in claim 16 includes regenerating the leach liquor and recycling the regenerated leach liquor to the heap of agglomerates.

18. The method defined in claim 12 wherein heap leaching includes controlling the heap temperature to be less than 50° C.

19. The method defined in claim 1 wherein the added silver concentration in agglomerates is less than 2 g silver per kg copper in the ore in agglomerates.

20. The method defined in claim 1 wherein the added silver concentration in agglomerates is less than 1 g silver per kg copper in the ore in the agglomerates.

21. The method defined in claim 1 wherein the added silver concentration in agglomerates is less than 0.5 g silver per kg copper in the ore in the agglomerates.

22. The method defined in claim 1 wherein added silver concentration in agglomerates is greater than 0.02 g silver per kg copper in the ore in agglomerates.

23. The method defined in claim 22 wherein the added silver concentration in agglomerates is greater than 0.2 g silver per kg copper in the ore in agglomerates.

24. The method defined in claim 1 includes steps (a)(i) or (a)(ii) and comprises adding the silver in a solution or in a solid form to chalcopyrite ore fragments.

25. The method defined in claim 1 includes forming agglomerates by also mixing microorganisms that can assist leaching of copper.

26. The method defined in claim 1 includes steps (a)(i) or (a)(ii) and comprises adding the silver in a spray or a mist to chalcopyrite ore fragments.

27. The method defined in claim 1 includes steps (a)(i) or (a)(ii) and comprises adding the silver in an aerosol to chalcopyrite ore fragments.

28. A method of leaching copper-containing ores that includes:
(a) forming agglomerates of fragments of (i) a copper-containing ore, (ii) silver, (iii) an acid, and (iv) optionally microorganisms, wherein the agglomerate forming step includes any one of (i) mixing together ore fragments and added silver in an agglomeration step, (ii) adding silver to ore fragments and then mixing together ore fragments in an agglomeration step, and (iii) adding silver to the agglomerates after the agglomerates have been formed, and wherein the added silver concentration in the agglomerates is less than 1 g silver per kg copper in the ore in the agglomerates;
(b) forming a heap of the agglomerates;
(c) leaching the agglomerates in the heap with a leach liquor in the presence of an activation agent that activates silver whereby the silver enhances copper extraction, with the activation agent being any one or more than one of chlorides, iodides, bromides, and thiourea; and
(d) recovering copper from the leach liquor.

29. A method of leaching copper-containing ores that includes:
(a) forming agglomerates of fragments of (i) a copper-containing ore, (ii) an acid, (iii) optionally silver, and (iv) optionally microorganisms, wherein when addition of silver is required, the agglomerate forming step includes any one of (i) mixing together ore fragments and added silver in an agglomeration step, (ii) adding silver to ore fragments and then mixing together ore fragments in an agglomeration step, and (iii) adding silver to the agglomerates after the agglomerates have been formed, wherein the amount of added silver is determined by taking into account catalyst properties for copper leaching of naturally occurring silver in the ore, and wherein the added silver concentration in the agglomerates is less than 1 g silver per kg copper in the ore in the agglomerates;
(b) forming a heap of the agglomerates;
(c) leaching the agglomerates in the heap with a leach liquor in the presence of an activation agent that activates silver whereby the silver enhances copper extraction, with the activation agent being any one or more than one of chlorides, iodides, bromides, and thiourea;

Assignees

• Tech Resources Pty Ltd

Inventors

• Hackl Ralph Peter
• Brown Paul Leslie
• Grocott Stephen Charles
• Kittelty Daniel Arthur

Classifications

• C22B3/18

  with the aid of microorganisms or enzymes, e.g. bacteria or algae · CPC title

• C22B3/06

  in inorganic acid solutions {, e.g. with acids generated in situ; in inorganic salt solutions other than ammonium salt solutions} · CPC title

• C22B15/0067 Primary

  with acids or salts thereof · CPC title

• C22B15/0065

  Leaching or slurrying (with organic compounds C22B3/16) · CPC title

• C22B15/0069

  containing halogen · CPC title