Heap Leaching

Patent metadata

Field	Value
Publication number	US-2019382869-A1
Application number	US-201615772296-A
Country	US
Kind code	A1
Filing date	Oct 28, 2016
Priority date	Oct 30, 2015
Publication date	Dec 19, 2019
Grant date	—

Abstract

A method of leaching chalcopyrite ores includes the steps of forming agglomerates of fragments of chalcopyrite ores and silver and leaching the agglomerates with suitable leach liquor.

First claim

1 . A method of leaching chalcopyrite ores includes the steps of:
(a) forming agglomerates of fragments of chalcopyrite ores and silver, defined herein as “added silver”, the agglomeration step including adding silver in a solution as a spray or a mist or in a solid form as an aerosol to the chalcopyrite ore fragments while the fragments are being mixed together; and (b) leaching the agglomerates with suitable leach liquor.

2 . The method defined in claim 1 wherein the agglomerates formed in the agglomeration step (a) have a low added silver concentration of less than 2 g silver per kg copper in the ore in the agglomerates.

3 - 9 . (canceled)

10 . The method defined in claim 1 wherein the agglomeration step (a) includes adding silver to the chalcopyrite ore fragments in the aerosol.

11 . The method defined in claim 1 wherein the agglomeration step (a) includes adding silver in the mist or the spray.

12 . The method defined in claim 1 wherein the agglomeration step (a) includes forming agglomerates by also mixing together an acid, typically sulfuric acid, with the chalcopyrite ore fragments and the added silver.

13 . (canceled)

14 . The method defined in claim 1 wherein the agglomeration step (a) includes forming agglomerates by also mixing microorganisms that can assist leaching of copper with the chalcopyrite ore fragments and added silver.

15 . (canceled)

16 . The method defined in claim 1 wherein the agglomeration step (a) includes simultaneously mixing and agglomerating fragments and the added silver.

17 . The method defined in claim 1 wherein the agglomeration step (a) includes mixing fragments in one step and then agglomerating the mixed fragments and the added silver in a subsequent step.

18 - 20 . (canceled)

21 . The method defined in claim 1 wherein the leaching step (b) is a heap leaching step.

22 . (canceled)

23 . The method defined in claim 21 wherein the heap leaching step (b) includes controlling the heap temperature to be less than 75° C., typically less than 65° C., typically less than 60° C., typically less than 55° C., typically less than 50° C., and more typically less than 45° C.

24 . The method defined in claim 21 includes controlling the oxidation potential of the leach liquor during an active leaching phase of the step to be less than 700 mV versus the standard hydrogen electrode in the heap leaching step (b).

25 . A method of leaching chalcopyrite ores includes the steps of:
(a) forming agglomerates of fragments of chalcopyrite ores and silver, defined herein as “added silver”, wherein the agglomerates formed in the agglomeration step (a) have a low added silver concentration of less than 1 g silver per kg copper in the ore in the agglomerates; and (b) leaching the agglomerates with suitable leach liquor.

26 - 28 . (canceled)

29 . The method defined in claim 25 wherein the added silver concentration in the agglomerates is less than 0.5 g silver per kg copper in the ore in the agglomerates.

30 . The method defined in claim 29 wherein the added silver concentration in the agglomerates is less than 0.25 g silver per kg copper in the ore in the agglomerates.

31 . The method defined in claim 29 wherein the added silver concentration in the agglomerates is less than 0.125 g silver per kg copper in the ore in the agglomerates.

32 . The method defined in claim 29 wherein the added silver concentration in the agglomerates is less than 0.075 g silver per kg copper in the ore in the agglomerates.

33 - 49 . (canceled)

50 . The method defined in claim 25 wherein the leaching step (b) is a heap leaching step.

51 . (canceled)

52 . The method defined in claim 50 wherein the heap leaching step (b) includes controlling the heap temperature to be less than 75° C., typically less than 65° C., typically less than 60° C., typically less than 55° C., typically less than 50° C., and more typically less than 45° C.

53 . The method defined in claim 50 includes controlling the oxidation potential of the leach liquor during an active leaching phase of the step to be less than 700 mV versus the standard hydrogen electrode in the heap leaching step (b).

54 . Agglomerates of fragments of chalcopyrite ores and silver suitable for use in a heap or other leaching process, with the silver being dispersed through the agglomerates, with the silver being defined herein as “added silver”, and with the added silver concentration in the agglomerates being less than 1 g silver per kg copper in the ore in the agglomerates.

55 - 64 . (canceled)

Assignees

• Tech Resources Pty Ltd

Inventors

• Brown Paul Leslie
• Hackl Ralph Peter
• Grocott Stephen Charles

Classifications

• C22B15/0067 Primary

  with acids or salts thereof · CPC title

• C22B3/18

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

• C22B3/08 Primary

  Sulfuric acid {, other sulfurated acids or salts thereof} · CPC title

• C22B15/0071

  containing sulfur · CPC title

• Y02P10/20

  Recycling · CPC title