IP Library Granted Patent US 8,070,851
Granted Patent B2
US 8,070,851 · App. 12/266,028 · Granted Dec 6, 2011

Chloride heap leaching

Assignee: BHP Billiton SA Limited
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Quick Facts
Patent No.
US 8,070,851
App. No.
12/266,028
Granted
Dec 6, 2011
Kind
B2
Abstract

A heap leaching method to recover copper from a primary copper sulphide mineral wherein the mineral is leached in an acidic chloride/sulphate solution in the presence of oxygen with the surface potential of the mineral below 600 mV (vs. SHE) to cause dissolution of the copper sulphide.

Claims (12)

1. A hydrometallurgical method of recovering copper from a material, in a heap, that contains a copper sulphide mineral which contains at least chalcopyrite comprising leaching the material in an acidic chloride solution or a mixed chloride/sulphate solution in the presence of dissolved oxygen and maintaining the mineral's surface potential within a range of 550 mV (vs. SHE) to 600 mV (vs. SHE) by controlling the chloride ion concentration at a level between 5 g/L to 100 g/L to control the ratio of Cu(II) to Cu(I) within the solution to cause dissolution of at least 40% of the copper sulphide in about 600 hours, and recovering copper from the solution.

2. The method according to claim 1 wherein the copper sulphide is in a low-grade transitional and hypogene ore.

3. The method according to claim 1 wherein the copper sulphide is in a low-grade supergene ore.

4. The method according to claim 1 wherein the pH of the solution is less than about 3.

5. The method according to claim 4 wherein the pH of the solution is between about 1 and about 2.

6. The method according to claim 1 which includes the steps of controlling the pH of the solution by the addition of H 2 SO 4 , HCl or HNO 3 .

7. The method according to claim 1 wherein the dissolved oxygen level is in excess of 1 ppm.

8. The method according to claim 1 wherein the chloride concentration is controlled by the addition of at least one of the following: HCl, NaCl, MgCl 2 , saline water, sea water or chloride-containing process water.

9. The method according to claim 1 comprising maintaining the mineral's surface potential within a range of 550 mV (vs. SHE) to 580 mV (vs. SHE).

10. The method according to claim 1 wherein the leaching solution contains less than about 5 g/L ferric ion.

11. The method according to claim 1 wherein the leaching solution does not contain any ferric ions.

12. The method according to claim 1 wherein the leaching is conducted at ambient temperature.

Assignments (3)
CHANGE OF ADDRESS Recorded Jul 11, 2022
From: CONSOLIDATED NOMINEES (PTY) LTD.
To: CONSOLIDATED NOMINEES (PTY) LTD.
Reel/Frame 060620/0546 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jun 23, 2015
From: BHP BILLITON SA LIMITED
To: CONSOLIDATED NOMINEES (PTY) LTD
Reel/Frame 035951/0690 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Mar 19, 2009
From: MULLER, ELMAR L.; BASSON, PETRUS; NICOL, MICHAEL J.
To: BHP BILLITON SA LIMITED
Reel/Frame 022420/0650 →
Priority Claims (1)
ZA 2006/03788 · May 12, 2006 · national
Continuity (2)
Continuation PCTZA2007000025 · May 9, 2007
Related Publication 20090173188A1 · Jul 9, 2009