IP Library Granted Patent US 10,961,633
Granted Patent B2
US 10,961,633 · App. 15/096,722 · Granted Mar 30, 2021

Recovery of copper from copper-containing sulfide ores

Inventor: Timothy Roy Hymer (Labadie, MO)
Assignee: THE DOE RUN RESOURCES CORPORATION
C25C1/12C22B3/10C22B15/0069C22B15/0078C22B15/0084Y02P10/20
View Patent ↗
Loading inventors, assignments & file history…
Monitor This Case
Get email alerts when status or documents change.
Order Certified Copies
Most orders are placed with the USPTO same day — all within 24 business hours.
Order via The Patent Place →
Pre-filled with this patent's details
Quick Facts
Patent No.
US 10,961,633
App. No.
15/096,722
Granted
Mar 30, 2021
Kind
B2
Abstract

A process for recovering copper from copper sulfide minerals, the method comprising the steps of leaching copper sulfide minerals with an aqueous solution of ammonium chloride containing cupric chloride at a temperature of between about 40° C. and about 95° C. at atmospheric pressure, to produce a solution of cuprous/cupric chloride.

Claims (20)

1. A process for recovering copper from copper sulfide minerals, the method comprising the steps of:

leaching copper sulfide minerals with an aqueous solution of ammonium chloride containing cupric chloride at a temperature of between about 75° C. and about 85° C. and a pH of between about 4 and about 7, at atmospheric pressure, to produce a solution of cuprous/cupric chloride.

2. The process according to claim 1 , wherein the copper sulfide minerals include at least one of Pb, Zn, Ag, Au, Fe, As, or Sb.

3. The process according to claim 1 , having cupric present.

4. The process according to claim 1 , having a range of NH 4 Cl from 50 g/l to 350 g/l.

5. The process according to claim 1 , further comprising at least one of NaCl and KCl.

6. The process according to claim 1 , using O 2 or air to regenerate the cuprous to cupric.

7. The process according to claim 1 , using agitated leach tanks or use in heap leaching.

8. The process according to claim 1 , using solvent extraction to recover copper from leach solution.

9. The process according to claim 1 , using direct electrowinning of copper from leach solution.

10. A process for recovering copper from copper sulfide minerals, the method comprising the steps of:

leaching copper sulfide minerals with an aqueous solution of ammonium chloride containing cupric chloride at a temperature of between about 75° C. and about 85° C. and a pH of between about 4 and about 7, at atmospheric pressure, to produce a solution of cuprous/cupric chloride:

filtering the solution resulting from the leaching step; subjecting the filtered solution to recover the copper as a product.

11. The process according to claim 10 , wherein the copper sulfide minerals include at least one of Pb, Zn, Ag, Au, Fe, As, or Sb.

12. The process according to claim 10 , having cupric present.

13. The process according to claim 10 , having a range of NH 4 Cl from 50 g/l to 350 g/l.

14. The process according to claim 10 , further comprising at least one of NaCl and KCl.

15. The process according to claim 10 , using O 2 or air to regenerate the cuprous to cupric.

16. The process according to claim 10 , using agitated leach tanks or use in heap leaching.

17. The process according to claim 10 , using ion exchange to recover copper from leach solution.

Assignments (2)
SECURITY AGREEMENT Recorded Oct 17, 2017
From: THE DOE RUN RESOURCES CORPORATION
To: WELLS FARGO BANK, NATIONAL ASSOCIATION
Reel/Frame 044217/0739 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded May 4, 2016
From: HYMER, TIMOTHY ROY
To: THE DOE RUN RESOURCES CORPORATION
Reel/Frame 038453/0265 →
Continuity (2)
Provisional Application 62146953 · Apr 13, 2015
Related Publication 20160298248A1 · Oct 13, 2016