Efficient copper leaching using alkanesulfonic acids

Patent metadata

Field	Value
Publication number	US-12077834-B2
Application number	US-201916976479-A
Country	US
Kind code	B2
Filing date	Feb 28, 2019
Priority date	Feb 28, 2018
Publication date	Sep 3, 2024
Grant date	Sep 3, 2024

Abstract

The present invention relates to use of alkysulfonic acids, with optionally an oxidant peroxide to leach copper from copper sulfide minerals or copper concentrates, a dichromate oxidant or a nitrate oxidant, or a combination thereof.

First claim

We claim:

1. A method of extracting copper from a copper sulfide mineral comprising contacting said copper sulfide mineral with an alkylsulfonic acid and optionally a peroxide, a dichromate salt, or a nitrate salt, or a combination thereof, wherein the peroxide is chosen from the group consisting of hydrogen peroxide and metal peroxide.

2. The method of claim 1 , wherein said copper sulfide mineral is Chalcopyrite (CuFeS 2 ), Covellite (CuS), Chalcocite (Cu 2 S), Enargite (CusAsS 4 ), Bornite (Cu 5 FeS 4 ), or Digenite (Cu 9 S 5 ).

3. The method of claim 1 , wherein said peroxide is in contact with copper ore for about 24 to about 96 hours.

4. The method of claim 1 , wherein said peroxide is added to said copper sulfide mineral or said copper concentrate periodically at a rate of about every 24 hours for up to about 48 hours to about 96 hours.

5. The method of claim 1 , wherein said peroxide is present in a concentration of about 0.3 to about 15% (v/v) peroxide.

6. The method of claim 1 , wherein said peroxide is present in a concentration of about 0.3 to about 4.5% (v/v) peroxide.

7. The method of claim 1 , wherein the alkylsulfonic acid is methanesulfonic acid present in a concentration of about 30 g/L and the peroxide is hydrogen peroxide present in a concentration of about 0.9% (v/v).

8. The method of claim 1 , wherein additional hydrogen peroxide is added periodically at a rate of about 24 hours for up to about 96 hours.

9. The method of claim 1 , wherein said alkylsulfonic acid is present at a concentration of about 1 to about 300 g/L.

10. The method of claim 1 , wherein said extraction is carried out at a temperature of about 20° C. to about 100° C.

11. The method of claim 1 , wherein said extraction is carried out at a pulp density of about 1%, 2%, 4.7%, or 9.1%.

12. The method of claim 1 , wherein said copper content is about 20% to about 40%.

13. The method of claim 1 , wherein said alkylsulfonic acid is methanesulfonic acid, ethanesulfonic acid, or propanesulfonic acid.

14. The method of claim 1 , wherein said nitrate salt and/or dichromate salt is in contact with copper ore for about 24 hours.

15. The method of claim 1 , wherein said nitrate salt is sodium nitrate (NaNO 3 ) or potassium nitrate (KNO 3 ).

16. The method of claim 1 , wherein said dichromate salt is potassium dichromate (K 2 Cr 2 O 7 ) or sodium dichromate (Na 2 Cr 2 O 7 ).

Assignees

• Univ Arizona

Inventors

• Lee Jaeheon
• Ahn Junmo

Classifications

• Y02P10/20

  Recycling · CPC title

• C22B3/165

  with organic acids · 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

  with acids or salts thereof · CPC title

• C22B15/0071 Primary

  containing sulfur · CPC title