Method of recovering copper from a dilute metal containing solution

Patent metadata

Field	Value
Publication number	US-10934192-B2
Application number	US-201716471586-A
Country	US
Kind code	B2
Filing date	Dec 19, 2017
Priority date	Dec 20, 2016
Publication date	Mar 2, 2021
Grant date	Mar 2, 2021

Abstract

The invention relates to a method of removing and/or recovering metals from a dilute metal containing solution. In particular, the invention concerns a method for recovering copper from a dilute copper-iron bearing mining water, particularly from a copper-iron bearing mining wastewater.

First claim

The invention claimed is:

1. A method of recovering and/or removal of copper from a copper-iron containing solution comprising:
a) an electrodeposition step, wherein an external potential or current is applied to an electrode placed in the copper-iron containing solution, thereby depositing iron and optionally copper on the electrode;
b) a redox replacement step, wherein the applied external potential or current used in step a) is cut-off and iron deposited on the electrode reduces spontaneously the copper still present in the solution, resulting in a deposit on the electrode which contains copper and possible iron;
c) optionally repeating steps a) and b); and
d) recovering copper from the electrode.

2. The method according to claim 1 , wherein the copper-iron containing solution has an iron concentration which is >10 ppm.

3. The method according to claim 1 , wherein the copper-iron containing solution has a copper concentration which is less than 100 ppm.

4. The method according to claim 1 , wherein the copper-iron containing solution has a Fe/Cu concentration ratio, which is 4<Fe/Cu<40000.

5. The method according to claim 1 , wherein the copper-iron containing solution is a mining water, and wherein the copper-iron containing solution further comprises noble metals, metal complexes, or compounds which are subjected to the redox replacement step along with copper and can be removed and/or recovered with the copper.

6. The method according to claim 5 , wherein the mining water has a concentration of the noble metals, metal complexes or compounds of less than 1 ppm.

7. The method according to claim 1 , wherein the copper-iron containing solution originates from a sulphide mineral mine, as a bleed or tailing water from a concentrator, from a flotation plant, from an abandoned mine, or from a leaching plant after metal recovery.

8. The method according to claim 1 , wherein the electrode(s) are in a form selected from the group consisting of a plate, ring, sheet, mesh, and stick.

9. The method according to claim 1 , wherein the electrodeposition step is conducted at a constant current, at a constant potential, or by varying the potential or current in a range in which iron deposits on the electrode.

10. The method according to claim 1 , wherein an external potential is applied in the electrodeposition step, and wherein the external potential in the electrodeposition step is such that iron can deposit on the electrode and hydrogen evolution does not destroy the deposition.

11. The method according to claim 1 , wherein an external potential is applied in the electrodeposition step, wherein the electrode comprises a platinum electrode, and wherein the applied potential is less than +0.2 V vs. SCE (saturated calomel electrode).

12. The method according to claim 1 , wherein a current is applied in the electrodeposition step, and wherein an absolute value of a current density in the electrodeposition step is in the range of 0.01-1000 mA/cm 2 .

13. The method according to claim 1 , wherein step a) has a residence time which is 1 second-60 minutes.

14. The method according to claim 1 , wherein the redox replacement step b) is finished after a pre-determined time or when an open circuit potential value reaches a pre-determined value.

15. The method according to claim 1 , wherein the electrode comprises a platinum electrode, and wherein the redox replacement step b) is finished when an open circuit potential value reaches a predetermined value, which is below 0.5 V vs. SCE (saturated calomel electrode).

16. The method according to claim 1 , wherein the redox replacement step b) is finished after a pre-determined time period that allows the replacement of iron to copper to take place, and wherein the pre-determined time period comprises 3 seconds-30 minutes.

17. The method according to claim 1 , wherein steps a) and b) are repeated consecutively (cycled) 1 to 100000 times before the recovering copper from the electrode.

18. The method according to claim 1 , wherein the electrode obtained after step a), after step b), or subsequent to cycling between steps a) and b), is subjected to leaching, a hydrometallurgical method, a pyrometallurgical method, chemical stripping, physical stripping or electrochemical stripping for recovering copper and possible noble metals from the electrode.

Assignees

• Aalto Univ Foundation Sr

Inventors

• Lundström Mari
• Yliniemi Kirsi

Classifications

• C02F2101/20

  Heavy metals or heavy metal compounds · CPC title

• C25C1/06

  or iron group metals, refractory metals or manganese · CPC title

• C02F2001/46152

  characterised by the shape or form · CPC title

• C25C1/20

  of noble metals · CPC title

• C25C1/12 Primary

  of copper · CPC title