Electrochemical recycling of lead-based materials

Patent metadata

Field	Value
Publication number	US-10774433-B2
Application number	US-201615735453-A
Country	US
Kind code	B2
Filing date	Jun 9, 2016
Priority date	Jun 12, 2015
Publication date	Sep 15, 2020
Grant date	Sep 15, 2020

Abstract

The present application relates to the electrochemical extraction of lead (Pb) from a lead-containing material using a deep eutectic solvent. This is of particular use in the recycling of the lead-based materials that result from energy generation processes.

First claim

The invention claimed is:

1. A method for extracting lead from a lead-based material, the method comprising:
dissolving the lead-based material in a deep eutectic solvent to form an electrolyte;
providing a working lead electrode in electrical contact with the electrolyte;
providing a counter electrode in electrical contact with the electrolyte; and
generating a potential through the electrolyte, thereby reducing a lead species of the lead-based material in the electrolyte at the working lead electrode, so as to deposit the reduced lead species as deposited, reduced lead metal onto the working lead electrode;
wherein the lead-based material is from a lead acid battery, a lead perovskite photovoltaic and/or lead thermoelectric and comprises PbO 2 , PbSO 4 , CH 3 NH 3 PbHaI 3 , HC(NH 2 ) 2 PbHaI 3 , CH 3 NH 3 PbI 3-X Cl X or PbTe, or a mixture thereof, wherein HaI is I, Cl, or Br, and X is a value between 0 and 3; and
wherein the deposited, reduced lead metal and the working lead electrode is suitable for direct recycling or reusing as one piece, without need for further processing to separate the lead from the electrode.

2. The method of claim 1 , wherein the deep eutectic solvent comprises a hydrogen bond donor and a quaternary ammonium salt.

3. The method of claim 1 , wherein the potential applied is equal to, or more negative than, the Pb(II) to Pb reduction potential.

4. The method of claim 1 , wherein the deep eutectic solvent is maintained at a temperature above about 20° C.

5. The method of claim 1 , wherein the method further comprises:
dissolving the lead-based material in a deep eutectic solvent to form the electrolyte;
providing a working electrode in electrical contact with the electrolyte;
providing a counter electrode in electrical contact with the electrolyte;
generating a potential through the electrolyte, thereby reducing the lead species of the lead-based material in the electrolyte at the working electrode so as to deposit the reduced lead species on the working electrode as lead metal; and
collecting the deposited lead metal.

6. The method of claim 1 , wherein the counter electrode is an IrO 2 -coated Ti electrode.

7. The method of claim 1 , wherein the method further comprises providing a reference electrode in electrical contact with the electrolyte.

8. The method of claim 1 , wherein the lead-based material is dissolved in the deep eutectic solvent at a temperature above about 20° C. to form the electrolyte.

9. An electrochemical cell capable of reducing a lead species in a lead-based material so that the reduced lead species is deposited at a working electrode, the cell comprising:
an electrolyte comprising a solution of the lead-based material dissolved in a deep eutectic solvent;
a working lead electrode in electrical contact with the electrolyte; and
a counter electrode in electrical contact with the electrolyte;
wherein the lead-based material is from a lead acid battery, a lead perovskite photovoltaic and/or lead thermoelectric and comprises PbO 2 , PbSO 4 , CH 3 NH 3 PbHaI 3 , HC(NH 2 ) 2 PbHaI 3 , CH 3 NH 3 PbI 3-X Cl X or PbTe, or a mixture thereof, wherein HaI is I, Cl, or Br, and X is a value between 0 and 3;
wherein the reduced lead species is deposited on the working lead electrode; and
wherein the deposited reduced lead metal adhered to the working lead electrode is suitable for direct recycling or reusing as one piece, without need for further processing to separate the lead from the electrode.

10. The electrochemical cell of claim 9 , wherein the counter electrode is an IrO 2 -coated Ti electrode.

11. The electrochemical cell of claim 9 comprising a reference electrode in electrical contact with the electrolyte.

12. The electrochemical cell of claim 9 , wherein the deep eutectic solvent comprises a hydrogen bond donor and a quaternary ammonium salt.

13. The electrochemical cell of claim 9 , wherein the electrolyte is maintained a temperature above about 20° C.

14. The electrochemical cell of claim 9 , wherein the lead-based material is dissolved in the deep eutectic solvent at a temperature above about 20° C. to form the electrolyte.

15. A method for extracting lead from a lead-based material, the method comprising:
dissolving the lead-based material from a lead acid battery, a lead perovskite photovoltaic and/or lead thermoelectric in a deep eutectic solvent to form an electrolyte;
providing a working lead electrode in electrical contact with the electrolyte;
providing a counter electrode in electrical contact with the electrolyte; and
generating a potential through the electrolyte, thereby reducing a lead species of the lead-based material in the electrolyte at the working electrode so as to deposit the reduced lead species as lead metal; and
wherein the deposited reduced lead metal and the working electrode is suitable for direct recycling or reusing as one piece, without need for further processing to separate the lead from the electrode.

16. The method of claim 2 , wherein the hydrogen bond donor is ethylene glycol or urea and the quaternary ammonium salt is choline chloride, and wherein the ethylene glycol:choline chloride, or urea:choline chloride are present in a molar ratio of 2:1.

17. The method of claim 1 , wherein the reference electrode is an Ag-wire quasi-reference electrode.

18. The electrochemical cell of claim 11 , wherein the reference electrode is an Ag-wire quasi-reference electrode.

19. The electrochemical cell of claim 12 , wherein the hydrogen bond donor is ethylene glycol or urea and the quaternary ammonium salt is choline chloride, and wherein the ethylene glycol:choline chloride, or urea:choline chloride are present in a molar ratio of 2:1.

Assignees

• Imperial Innovations Ltd
• Imperial White City Incubator Ltd

Inventors

• Poll Christopher Gavin
• Riley David Jason
• Payne David James

Classifications

• H10K85/50

  Organic perovskites; Hybrid organic-inorganic perovskites [HOIP], e.g. CH3NH3PbI3 · CPC title

• C25C1/18 Primary

  of lead · CPC title

• H01M10/54

  Reclaiming serviceable parts of waste accumulators · CPC title

• C25C7/00

  Constructional parts, or assemblies thereof, of cells; Servicing or operating of cells (for the production of aluminium C25C3/06 - C25C3/22) · CPC title

• C22B13/045

  Recovery from waste materials · CPC title