Hydrometallurgical electrowinning of lead from spent lead-acid batteries

Patent metadata

Field	Value
Publication number	US-10062933-B2
Application number	US-201615145256-A
Country	US
Kind code	B2
Filing date	May 3, 2016
Priority date	Dec 14, 2015
Publication date	Aug 28, 2018
Grant date	Aug 28, 2018

Abstract

The present disclosure relates generally to recycling lead-acid batteries, and more specifically, relates to purifying and recycling the lead content from lead-acid batteries. A method includes reacting a lead-bearing material with a first carboxylate source to generate a first lead carboxylate. The method includes reacting the first lead carboxylate with a second carboxylate source to generate a second lead carboxylate. The method further includes applying an electrical bias to an aqueous solution of the second lead carboxylate to generate metallic lead.

First claim

The invention claimed is:

1. A method, comprising:
reacting a lead-bearing material with a first carboxylate source to generate a first lead carboxylate;
reacting the first lead carboxylate with a second carboxylate source to generate a second lead carboxylate; and
applying an electrical bias to an aqueous solution of the second lead carboxylate to generate metallic lead.

2. The method of claim 1 , wherein the first carboxylate source comprises an acetate and the second carboxylate source comprises a citrate.

3. The method of claim 1 , comprising processing spent lead-acid batteries to generate the lead-bearing material, wherein the lead bearing material comprises grids, posts, interconnects, plates, spines, battery paste, lead oxides, or lead sulfates, or combinations thereof, extracted from the processed spent lead-acid batteries.

4. The method of claim 1 , wherein the first lead carboxylate is generated in a leaching mixture, and wherein the generated first lead carboxylate is dissolved in a liquid component of the leaching mixture.

5. The method of claim 1 , wherein the second lead carboxylate is generated in a carboxylate exchange mixture that includes the second carboxylate source, and wherein the second lead carboxylate precipitates from the carboxylate exchange mixture.

6. The method of claim 5 , comprising isolating the second lead carboxylate from the carboxylate exchange mixture, and dissolving and/or suspending the second lead carboxylate in water to generate the aqueous solution of the second lead carboxylate.

7. The method of claim 1 , wherein applying the electrical bias comprises applying a voltage of approximately 3.5 volts (V) and a current between approximately 10 milliamps per square centimeter (mA/cm 2 ) and approximately 100 mA/cm 2 to the cathode and anode to generate the metallic lead.

8. The method of claim 1 , comprising processing the metallic lead to manufacture a component of a lead-acid battery, and then manufacturing the lead-acid battery using the component.

9. A method, comprising:
processing spent lead-acid batteries to generate a lead-bearing material;
leaching the lead-bearing material using a first carboxylate source to generate a leaching mixture, wherein the leaching mixture includes a dissolved first lead carboxylate;
separating unleached solids from a liquid component of the leaching mixture;
mixing the liquid component of the leaching mixture with a second carboxylate source to generate a carboxylate exchange mixture, wherein the carboxylate exchange mixture includes solid particles of a second lead carboxylate;
separating the solid particles of the second lead carboxylate from a liquid component of the carboxylate exchange mixture;
generating an aqueous solution from the solid particles of the second lead carboxylate; and
applying an electrical bias to the aqueous solution of the second lead carboxylate to generate metallic lead.

10. The method of claim 9 , wherein the leaching mixture comprises hydroxide and a peroxide to facilitate the leaching of the lead-bearing material.

11. The method of claim 9 , comprising treating the liquid component of the carboxylate exchange mixture to regenerate a portion of the first carboxylate source, and then recycling this portion of the first carboxylate source back to generate the leaching mixture.

12. The method of claim 9 , comprising treating the liquid component of the aqueous solution after applying the electrical bias to regenerate a portion of the second carboxylate source, and then recycling this portion of the second carboxylate source back to generate the carboxylate exchange mixture.

13. The method of claim 9 , wherein the aqueous solution of the second lead carboxylate is a supersaturated solution.

14. The method of claim 9 , wherein the electrical bias is applied using a lead anode, wherein the metallic lead is generated at the surface of the lead anode.

15. The method of claim 9 , comprising alloying one or more metals with the metallic lead to generate a lead alloy, and then using the lead alloy to manufacture a component of a lead-acid battery.

16. The method of claim 9 , comprising oxidizing the metallic lead to generate lead oxide, and then using the lead oxide to manufacture an active material of a lead-acid battery.

17. The method of claim 9 , wherein the aqueous solution is supersaturated in the second lead carboxylate such that a portion of the second lead carboxylate in the aqueous solution remains undissolved.

18. The method of claim 9 , comprising adding hydroxide to the aqueous solution of the second lead carboxylate increase a pH of the aqueous solution to 8 or more before applying the electrical bias, wherein the increased pH increases the solubility of the second lead carboxylate in the aqueous solution.

19. The method of claim 1 , wherein reacting the lead-bearing material with the first carboxylate source comprises leaching the lead-bearing material using the first carboxylate source to generate a leaching mixture having the first lead carboxylate dissolved therein.

20. The method of claim 19 , comprising separating unleached solids from a liquid component of the leaching mixture, wherein the first lead carboxylate remains dissolved in the liquid component of the leaching mixture after separating.

21. The method of claim 20 , wherein reacting the first lead carboxylate with the second carboxylate source comprises mixing the separated liquid component of the leaching mixture having the first lead carboxylate dissolved therein with the second carboxylate source to generate a carboxylate exchange mixture, wherein the carboxylate exchange mixture includes solid particles of the second lead carboxylate.

22. The method of claim 21 , comprising:
separating the solid particles of the second lead carboxylate from a liquid component of the carboxylate exchange mixture; and
generating the aqueous solution of the second lead carboxylate from the separated solid particles of the second lead carboxylate.

Assignees

• Johnson Controls Tech Co

Inventors

• Spence Matthew A

Classifications

• C25C1/18 Primary

  of lead · CPC title

• H01M4/56

  of lead · CPC title

• C25C7/007

  of cells comprising at least a movable electrode (C25C7/002, C25C7/02 - C25C7/06 take precedence) · CPC title

• H01M10/54 Primary

  Reclaiming serviceable parts of waste accumulators · CPC title

• C22B13/045

  Recovery from waste materials · CPC title