Methods for purifying and recycling lead from spent lead-acid batteries

Patent metadata

Field	Value
Publication number	US-9751067-B2
Application number	US-201414498748-A
Country	US
Kind code	B2
Filing date	Sep 26, 2014
Priority date	Jun 20, 2014
Publication date	Sep 5, 2017
Grant date	Sep 5, 2017

Abstract

The present disclosure relates to methods by which lead from spent lead-acid batteries may be extracted, purified, and used in the construction of new lead-acid batteries. A method includes: (A) forming a mixture including a carboxylate source and a lead-bearing material; (B) generating a first lead salt precipitate in the mixture as the carboxylate source reacts with the lead-bearing material; (C) increasing the pH of the mixture to dissolve the first lead salt precipitate; (D) isolating a liquid component of the mixture from one or more insoluble components of the mixture; (E) decreasing the pH of the liquid component of the mixture to generate a second lead salt precipitate; and (F) isolating the second lead salt precipitate from the liquid component of the mixture. Thereafter, the isolated lead salt precipitate may be converted to leady oxide for use in the manufacture of new lead-acid batteries.

First claim

The invention claimed is:

1. A method, comprising performing the following steps in the recited order:
(A) forming a mixture comprising a carboxylate source and a lead-bearing material disposed in a liquid component;
(B) generating a lead carboxylate precipitate in the mixture as the carboxylate source reacts with the lead-bearing material;
(C) increasing the pH of the liquid component of the mixture to dissolve the lead carboxylate precipitate into the liquid component of the mixture;
(D) isolating the liquid component of the mixture from one or more insoluble components of the lead-bearing material in the mixture;
(E) regenerating the lead carboxylate precipitate either by adding an antisolvent to the liquid component of the mixture or by adding an acid to decrease the pH of the liquid component of the mixture; and
(F) isolating the regenerated lead carboxylate precipitate from the liquid component of the mixture.

2. The method of claim 1 , comprising treating the isolated regenerated lead carboxylate precipitate using calcination or a base treatment to yield leady oxide.

3. The method of claim 2 , wherein the leady oxide comprises between approximately 0% and approximately 35% free lead.

4. The method of claim 2 , wherein the leady oxide comprises leady oxide particles having a D 50 between approximately 0.2 μm and approximately 20 μm.

5. The method of claim 2 , wherein the leady oxide has a Brunauer-Emmett-Teller (BET) surface area greater than approximately 2.5 square meters per gram (m 2 /g).

6. The method of claim 2 , wherein the leady oxide has an acid absorption greater than approximately 250 milligrams H 2 SO 4 per gram.

7. The method of claim 2 , wherein the leady oxide comprises less than approximately 20% beta phase lead oxide.

8. The method of claim 2 , comprising:
forming an active material for use in a lead-acid battery, wherein the active material comprises the leady oxide; and
constructing a battery comprising the active material.

9. The method of claim 1 , comprising reacting one or more impurities from the lead-bearing material present in the liquid component of the mixture isolated in step (D) with at least one reducing agent to evolve one or more impurity gases that are released from the liquid component before step (E) to remove the one or more impurities from the liquid component, wherein the one or more impurities comprise an element or compound of Group 14, an element or compound of Group 15, an element or compound of Group 16, an element or compound of Group 17, or a combination thereof.

10. The method of claim 1 , wherein the regenerated lead carboxylate precipitate includes less than approximately 0.1% sulfates.

11. The method of claim 1 , comprising grinding one or more spent lead-acid batteries to generate the lead-bearing material.

12. The method of claim 1 , wherein the carboxylate source comprises a Group 1 or Group 2 citrate, citric acid, ammonium citrate, a Group 1 or Group 2 acetate, ammonium acetate, acetic acid, or a combination thereof.

13. The method of claim 1 , wherein increasing the pH of the mixture comprises raising the pH of the mixture above 7.

14. The method of claim 1 , wherein increasing the pH of the mixture comprises raising the pH of the mixture to a value between approximately 8 and 14.

15. The method of claim 1 , wherein increasing the pH of the mixture comprises adding a hydroxide to the mixture, wherein the hydroxide comprises a Group 1 or Group 2 hydroxide, ammonium hydroxide, or a combination thereof.

16. The method of claim 1 , wherein the one or more insoluble components of the lead-bearing material in the mixture comprise barium sulfate, carbon black, glass, polymer, or combinations thereof.

17. The method of claim 1 , wherein the one or more insoluble components of the lead-bearing material in the mixture include metallic parts comprising lead, antimony, arsenic, selenium, calcium, tin, silver, cadmium or a combination thereof.

18. The method of claim 9 , wherein the one or more impurities comprise tellurium, antimony, tin, selenium, arsenic, germanium, silicon, phosphorus, sulfur, or a combination thereof.

19. The method of claim 9 , wherein the at least one reducing agent comprises sodium tetraborohydride.

20. The method of claim 9 , wherein the at least one reducing agent comprises sodium hydride.

21. The method of claim 9 , wherein the at least one reducing agent comprises hydrogen gas.

22. The method of claim 9 , wherein the at least one reducing agent comprises syngas.

23. The method of claim 9 , wherein the one or more impurity gases comprise hydrogen telluride, antimony trihydride (stibine), tin tetrahydride (stannane), hydrogen selenide, arsenic trihydride (arsine), germanium tetrahydride (germane), silicon hydrides (silane), phosphine, hydrogen disulfide, or a combination thereof.

24. The method of claim 1 , wherein the lead carboxylate precipitate is regenerated by adding the antisolvent to the isolated liquid component of the mixture in step (E), and wherein the antisolvent comprises: methanol, ethanol, propanol, ethylene glycol, or combinations thereof.

25. The method of claim 1 , comprising: (G) recovering the antisolvent from the liquid component via distillation.

26. The method of claim 25 , comprising: (H) recycling the antisolvent into step (E) to regenerate the lead carboxylate precipitate.

27. The method of claim 25 , comprising: (H) recycling the liquid component into step (A) to facilitate leaching of lead solids.

28. The method of claim 25 , comprising: (H) recycling the liquid component into step (C) to increase the pH of the mixture.

29. The method of claim 1 , wherein the carboxylate source is a Group 1 or Group 2 citrate, citric acid, ammonium citrate, or a combination thereof, and wherein the lead carboxylate precipitate is lead citrate.

Assignees

• Johnson Controls Tech Co

Inventors

• Spence Matthew A

Classifications

• Y02W30/84

  Recycling of batteries or fuel cells · CPC title

• H01M6/52

  Reclaiming serviceable parts of waste cells or batteries {, e.g. recycling} · CPC title

• C22B3/02

  Apparatus therefor · CPC title

• B01J8/008 Primary

  Details of the reactor or of the particulate material; Processes to increase or to retard the rate of reaction (B01J8/0285, B01J8/067, B01J8/087, B01J8/1836 take precedence) · CPC title

• C22B7/006

  Wet processes · CPC title