Systems and methods for closed-loop recycling of a liquid component of a leaching mixture when recycling lead from spent lead-acid batteries

Patent metadata

Field	Value
Publication number	US-10403940-B2
Application number	US-201715398962-A
Country	US
Kind code	B2
Filing date	Jan 5, 2017
Priority date	Jun 20, 2014
Publication date	Sep 3, 2019
Grant date	Sep 3, 2019

Abstract

The present disclosure relates generally to systems and methods for recycling lead-acid batteries, and more specifically, relates to purifying and recycling the lead content from lead-acid batteries. A system includes a reactor that receives and mixes a lead-bearing material waste, a carboxylate source, and a recycled liquid component to form a leaching mixture yielding a lead carboxylate precipitate. The system also includes a phase separation device coupled to the reactor, wherein the phase separation device isolates the lead carboxylate precipitate from a liquid component of the leaching mixture. The system further includes a closed-loop liquid recycling system coupled to the phase separation device and to the reactor, wherein the closed-loop liquid recycling system receives the liquid component isolated by the phase separation device and recycles a substantial portion of the received liquid component back to the reactor as the recycled liquid component.

First claim

The invention claimed is:

1. A system, comprising:
a reactor that receives and mixes lead-bearing material, a carboxylate source, and a recycled liquid component to form a leaching mixture yielding a lead carboxylate precipitate;
a phase separation device coupled to the reactor, wherein the phase separation device isolates the lead carboxylate precipitate from a liquid component of the leaching mixture; and
a closed-loop liquid recycling system coupled to the phase separation device and to the reactor, wherein the closed-loop liquid recycling system receives the liquid component isolated by the phase separation device and recycles a substantial portion of the received liquid component back to the reactor as the recycled liquid component.

2. The system of claim 1 , wherein the closed-loop liquid recycling system comprises a purification device that removes at least one impurity from the received liquid component before recycling.

3. The system of claim 2 , wherein the at least one impurity comprises dissolved sulfates.

4. The system of claim 2 , wherein the at least one impurity comprises one or more elements other than lead.

5. The system of claim 4 , wherein the one or more elements comprise sodium, barium, calcium, antimony, arsenic, tin, or combinations thereof.

6. The system of claim 2 , wherein the purification device comprises:
another reactor that mixes calcium hydroxide with the received liquid component; and
another phase separation device that subsequently removes a resulting calcium sulfate precipitate from the received liquid component before recycling.

7. The system of claim 2 , wherein the purification device comprises a nanofilter or ion exchange resin.

8. The system of claim 2 , wherein a dissolved lead carboxylate content of the liquid component is substantially the same before and after the purification device removes the at least one impurity.

9. The system of claim 1 , wherein the carboxylate source comprises citric acid, a salt of citric acid, ammonium citrate, or a combination thereof.

10. The system of claim 1 , wherein the recycled liquid component is a solution at least 10% saturated in dissolved lead carboxylate.

11. The system of claim 1 , wherein the closed-loop liquid recycling system receives wash water along with the liquid component from the phase separation device and recycles the wash water along with the liquid component.

12. The system of claim 1 , wherein the phase separation device comprises a belt dryer, a filter press, a clarifier, or a cyclone separator.

13. The system of claim 1 , comprising a lead-acid battery processing device that is configured to receive at least one lead-acid battery and grind the at least one lead-acid battery into the lead-bearing material.

14. The system of claim 1 , comprising a lead carboxylate precipitate treatment device that is configured to receive the lead carboxylate precipitate isolated by the phase separation device and treat the lead carboxylate precipitate to form leady oxide.

15. The system of claim 14 , wherein the lead carboxylate precipitate treatment device comprises a belt dryer, a spray calciner, a stirred pot reactor, a rotary kiln calciner.

16. A system, comprising:
a leaching vessel containing a leaching mixture comprising: a lead-bearing material, a carboxylate source, a lead carboxylate precipitate, and a purified liquid component; and
a closed-loop liquid recycling system coupled to the leaching vessel, wherein the closed-loop liquid recycling system receives a liquid component of the leaching mixture, purifies the received liquid component to generate the purified liquid component, and provides the purified liquid component to the leaching vessel, wherein the purified liquid component has a lower sulfate content than the received liquid component.

17. The system of claim 16 , comprising a phase separation device coupled to the leaching vessel and the closed-loop liquid recycling system, wherein the phase separation device receives the leaching mixture, including the liquid component, from the leaching vessel, isolates the lead carboxylate precipitate from the liquid component of the leaching mixture, and provides the liquid component to the closed-loop liquid recycling system.

18. The system of claim 16 , wherein the purified liquid component includes substantially the same amount of the dissolved lead carboxylate as the received liquid component.

19. The system of claim 16 , wherein the carboxylate source comprises citric acid, a metal citrate salt, ammonium citrate, or a combination thereof.

20. A system, comprising:
a leaching vessel configured to receive and mix a lead-bearing material, a carboxylate source, and a recycled liquid component to form a leaching mixture that yields a lead carboxylate precipitate;
a phase separation device configured to be coupled to the leaching vessel, wherein the phase separation device is configured to isolate the lead carboxylate precipitate from a liquid component of the leaching mixture; and
a closed-loop liquid recycling system configured to be coupled to the phase separation device and to the reactor, wherein the closed-loop liquid recycling system is configured to receive the liquid component isolated by the phase separation device, purify the liquid component, and recycle the purified liquid component back to the leaching vessel as the recycled liquid component.

21. The system of claim 20 , wherein the carboxylate source comprises citric acid, a metal citrate salt, ammonium citrate, or a combination thereof.

22. The system of claim 20 , wherein the closed-loop recycling system comprises a nanofilter purification device configured to remove at least one impurity from the received liquid component to purify the liquid component.

23. The system of claim 20 , wherein the purified liquid component includes substantially the same amount of a dissolved lead carboxylate as the received liquid component.

Assignees

• Johnson Controls Autobatterie Gmbh & Co Kgaa
• Johnson Controls Tech Co
• Cps Tech Holdings Llc

Inventors

• Meissner Jr Eberhard
• Bauer Jürgen
• Spence Matthew A

Classifications

• H01M6/52

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

• B01J6/002

  using rotating drums · CPC title

• C22B7/006

  Wet processes · CPC title

• C22B7/009

  General processes for recovering metals or metallic compounds from spent catalysts (for recovering specific metals C22B11/00 - C22B61/00) · CPC title

• Y02W30/84

  Recycling of batteries or fuel cells · CPC title