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-2020235443-A1
Application number	US-201916557699-A
Country	US
Kind code	A1
Filing date	Aug 30, 2019
Priority date	Jun 20, 2014
Publication date	Jul 23, 2020
Grant date	—

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-beating 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

1 - 23 . (canceled)

24 . 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; a calciner coupled to the phase separation device and configured to receive the lead carboxylate precipitate isolated by the phase separation device and treat the lead carboxylate precipitate to yield leady oxide; 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.

25 . The system of claim 24 , wherein the closed-loop liquid recycling system comprises a purification device that removes at least one impurity from the received liquid component before recycling.

26 . The system of claim 25 , 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.

27 . The system of claim 24 , wherein the carboxylate source comprises citric acid, a salt of citric acid, ammonium citrate, or a combination thereof.

28 . The system of claim 24 , wherein the recycled liquid component is a solution at least 10% saturated in dissolved lead carboxylate.

29 . The system of claim 24 , 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.

30 . The system of claim 24 , 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.

31 . The system of claim 24 , wherein the calciner comprises a heat source configured to heat the lead carboxylate precipitate to a temperature less than or equal to 450° C.

32 . The system of claim 36 , wherein a gas source is provided and heating occurs in the presence of a gas stream delivered by the gas source.

33 . The system of claim 24 , whererin the system includes process controls selected from the group consisting of temperature of calcination, time, droplet size, lead salt particle size, amount of residual water in the lead salt, rate of heating of the lead salt to the calcination temperature, and oxygen temperature in a gas stream.

34 . 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; a purification device coupled to the phase separation device and configured to receive the liquid component, wherein the purification device removes at least one impurity from the received liquid component; 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.

35 . The system of claim 34 , wherein the purification device comprises a reactor for chemical purification.

36 . The system of claim 35 , wherein the chemical purification comprises introducing calcium hydroxide to the liquid component to form insoluble calcium sulfate.

37 . The system of claim 34 , wherein the purification device comprises a physical purification device.

38 . The system of claim 37 , wherein the physical purification device comprises a reverse osmosis device.

39 . The system of claim 37 , wherein the physical purification device comprises a nanofiltration device.

40 . The system of claim 34 , wherein the purification device comprises an ion exchange resin.

41 . The system of claim 34 , 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.

42 . The system of claim 34 , wherein the at least one impurity comprises dissolved sulfates.

43 . The system of claim 34 , wherein the at least one impurity comprises one or more elements other than lead.

44 . The system of claim 34 , wherein the phase separation device comprises a belt dryer, a filter press, a clarifier, or a cyclone separator.

Assignees

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

Inventors

• Meissner Jr Eberhard
• Bauer Jurgen
• Spence Matthew A

Classifications

• Y02P10/20

  Recycling · CPC title

• H01M10/54 Primary

  Reclaiming serviceable parts of waste accumulators · CPC title

• C22B3/04

  by leaching (C22B3/18 takes precedence) · 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

• B01J19/2465

  externally, i.e. the mixture leaving the vessel and subsequently re-entering it · CPC title