Systems and methods for closed-loop recycling of a liquid component of a leaching mixture when recycling lead from spent lead-acid batteries
View Patent ↗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 salt precipitate. The system also includes a phase separation device coupled to the reactor, wherein the phase separation device isolates the lead salt 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.
1. A method, comprising:
forming a leaching mixture comprising a lead-bearing material, a carboxylate source, and a recycled liquid component, wherein the leaching mixture generates a lead carboxylate precipitate as the carboxylate source reacts with the lead-bearing material in the leaching mixture, wherein the carboxylate source comprises citric acid, a salt of citric acid, or a combination thereof;
isolating a liquid component from the lead carboxylate precipitate of the leaching mixture;
purifying at least a portion of the isolated liquid component, wherein purifying comprises removing at least a portion of one or more sulfates from the portion of the isolated liquid component; and
recycling the portion of the isolated liquid component back into the leaching mixture as the recycled liquid component after purification.
2. The method of claim 1 , wherein purifying comprises removing at least one dissolved metal other than lead from the portion of the isolated liquid component.
3. The method of claim 1 , wherein purifying comprises mixing calcium hydroxide with the portion of the isolated liquid component and subsequently removing calcium sulfate precipitate before recycling.
4. The method of claim 1 , wherein purifying comprises using an ion exchange resin to remove one or more sulfates from the portion of the isolated liquid component.
5. The method of claim 1 , wherein purifying comprises removing one or more impurities from the portion of the isolated liquid component without substantially removing dissolved lead carboxylate.
6. The method of claim 1 , wherein isolating the liquid component from the lead carboxylate precipitate comprises using a belt dryer, a filter press, a clarifier, or a cyclone separator to isolate the liquid component.
7. The method of claim 1 , comprising treating the lead carboxylate precipitate to yield leady oxide after isolating the liquid component from the lead carboxylate precipitate.
8. The method of claim 7 , wherein treating comprises oxidizing the lead carboxylate precipitate into leady oxide using a belt dryer, a spray calciner, a stirred pot reactor, a rotary kiln calciner, or a combination thereof.
9. The method of claim 7 , wherein treating comprises reacting the lead carboxylate precipitate with a hydroxide to yield the leady oxide.
10. The method of claim 1 , wherein the carboxylate source comprises acetic acid, a salt of acetic acid, or a combination thereof.
11. The method of claim 1 , wherein the leaching mixture comprises a peroxide.
12. The method of claim 1 , wherein purifying comprises using a nanofilter to remove one or more sulfates from the portion of the isolated liquid component.
13. The method of claim 2 , wherein the at least one metal comprises sodium, barium, calcium, antimony, arsenic, tin, or combinations thereof.