Method for recovering lead oxide from waste lead paste
US-10135100-B2 · Nov 20, 2018 · US
US9670565B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9670565-B2 |
| Application number | US-201414586111-A |
| Country | US |
| Kind code | B2 |
| Filing date | Dec 30, 2014 |
| Priority date | Jun 20, 2014 |
| Publication date | Jun 6, 2017 |
| Grant date | Jun 6, 2017 |
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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 lead recovery system includes a first reactor configured to receive and mix a lead-bearing material and a first carboxylate source to yield a first mixture, wherein the first mixture includes a first lead carboxylate that is dissolved in a liquid component of the first mixture. The system includes a second reactor configured to receive and mix the liquid component of the first mixture and a second carboxylate source to yield a second mixture, wherein the second mixture includes solid particles of a second lead carboxylate. The system includes a third reactor configured to receive and mix the solid particles of the second lead carboxylate and a hydroxide solution to yield a third mixture, wherein the third mixture includes solid particles of lead oxide.
Opening claim text (preview).
The invention claimed is: 1. A method of producing lead oxide from a lead-bearing material, comprising: leaching the lead-bearing material with a first carboxylate source to generate a leaching mixture that 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 that includes solid particles of a second lead carboxylate and the first carboxylate source; separating the solid particles of the second lead carboxylate from a liquid component of the carboxylate exchange mixture; mixing the separated solid particles of the second lead carboxylate with a hydroxide solution to generate a hydroxylation mixture that includes solid particles of lead oxide; and separating the solid particles of lead oxide from a liquid component of the hydroxylation mixture. 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 , wherein the separated solid particles of lead oxide consist of tetragonal lead oxide. 4. The method of claim 1 , comprising: mixing the liquid component of the carboxylate exchange mixture with an acid to yield an acetate/sulfate mixture that includes a liquid component having the first carboxylate source and insoluble impurities; separating the insoluble impurities from the liquid component of the acetate/sulfate mixture; separating the first carboxylate source from the liquid component of the acetate/sulfate mixture; and recycling the separated first carboxylate source to generate the leaching mixture. 5. The method of claim 4 , wherein mixing the liquid component of the carboxylate exchange mixture with the acid comprises mixing the liquid component of the carboxylate exchange mixture with sulfuric acid recovered from a spent lead-acid battery. 6. The method of claim 1 , comprising: mixing the liquid component of the hydroxylation mixture with an antisolvent to yield a recovery mixture that includes solid particles of the second carboxylate source; separating the solid particles of the second carboxylate source from a liquid component of the recovery mixture; recycling the solid particles of the second carboxylate source to generate the carboxylate exchange mixture; separating the liquid component of the recovery mixture to separately recover the antisolvent and the hydroxide solution; recycling the recovered antisolvent to generate the recovery mixture; and recycling the recovered hydroxide solution to generate the hydroxylation mixture.
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