Processing hard rock lithium minerals or other materials to produce lithium materials and byproducts converted from a sodium sulfate intermediate product
US-2024425381-A1 · Dec 26, 2024 · US
US2024047776A1 · US · A1
| Field | Value |
|---|---|
| Publication number | US-2024047776-A1 |
| Application number | US-202118265708-A |
| Country | US |
| Kind code | A1 |
| Filing date | Oct 26, 2021 |
| Priority date | Dec 14, 2020 |
| Publication date | Feb 8, 2024 |
| Grant date | — |
A practical reading order for non-experts. Skip the full description unless you need deep technical detail.
What the patent document calls the invention.
A short plain-language summary of the technical disclosure.
Who owns or filed the patent and who is credited as inventor.
Filing, priority, publication, and grant dates set the timeline.
The legal scope of protection — read this for what is actually claimed.
Technology tags used to group this patent with similar filings.
Prior art links and similar publications in this corpus.
Official abstract text for this publication.
Provided is a method for processing lithium ion battery waste, which can effectively precipitate aluminum ions and iron ions in the solution by neutralization and relatively easily separate the precipitate. The method for processing lithium ion battery waste includes: a leaching step of leaching battery powder in an acid, the battery powder containing at least aluminum and iron and being obtained from lithium ion battery waste, and removing a leached residue by solid-liquid separation to obtain a leached solution containing at least aluminum ions and iron ions; and a neutralization step of adding phosphoric acid and/or a phosphate salt and an oxidizing agent to the leached solution, increasing a pH of the leached solution to a range of 2.0 to 3.5, precipitating the aluminum ions and the iron ions in the leached solution as aluminum phosphate and iron phosphate, respectively, and removing a neutralized residue by solid-liquid separation to obtain a neutralized solution.
Opening claim text (preview).
1 . A method for processing lithium ion battery waste, the method comprising: a leaching step of leaching battery powder in an acid, the battery powder containing at least aluminum and iron and being obtained from lithium ion battery waste, and removing a leached residue by solid-liquid separation to obtain a leached solution containing at least aluminum ions and iron ions; and a neutralization step of adding phosphoric acid and/or a phosphate salt and an oxidizing agent to the leached solution, increasing a pH of the leached solution to a range of 2.0 to 3.5, precipitating the aluminum ions and the iron ions in the leached solution as aluminum phosphate and iron phosphate, respectively, and removing a neutralized residue by solid-liquid separation to obtain a neutralized solution. 2 . The method for processing lithium ion battery waste according to claim 1 , wherein, in the neutralization step, an amount of the phosphoric acid and/or the phosphate salt added to the leached solution is such that an amount of phosphorus in the phosphoric acid and/or the phosphate salt is 0.6-fold molar equivalent to 1.2-fold molar equivalent base on the total amount of the aluminum ions and the iron ions in the leached solution. 3 . The method for processing lithium ion battery waste according to claim 1 , wherein: the leached solution further comprises manganese ions derived from the battery powder, the neutralization step comprises precipitating the aluminum phosphate and the iron phosphate while suppressing precipitation of the manganese ions, at a pH in said range. 4 . The method for processing lithium ion battery waste according to claim 3 , wherein the leached solution further comprises one or more metal ions of cobalt ions and nickel ions derived from the battery powder, and wherein the method further comprises a metal extraction step of using a solvent comprising a carboxylic acid-based extracting agent for the neutralized solution, adjusting an equilibrium pH to 6.5 to 7.5 and extracting manganese ions and the one or more metal ions in the neutralized solution into the solvent, and then back-extracting the manganese ions and the one or more metal ions from the solvent to obtain a mixed metal solution. 5 . The method for processing lithium ion battery waste according to claim 4 , wherein, in the metal extraction step, during the extraction, phosphorus contained in neutralized solution is left in the neutralized solution and separated from the manganese ions and the one or more metal ions extracted into the solvent. 6 . The method for processing lithium ion battery waste according to claim 4 , wherein, in the metal extraction step, the carboxylic acid-based extracting agent contained in the solvent comprises neodecanoic acid. 7 . The method for processing lithium ion battery waste according to claim 4 , further comprising a precipitation step of precipitating a mixed metal salt comprising a metal salt of manganese and a metal salt of at least one of cobalt and nickel from the mixed metal solution. 8 . The method for processing lithium ion battery waste according to claim 7 , wherein the precipitation step comprises neutralizing the mixed metal solution with sodium hydroxide, and precipitating a mixed metal comprising a hydroxide of manganese and a hydroxide of at least one of cobalt and nickel. 9 . The method for processing lithium ion battery waste according to claim 7 , wherein the mixed metal salt is used for production of lithium ion batteries.
Reclaiming serviceable parts of waste accumulators · CPC title
by acid leaching · CPC title
by chemical processes (treatment or purification of solutions by liquid-liquid extraction C22B3/26, by ion-exchange extraction C22B3/42) · CPC title
Carboxylic acids · CPC title
Obtaining lithium · CPC title
Related publications grouped by family.
Answers are generated from the same data shown on this page.