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
US2025354237A1 · US · A1
| Field | Value |
|---|---|
| Publication number | US-2025354237-A1 |
| Application number | US-202519204750-A |
| Country | US |
| Kind code | A1 |
| Filing date | May 12, 2025 |
| Priority date | May 14, 2024 |
| Publication date | Nov 20, 2025 |
| Grant date | — |
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Disclosed are methods of recovering lithium precursors, methods of preparing positive electrode active materials, and rechargeable lithium batteries. The method of recovering a lithium precursor comprises preparing a first solution that includes lithium ions and transition metal ions, preparing a second solution by mixing the first solution and a first basic reagent, preparing a third solution by extracting a transition metal from the second solution, preparing a fourth solution by mixing the third solution and a second basic reagent, and extracting the lithium precursor from the fourth solution. The first basic reagent is prepared using a waste solution produced in a washing process of a positive electrode active material.
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What is claimed is: 1 . A method of recovering a lithium precursor, the method comprising: preparing a first solution that includes lithium ions and transition metal ions; preparing a second solution by mixing the first solution and a first basic reagent; preparing a third solution by extracting a transition metal from the second solution; preparing a fourth solution by mixing the third solution and a second basic reagent; and extracting the lithium precursor from the fourth solution, wherein the first basic reagent is prepared using a waste solution produced in a washing process of a positive electrode active material. 2 . The method of claim 1 , wherein the second basic reagent is prepared using a waste solution produced in a washing process of a positive electrode active material. 3 . The method of claim 1 , wherein preparation of the first solution includes dissolving a discarded lithium transition metal composite oxide in an acidic solution, wherein the discarded lithium transition metal composite oxide originates from a powdered discarded rechargeable lithium battery or waste generated during a fabrication process of a rechargeable lithium battery, wherein the discarded lithium transition metal composite oxide includes a compound of Chemical Formula 1: with 0≤a≤1, 0≤b≤1, 0≤c≤1, 0≤d≤1, and a+b+c+d=1, and with each of M1, M2, M3, and M4 being selected from Ni, Co, Al, Cu, Mn, Ti, Mo, Zn, Zr, Si, Ge, V, Cr, B, Mg, Na, Sr, Ag, Nb, Ga, Ca, and Ba. 4 . The method of claim 1 , wherein preparation of the first basic reagent includes: washing a calcined positive electrode active material with a washing solution; removing a solid substance by recovering a waste solution generated after the washing; and adjusting the waste solution to a pH of about 8 to about 16. 5 . The method of claim 4 , wherein the positive electrode active material is expressed by Chemical Formula 2: with 0≤e≤1, 0≤f≤1, 0≤g≤1, 0≤h≤1, and e+f+g+h=1, and with each of M5, M6, M7, and M8 being selected from Ni, Co, Al, Cu, Mn, Ti, Mo, Zn, Zr, Si, Ge, V, Cr, B, Mg, Na, Sr, Ag, Nb, Ga, Ca, and Ba. 6 . The method of claim 4 , wherein removing the solid substance from the waste solution includes using a decanter (i.e., a centrifugal separator), a filter, or a filter press, wherein the filter or the filter press comprises a filter paper having a pore size of about 0.5 μm to about 5 μm. 7 . The method of claim 4 , wherein adjusting the pH of the waste solution includes one of: introducing alkali hydroxide to the waste solution; and evaporating the waste solution. 8 . The method of claim 1 , wherein a pH of the first basic reagent is about 12 to about 16. 9 . The method of claim 1 , wherein the first basic reagent includes one or both of lithium carbonate (Li 2 CO 3 ) and lithium hydroxide (LiOH). 10 . The method of claim 1 , wherein a mass of lithium ions in the first basic reagent is about 1,000 ppm to about 10,000 ppm relative to a total mass of the first basic reagent. 11 . The method of claim 1 , wherein a mass of impurity ions in the first basic reagent is about 20 ppm to about 14,000 ppm relative to a total mass of the first basic reagent. 12 . The method of claim 1 , wherein the washing process includes washing a positive electrode active material with the lithium precursor recovered by the method of claim 1 . 13 . The method of claim 1 , wherein preparation of the second solution includes mixing the first solution and the first basic reagent to cause the second solution to have a pH of about 3 to about 4. 14 . The method of claim 1 , wherein preparation of the fourth solution includes mixing the third solution and the second basic reagent while satisfying a condition that a mass of lithium in the fourth solution does not fall below about 3,000 ppm relative to a total mass of the fourth solution. 15 . The method of claim 1 , wherein a mass ratio of lithium ions in the recovered lithium precursor to a total mass of the recovered lithium precursor is equal to or greater than about 99%. 16 . The method of claim 1 , wherein the recovered lithium precursor includes lithium carbonate (Li 2 CO 3 ) or lithium hydroxide (LiOH). 17 . A method of preparing a positive electrode active material for a rechargeable lithium battery, the method comprising: mixing and calcining a transition metal precursor and a lithium precursor that is recovered by the method of claim 1 ; and washing the calcined mixture. 18 . The method of claim 17 , wherein the transition metal precursor is a compound of Chemical Formula 3: with 0≤i≤1, 0≤j≤1, 0≤k≤1, 0≤1≤1, and i+j+k+1=1, and with M9, M10, M11, and M12 being selected from Ni, Co, Al, Cu, Mn, Ti, Mo, Zn, Zr, Si, Ge, V, Cr, B, Mg, Na, Sr, Ag, Nb, Ga, Ca, and Ba. 19 . The method of claim 18 , wherein M9 of Chemical Formula 3 is Ni. 20 . A rechargeable lithium battery comprising the positive electrode active material prepared according to claim 17 .
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