Process for making a coated electrode active material
US-2022320496-A1 · Oct 6, 2022 · US
US12577127B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-12577127-B2 |
| Application number | US-202118247275-A |
| Country | US |
| Kind code | B2 |
| Filing date | Sep 16, 2021 |
| Priority date | Oct 1, 2020 |
| Publication date | Mar 17, 2026 |
| Grant date | Mar 17, 2026 |
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Described herein is a process for manufacture of a cathode active material including the steps of (a) providing a particulate electrode active material according to general formula Li 1+x TM 1−x O 2 , where TM is Ni and, optionally, at least one element selected from the group consisting of Al, Mg, Ba, and transition metals other than Ni, and x is in a range of from −0.05 to 0.2, and where at least 50 mole-% of TM is Ni, (b) adding an aqueous medium that includes LiOH in dissolved form to the particulate electrode active material provided in step (a), (c) removing the liquid phase by a solid-liquid separation method, and (d) at least partially recycling the liquid phase from step (c) for use in a treatment step.
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The invention claimed is: 1 . A process for manufacture of a cathode active material comprising the steps of (a) providing a particulate electrode active material according to general formula Li 1+x TM 1-x O 2 , wherein TM is Ni and, optionally, at least one element selected from the group consisting of Al, Mg, Ba, and transition metals other than Ni, and x is in a range of from −0.02 to 0.2, and wherein at least 50 mole-% of TM is Ni, (b) adding an aqueous medium that comprises LiOH in dissolved form to the particulate electrode active material provided in step (a), (c) removing the liquid phase by a solid-liquid separation method, and (d) at least partially recycling the liquid phase from step (c) for use in a treatment step. 2 . The process according to claim 1 , wherein TM is a combination of metals according to general formula (I) (Ni a Co b Mn c ) 1-d M d (I) with a being in a range of from 0.6 to 0.99, b being zero or in a range of from 0.01 to 0.2, c being in a range of from zero to 0.2, and d being in a range of from zero to 0.1, M is at least one of Al, Mg, Nb, Ta, Ti, Mo, W and Zr, and a+b+c=1. 3 . The process according to claim 1 , wherein the solid-liquid separation method in step (c) is a filtration. 4 . The process according to claim 1 , wherein an electric conductivity of the aqueous medium added in step (b) is in a range of from 0.8 to 80 mS/cm, determined at ambient temperature. 5 . The process according to claim 1 , wherein a concentration of LiOH of the aqueous medium added in step (b) is in a range of from 20 to 3,500 ppm by weight. 6 . The process according to claim 1 further comprising a subsequent step (e): (e) treating the solid residue from step (c) thermally. 7 . The process according to claim 1 , wherein the aqueous medium added in step (b) is obtained by diluting the liquid phase removed in step (c) with water and re-using said diluted liquid phase for treatment of an untreated particulate electrode active material. 8 . The process according to claim 1 , wherein the aqueous medium added in step (b) is essentially free from compounds of Sb, Mg, Zn, Sn, and Te.
Positive electrodes · CPC title
of mixed oxides or hydroxides containing iron, cobalt or nickel for inserting or intercalating light metals, e.g. LiNiO2, LiCoO2 or LiCoOxFy · CPC title
of mixed oxides or hydroxides containing manganese for inserting or intercalating light metals, e.g. LiMn2O4 or LiMn2OxFy · CPC title
Electric properties · CPC title
one element only · CPC title
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