Positive electrode active material and preparation method thereof, positive electrode plate, secondary battery, battery module, battery pack, and electric apparatus
US-2024429384-A1 · Dec 26, 2024 · US
US2023365410A1 · US · A1
| Field | Value |
|---|---|
| Publication number | US-2023365410-A1 |
| Application number | US-202217743071-A |
| Country | US |
| Kind code | A1 |
| Filing date | May 12, 2022 |
| Priority date | May 12, 2022 |
| Publication date | Nov 16, 2023 |
| Grant date | — |
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A process of preparing a lithium metal phosphate includes contacting a water-soluble metal precursor, a water-insoluble metal precursor, and a phosphate precursor in an acidic aqueous medium; to form a reaction mixture; precipitating from the reaction mixture a metal phosphate; collecting the metal phosphate; combining the metal phosphate with a lithium precursor; and calcining the combined metal phosphate and lithium precursor at elevated temperature to form a lithium metal phosphate; wherein a mol ratio of water-soluble metal precursor to water-insoluble metal precursor is from 0.5:99.5 to 99.5:0.5.
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What is claimed is: 1 . A process of preparing a lithium metal phosphate, the process comprising: contacting a water-soluble metal precursor, a water-insoluble metal precursor, and a phosphate precursor in an acidic aqueous medium to form a reaction mixture; precipitating a metal phosphate from the reaction mixture; collecting the metal phosphate; combining the metal phosphate with a lithium precursor; and calcining the combined metal phosphate and lithium precursor at elevated temperature to form a lithium metal phosphate; wherein a mol ratio of water-soluble metal precursor to water-insoluble metal precursor is from 0.5:99.5 to 99.5:0.5. 2 . The process of claim 1 , wherein the water-insoluble metal precursor comprises iron metal, iron oxide, manganese metal, a manganese oxide, cobalt metal, a cobalt oxide, nickel metal, a nickel oxide, or a mixture of any two or more thereof. 3 . The process of claim 1 , wherein the water-soluble metal precursor comprises a metal halide, a metal nitrate, a metal sulfate, or a mixture of any two or more thereof. 4 . The process of claim 3 , wherein the water-soluble metal precursor comprises FeCl 2 , FeCl 3 , FeCl 2 ·4H 2 O, FeCl 3 ·6H 2 O, Fe(NO 3 ) 3 , Fe(NO 3 ) 3 ·6H 2 O, Fe(NO 3 ) 3 ·9H 2 O, FeSO 4 , FeSO 4 ·6H 2 O, FeSO 4 ·7H 2 O, MnCl 2 , MnCl 2 ·H 2 O, MnCl 2 ·4H 2 O, MnCl 2 ·xH 2 O, Mn(NO 3 ) 2 , Mn(NO 3 ) 2 ·xH 2 O, Mn(NO 3 ) 2 ·4H 2 O, MnSO 4 , MnSO 4 ·xH 2 O, MnSO 4 ·4H 2 O, NiCl 2 , NiCl 2 ·6H 2 O, Ni(NO 3 ) 2 , Ni(NO 3 ) 2 ·6H 2 O, NiSO 4 , NiSO 4 ·6H 2 O, NiSO 4 ·7H 2 O, CoCl 2 , CoCl 2 ·xH 2 O, CoCl 2 ·6H 2 O, Co(NO 3 ) 2 , Co(NO 3 ) 2 ·6H 2 O, CoSO 4 , CoSO 4 ·xH 2 O, CoSO 4 ·7H 2 O, or a mixture of any two or more thereof. 5 . The process of claim 1 , wherein the phosphate precursor is an acid or forms an acid to acidify the acid aqueous medium. 6 . The process of claim 1 , wherein the phosphate precursor comprises H 3 PO 4 , P 2 O 5 , pyrophosphoric acid, polyphosphoric acid, a phosphate salt, and a ammonium phosphates, or a mixture of any two or more thereof. 7 . The process of claim 1 , wherein a mol ratio of water-soluble metal precursor to water-insoluble metal precursor is from 20:80 to 80:20. 8 . The process of claim 1 , wherein the water-insoluble metal source comprises Fe 2 O 3 , Fe 3 O 4 , FeO, FeC 2 O 4 , FeC 2 O 4 ·2H 2 O, or a mixture of any two or more thereof. 9 . The process of claim 1 , wherein the lithium precursor comprises LiOH, LiOH·H 2 O, LiHCO 3 , or a mixture of any two or more thereof. 10 . The process of claim 1 , wherein the reaction mixture further comprises a carbon coating precursor agent. 11 . The process of claim 10 , wherein the lithium metal phosphate is characterized by a mixed morphology exhibiting a greater packing density compared to lithium metal phosphate materials obtained processes in which a water-soluble metal precursor is not combined with a water-insoluble metal precursor, and wherein the packing density being defined as mass weight of materials per given electrode volume. 12 . The process of claim 10 , wherein the carbon coating precursor agent comprises oxalic acid, citric acid, sugar, glucose, ascorbic acid, or a mixture of any two or more thereof. 13 . The process of claim 1 , wherein the combining the metal phosphate with the lithium precursor further comprises adding a carbon source prior to calcining. 14 . The process of claim 13 , wherein the carbon source comprises oxalic acid, citric acid, sugar, glucose, ascorbic acid, or a mixture of any two or more thereof. 15 . The process of claim 1 , wherein the acid aqueous medium further comprises one or more polar solvents other than water. 16 . The process of claim 1 , wherein the collecting comprising collecting the metal phosphate via filtration and washing the metal phosphate with an aqueous solution. 17 . The process of claim 1 further comprising drying the metal phosphate prior to calcining. 18 . The process of claim 15 , wherein the drying comprises spray drying to yield particles of the metal phosphate exhibiting a volume-average diameter of about 1 micrometer to about 20 micrometers. 19 . The process of claim 1 , wherein the precipitating is conducted at a temperature of about 0° C. to about 100° C. 20 . The process of claim 1 further comprising recrystallizing the metal phosphate.
Oxygenated metallic salts or polyanionic structures, e.g. borates, phosphates, silicates, olivines · CPC title
containing plural metal, or metal and ammonium · CPC title
from phosphates · CPC title
Rocking-chair batteries, i.e. batteries with lithium insertion or intercalation in both electrodes; Lithium-ion batteries · CPC title
Electric properties · CPC title
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