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
US2016036043A1 · US · A1
| Field | Value |
|---|---|
| Publication number | US-2016036043-A1 |
| Application number | US-201414449987-A |
| Country | US |
| Kind code | A1 |
| Filing date | Aug 1, 2014 |
| Priority date | Aug 1, 2014 |
| Publication date | Feb 4, 2016 |
| Grant date | — |
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The disclosed embodiments relate to the manufacture of a precursor co-precipitate material for a cathode active material composition. During manufacture of the precursor co-precipitate material, an aqueous solution containing at least one of a manganese sulfate and a cobalt sulfate is formed. Next, a NH 4 OH solution is added to the aqueous solution to form a particulate solution comprising irregular secondary particles of the precursor co-precipitate material. A constant pH in the range of 10-12 is also maintained in the particulate solution by adding a basic solution to the particulate solution.
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What is claimed is: 1 . A method for manufacturing a precursor co-precipitate material for a cathode active material composition, comprising: forming an aqueous solution comprising at least one of a manganese sulfate and a cobalt sulfate; adding a NH 4 OH solution to the aqueous solution to form a particulate solution comprising irregular secondary particles of the precursor co-precipitate material; and maintaining a constant pH in the range of 10-12 in the particulate solution by adding a basic solution to the particulate solution. 2 . The method of claim 1 , further comprising: agitating the particulate solution to form spherical co-precipitate particles from the irregular secondary particles. 3 . The method of claim 2 , further comprising: filtering the spherical co-precipitate particles from the particulate solution; washing the filtered spherical co-precipitate particles; and drying the spherical co-precipitate particles. 4 . The method of claim 2 , wherein the spherical co-precipitate particles have a median particle size of greater than 5 microns. 5 . The method of claim 2 , wherein the particulate solution is agitated for 3-72 hours or continuously. 6 . The method of claim 1 , wherein the particulate solution is maintained at a constant temperature in the range of 30-65° C. 7 . The method of claim 1 , wherein the basic solution comprises at least one of an alkali metal hydroxide, an alkali carbonate, and an alkali oxalate. 8 . The method of claim 7 , wherein a concentration of the alkali metal hydroxide in the basic solution ranges from 0.5 mol/L to 10 mol/L. 9 . The method of claim 1 , wherein the precursor co-precipitate material has a composition represented by Mn x M y Co z (OH) 2 . 10 . The method of claim 9 , wherein M comprises one or more metal cations selected from one or more monovalent, divalent, trivalent or tetravalent cations and Ru. 11 . The method of claim 9 , wherein a concentration of the manganese, M, and cobalt sulfates in the aqueous solution ranges from 0.5 mol/L to 5 mol/L. 12 . A precursor to a cathode active material composition, having a composition represented by Mn x M y Co z (OH) 2 . 13 . The precursor of claim 12 , wherein the cathode active material composition has a composition represented by xLi 2 MO 3 .(1−x)LiCo 2 M′ (1−y) O 2 . 14 . The precursor of claim 13 , wherein Mn, Co, M, and M′ possess an average oxidation state of three in the cathode active material composition. 15 . The precursor of claim 13 , wherein the cathode active material composition is created using a solid-state reaction of the precursor and a lithium salt. 16 . The precursor of claim 12 , wherein 0.01≦x<1.00, 0≦y<1.00, and 0.50≦z<1.00. 17 . The precursor of claim 12 , wherein the precursor is formed using a solution co-precipitation reaction. 18 . An apparatus for manufacturing a precursor co-precipitate material for a cathode active material composition, comprising: a reactor maintained at a constant temperature and under an inert gas atmosphere; a first feeding mechanism configured to add an aqueous solution comprising at least one of a manganese sulfate and a cobalt sulfate to the reactor; a second feeding mechanism configured to add a NH 4 OH solution to the aqueous solution to form a particulate solution comprising irregular secondary particles of the precursor co-precipitate material; and a pH controller configured to maintain a constant pH in the range of 10-12 in the particulate solution by adding a basic solution to the particulate solution. 19 . The apparatus of claim 18 , further comprising: an agitator in the reactor, configured to agitate the particulate solution to form spherical co-precipitate particles from the irregular secondary particles. 20 . The apparatus of claim 19 , wherein the particulate solution is agitated for 3-72 hours or continuously. 21 . The apparatus of claim 18 , wherein the constant temperature is in the range of 30-65° C. 22 . The apparatus of claim 18 , wherein the precursor co-precipitate material has a composition represented by Mn x M y Co z (OH) 2 . 23 . The apparatus of claim 18 , wherein the basic solution comprises at least one of an alkali metal hydroxide, an alkali carbonate, and an alkali oxalate. 24 . The apparatus of claim 23 , wherein a concentration of the alkali metal hydroxide in the basic solution ranges from 0.5 mol/L to 10 mol/L. 25 . A spherical precursor co-precipitate material for a cathode active material composition, having a composition represented by Mn x M y Co z (OH) 2 . 26 . The spherical precursor co-precipitate material of claim 25 , wherein M comprises one or more metal cations selected from one or more monovalent, divalent, trivalent or tetravalent cations and Ru. 27 . The spherical precursor co-precipitate material of claim 25 , wherein 0.01≦x≦0.30, 0≦y≦0.20, and 0.70≦z<1.00.
of the type (MnO2)n-, e.g. Li(NixMn1-x)O2 or Li(MyNixMn1-x-y)O2 · CPC title
Solid solutions · CPC title
Powder tap density · CPC title
by d-values or two theta-values, e.g. as X-ray diagram · CPC title
of mixed oxides or hydroxides containing manganese for inserting or intercalating light metals, e.g. LiMn2O4 or LiMn2OxFy · CPC title
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