Transition metal-containing hydroxide, and method for producing lithium-containing composite oxide
US-2019044139-A1 · Feb 7, 2019 · US
US2022238871A1 · US · A1
| Field | Value |
|---|---|
| Publication number | US-2022238871-A1 |
| Application number | US-202017606648-A |
| Country | US |
| Kind code | A1 |
| Filing date | Sep 25, 2020 |
| Priority date | Sep 26, 2019 |
| Publication date | Jul 28, 2022 |
| Grant date | — |
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A method of preparing a positive electrode active material precursor for a secondary battery includes preparing a positive electrode active material precursor by a co-precipitation reaction while adding a transition metal-containing solution containing transition metal cations, a basic solution, and an ammonium solution to a batch-type reactor, wherein a molar ratio of ammonium ions contained in the ammonium solution to the transition metal cations contained in the transition metal-containing solution added to the batch-type reactor is 0.5 or less, and a pH in the batch-type reactor is maintained at 11.2 or less.
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1 . A method of preparing a positive electrode active material precursor for a secondary battery, the method comprising: preparing a positive electrode active material precursor by a co-precipitation reaction while adding a transition metal-containing solution containing transition metal cations, a basic solution, and an ammonium solution to a batch-type reactor, wherein a molar ratio of ammonium ions contained in the ammonium solution to the transition metal cations contained in the transition metal-containing solution added to the batch-type reactor is 0.5 or less, and a pH in the batch-type reactor is maintained at 11.2 or less. 2 . The method of claim 1 , wherein the molar ratio of the ammonium ions contained in the ammonium solution to the transition metal cations contained in the transition metal-containing solution added to the batch-type reactor is in a range of 0.1 to 0.5. 3 . The method of claim 1 , wherein the pH in the batch-type reactor is maintained at 10.8 to 11.2. 4 . The method of claim 1 , wherein particle nucleation and particle growth are performed without changing the pH in the batch-type reactor during the co-precipitation reaction. 5 . The method of claim 1 , wherein, during the co-precipitation reaction, a stirring speed in a particle nucleation step is in a range of 600 rpm to 800 rpm, and a stirring speed in a particle growth step is in a range of 200 rpm to 400 rpm. 6 . The method of claim 1 , wherein the positive electrode active material precursor has an aspect ratio of a primary particle of less than 0.5. 7 . The method of claim 1 , wherein the positive electrode active material precursor has an average particle diameter (D 50 ) of a secondary particle of 4 μm to 20 μm and has a specific surface area of 9 m 2 /g or more. 8 . The method of claim 7 , wherein the specific surface area is from 9 m 2 /g to 13 m 2 /g. 9 . The method of claim 1 , wherein the positive electrode active material precursor is represented by Formula 1: [Ni x Co y Mn z M 1 w ](OH) 2 [Formula 1] wherein, in Formula 1, M 1 comprises at least one element selected from the group consisting of zirconium (Zr), boron (B), tungsten (W), molybdenum (Mo), chromium (Cr), niobium (Nb), aluminum (Al), magnesium (Mg), hafnium (Hf), tantalum (Ta), lanthanum (La), titanium (Ti), strontium (Sr), barium (Ba), cerium (Ce), fluorine (F), phosphorus (P), sulfur (S), and yttrium (Y), 0.8≤x<1, 0<y≤0.1, 0<z≤0.1, 0≤w≤0.1, and x+y+z+w=1. 10 . A method of preparing a positive electrode active material for a secondary battery, comprising: mixing the positive electrode active material precursor for a secondary battery, which is prepared according to claim 1 , with a lithium source and sintering the mixture to form a lithium transition metal oxide. 11 . A positive electrode active material precursor for a secondary battery which is prepared according to claim 1 , wherein an aspect ratio of a primary particle is less than 0.5, an average particle diameter (D 50 ) of a secondary particle is in a range of 4 μm to 20 μm, and a specific surface area is 9 m 2 /g or more. 12 . A positive electrode active material for a secondary battery which is prepared according to claim 10 , wherein a pellet density is 2.80 g/cc or more.
Energy storage using batteries · CPC title
Electric properties · CPC title
Surface area · CPC title
Powder tap density · CPC title
Solid density · CPC title
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