Degassing method for electrode paste
US-2016248076-A1 · Aug 25, 2016 · US
US11251418B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-11251418-B2 |
| Application number | US-201815900559-A |
| Country | US |
| Kind code | B2 |
| Filing date | Feb 20, 2018 |
| Priority date | Feb 8, 2016 |
| Publication date | Feb 15, 2022 |
| Grant date | Feb 15, 2022 |
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Provided is a method for manufacturing a slurry for a positive electrode of a nonaqueous electrolyte secondary battery containing an alkali metal complex oxide, the method making it possible to reliably deaerate surplus carbonic acid gas after an alkali component of a slurry containing the alkali metal complex oxide is neutralized within a short period of time. The method for manufacturing a slurry for a positive electrode of a nonaqueous electrolyte secondary battery includes a step of manufacturing an electrode slurry including a step of performing a neutralization treatment on an alkali component in the slurry by using inorganic carbon dissolved in a solvent of the slurry and a step of deaerating the inorganic carbon in the slurry as carbonic acid gas by causing cavitation.
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What is claimed is: 1. A method for manufacturing a slurry, the method comprising: performing, by a dispersing and mixing apparatus, a dispersing and mixing step of dispersing and mixing a powder and a solvent to generate a preliminary slurry that comprises a positive electrode active material; performing, by the dispersing and mixing apparatus after the dispersing and mixing apparatus performs the dispersing and mixing step, a neutralizing step of producing a primary neutralized slurry by neutralizing the preliminary slurry; and performing, by the dispersing and mixing apparatus after the dispersing and mixing apparatus performs the neutralizing step, a deaerating step of producing a secondary neutralized slurry by deaerating the primary neutralized slurry, wherein the deaerating step comprises applying, to the primary neutralized slurry, a shearing force in a manner that causes cavitation. 2. The method according to claim 1 , wherein water is used as the solvent. 3. The method according to claim 1 , wherein the neutralizing step comprises adding carbonic acid gas to the preliminary slurry. 4. The method according to claim 3 , wherein the carbonic acid gas in the solvent is used to generate an inorganic carbon in the solvent. 5. The method according to claim 3 , wherein a pressure of the carbonic acid gas is equal to or higher than 0.12 MPa and equal to or lower than 100 MPa. 6. The method according to claim 3 , wherein a pressure of the carbonic acid gas is equal to or higher than 0.2 MPa and equal to or lower than 50 MPa. 7. The method according to claim 3 , wherein a pressure of the carbonic acid gas is equal to or higher than 0.3 MPa and equal to or lower than 10 MPa. 8. The method according to claim 3 , wherein the deaerating step comprises causing, by the dispersing and mixing apparatus, cavitation to deaerate an inorganic carbon in the primary neutralized slurry. 9. The method according to claim 1 , wherein the secondary neutralized slurry is for a positive electrode of a nonaqueous electrolyte secondary battery. 10. The method according to claim 9 , wherein the nonaqueous electrolyte secondary battery comprises an alkali metal complex oxide. 11. The method according to claim 10 , wherein the alkali metal complex oxide is a lithium complex oxide. 12. The method according to claim 1 , wherein the preliminary slurry further comprises a binder and a conductive material. 13. The method according to claim 12 , wherein with respect to a total amount of the positive electrode active material, the binder, and the conductive material: an amount of the positive electrode active material is 60% to 99% by mass, an amount of the binder is 0.1% to 25% by mass, and an amount of the conductive material is 0.1% to 10% by mass. 14. The method according to claim 12 , wherein with respect to a total amount of the positive electrode active material, the binder, and the conductive material: an amount of the positive electrode active material is 80% to 95% by mass, an amount of the binder is 0.5% to 15% by mass, and an amount of the conductive material is 0.5% to 5% by mass. 15. The method according to claim 1 , wherein the secondary neutralized slurry is recirculated to the dispersing and mixing apparatus to be used in the neutralizing step.
containing alkali metals, e.g. LiNiO2 · CPC title
of the type (Mn2O4)-, e.g. LiMn2O4 or Li(MxMn2-x)O4 · CPC title
of electrodes based on mixed oxides or hydroxides, or on mixtures of oxides or hydroxides, e.g. LiCoOx · CPC title
Electrodes based on mixed oxides or hydroxides, or on mixtures of oxides or hydroxides, e.g. LiCoOx · CPC title
containing alkali metals, e.g. LiCoO2 · CPC title
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