WO2024060557A1 - Carbonate de cobalt dopé à l'aluminium et sa méthode de préparation - Google Patents
Carbonate de cobalt dopé à l'aluminium et sa méthode de préparation Download PDFInfo
- Publication number
- WO2024060557A1 WO2024060557A1 PCT/CN2023/083440 CN2023083440W WO2024060557A1 WO 2024060557 A1 WO2024060557 A1 WO 2024060557A1 CN 2023083440 W CN2023083440 W CN 2023083440W WO 2024060557 A1 WO2024060557 A1 WO 2024060557A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- aluminum
- cobalt carbonate
- doped cobalt
- molten metal
- liquid
- Prior art date
Links
- 229910021446 cobalt carbonate Inorganic materials 0.000 title claims abstract description 99
- ZOTKGJBKKKVBJZ-UHFFFAOYSA-L cobalt(2+);carbonate Chemical compound [Co+2].[O-]C([O-])=O ZOTKGJBKKKVBJZ-UHFFFAOYSA-L 0.000 title claims abstract description 99
- 238000002360 preparation method Methods 0.000 title claims abstract description 44
- 229910052751 metal Inorganic materials 0.000 claims abstract description 118
- 239000002184 metal Substances 0.000 claims abstract description 117
- 239000007788 liquid Substances 0.000 claims abstract description 113
- 238000006243 chemical reaction Methods 0.000 claims abstract description 101
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 37
- 239000013078 crystal Substances 0.000 claims abstract description 32
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 claims abstract description 20
- 150000001868 cobalt Chemical class 0.000 claims abstract description 19
- 239000002270 dispersing agent Substances 0.000 claims abstract description 14
- BVKZGUZCCUSVTD-UHFFFAOYSA-L Carbonate Chemical compound [O-]C([O-])=O BVKZGUZCCUSVTD-UHFFFAOYSA-L 0.000 claims abstract description 11
- AZDRQVAHHNSJOQ-UHFFFAOYSA-N alumane Chemical class [AlH3] AZDRQVAHHNSJOQ-UHFFFAOYSA-N 0.000 claims abstract description 7
- BVKZGUZCCUSVTD-UHFFFAOYSA-M Bicarbonate Chemical compound OC([O-])=O BVKZGUZCCUSVTD-UHFFFAOYSA-M 0.000 claims abstract description 5
- 229910052782 aluminium Inorganic materials 0.000 claims description 37
- 229910001429 cobalt ion Inorganic materials 0.000 claims description 29
- XLJKHNWPARRRJB-UHFFFAOYSA-N cobalt(2+) Chemical compound [Co+2] XLJKHNWPARRRJB-UHFFFAOYSA-N 0.000 claims description 29
- PUKLDDOGISCFCP-JSQCKWNTSA-N 21-Deoxycortisone Chemical group C1CC2=CC(=O)CC[C@]2(C)[C@@H]2[C@@H]1[C@@H]1CC[C@@](C(=O)C)(O)[C@@]1(C)CC2=O PUKLDDOGISCFCP-JSQCKWNTSA-N 0.000 claims description 23
- FCYKAQOGGFGCMD-UHFFFAOYSA-N Fulvic acid Natural products O1C2=CC(O)=C(O)C(C(O)=O)=C2C(=O)C2=C1CC(C)(O)OC2 FCYKAQOGGFGCMD-UHFFFAOYSA-N 0.000 claims description 22
- 229940095100 fulvic acid Drugs 0.000 claims description 22
- 239000002509 fulvic acid Substances 0.000 claims description 22
- -1 aluminum ions Chemical class 0.000 claims description 21
- ATRRKUHOCOJYRX-UHFFFAOYSA-N Ammonium bicarbonate Chemical group [NH4+].OC([O-])=O ATRRKUHOCOJYRX-UHFFFAOYSA-N 0.000 claims description 18
- 239000001099 ammonium carbonate Substances 0.000 claims description 18
- 239000007787 solid Substances 0.000 claims description 18
- 238000000034 method Methods 0.000 claims description 17
- 229910000013 Ammonium bicarbonate Inorganic materials 0.000 claims description 14
- 235000012538 ammonium bicarbonate Nutrition 0.000 claims description 14
- 235000012501 ammonium carbonate Nutrition 0.000 claims description 4
- 239000003795 chemical substances by application Substances 0.000 claims description 3
- 230000001376 precipitating effect Effects 0.000 claims description 2
- 239000002245 particle Substances 0.000 abstract description 33
- 238000000926 separation method Methods 0.000 abstract description 7
- 238000009826 distribution Methods 0.000 abstract description 5
- 230000000052 comparative effect Effects 0.000 description 23
- 238000003756 stirring Methods 0.000 description 22
- KRKNYBCHXYNGOX-UHFFFAOYSA-N citric acid Chemical compound OC(=O)CC(O)(C(O)=O)CC(O)=O KRKNYBCHXYNGOX-UHFFFAOYSA-N 0.000 description 18
- 238000005406 washing Methods 0.000 description 18
- LFHXPRTYXDXTDD-UHFFFAOYSA-H bis(2,2-dioxo-1,3,2,4-dioxathialumetan-4-yl) sulfate octahydrate Chemical compound O.O.O.O.O.O.O.O.[Al+3].[Al+3].[O-]S([O-])(=O)=O.[O-]S([O-])(=O)=O.[O-]S([O-])(=O)=O LFHXPRTYXDXTDD-UHFFFAOYSA-H 0.000 description 12
- 238000001878 scanning electron micrograph Methods 0.000 description 11
- GVPFVAHMJGGAJG-UHFFFAOYSA-L cobalt dichloride Chemical compound [Cl-].[Cl-].[Co+2] GVPFVAHMJGGAJG-UHFFFAOYSA-L 0.000 description 10
- 238000001035 drying Methods 0.000 description 9
- 238000012360 testing method Methods 0.000 description 9
- 229910017052 cobalt Inorganic materials 0.000 description 8
- 239000010941 cobalt Substances 0.000 description 8
- GUTLYIVDDKVIGB-UHFFFAOYSA-N cobalt atom Chemical compound [Co] GUTLYIVDDKVIGB-UHFFFAOYSA-N 0.000 description 8
- 229910000625 lithium cobalt oxide Inorganic materials 0.000 description 6
- BFZPBUKRYWOWDV-UHFFFAOYSA-N lithium;oxido(oxo)cobalt Chemical compound [Li+].[O-][Co]=O BFZPBUKRYWOWDV-UHFFFAOYSA-N 0.000 description 6
- 230000002776 aggregation Effects 0.000 description 5
- 239000012071 phase Substances 0.000 description 5
- SECXISVLQFMRJM-UHFFFAOYSA-N N-Methylpyrrolidone Chemical compound CN1CCCC1=O SECXISVLQFMRJM-UHFFFAOYSA-N 0.000 description 4
- 238000005054 agglomeration Methods 0.000 description 4
- 230000015572 biosynthetic process Effects 0.000 description 4
- UBEWDCMIDFGDOO-UHFFFAOYSA-N cobalt(2+);cobalt(3+);oxygen(2-) Chemical compound [O-2].[O-2].[O-2].[O-2].[Co+2].[Co+3].[Co+3] UBEWDCMIDFGDOO-UHFFFAOYSA-N 0.000 description 4
- 150000002500 ions Chemical class 0.000 description 4
- 230000008569 process Effects 0.000 description 4
- 239000010406 cathode material Substances 0.000 description 3
- UFMZWBIQTDUYBN-UHFFFAOYSA-N cobalt dinitrate Chemical compound [Co+2].[O-][N+]([O-])=O.[O-][N+]([O-])=O UFMZWBIQTDUYBN-UHFFFAOYSA-N 0.000 description 3
- 229910001981 cobalt nitrate Inorganic materials 0.000 description 3
- 229940044175 cobalt sulfate Drugs 0.000 description 3
- 229910000361 cobalt sulfate Inorganic materials 0.000 description 3
- KTVIXTQDYHMGHF-UHFFFAOYSA-L cobalt(2+) sulfate Chemical compound [Co+2].[O-]S([O-])(=O)=O KTVIXTQDYHMGHF-UHFFFAOYSA-L 0.000 description 3
- 230000007423 decrease Effects 0.000 description 3
- 229910021645 metal ion Inorganic materials 0.000 description 3
- 238000003786 synthesis reaction Methods 0.000 description 3
- 238000009827 uniform distribution Methods 0.000 description 3
- WHXSMMKQMYFTQS-UHFFFAOYSA-N Lithium Chemical compound [Li] WHXSMMKQMYFTQS-UHFFFAOYSA-N 0.000 description 2
- HBBGRARXTFLTSG-UHFFFAOYSA-N Lithium ion Chemical compound [Li+] HBBGRARXTFLTSG-UHFFFAOYSA-N 0.000 description 2
- 239000002033 PVDF binder Substances 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 2
- 229910001338 liquidmetal Inorganic materials 0.000 description 2
- 229910052744 lithium Inorganic materials 0.000 description 2
- 229910001416 lithium ion Inorganic materials 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 230000006911 nucleation Effects 0.000 description 2
- 238000010899 nucleation Methods 0.000 description 2
- 238000011056 performance test Methods 0.000 description 2
- 229920002981 polyvinylidene fluoride Polymers 0.000 description 2
- 239000002002 slurry Substances 0.000 description 2
- 238000006467 substitution reaction Methods 0.000 description 2
- QGZKDVFQNNGYKY-UHFFFAOYSA-O Ammonium Chemical compound [NH4+] QGZKDVFQNNGYKY-UHFFFAOYSA-O 0.000 description 1
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 1
- 239000006230 acetylene black Substances 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 238000004220 aggregation Methods 0.000 description 1
- DIZPMCHEQGEION-UHFFFAOYSA-H aluminium sulfate (anhydrous) Chemical compound [Al+3].[Al+3].[O-]S([O-])(=O)=O.[O-]S([O-])(=O)=O.[O-]S([O-])(=O)=O DIZPMCHEQGEION-UHFFFAOYSA-H 0.000 description 1
- AMVQGJHFDJVOOB-UHFFFAOYSA-H aluminium sulfate octadecahydrate Chemical group O.O.O.O.O.O.O.O.O.O.O.O.O.O.O.O.O.O.[Al+3].[Al+3].[O-]S([O-])(=O)=O.[O-]S([O-])(=O)=O.[O-]S([O-])(=O)=O AMVQGJHFDJVOOB-UHFFFAOYSA-H 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 125000002915 carbonyl group Chemical group [*:2]C([*:1])=O 0.000 description 1
- 125000003178 carboxy group Chemical group [H]OC(*)=O 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 239000002738 chelating agent Substances 0.000 description 1
- IVMYJDGYRUAWML-UHFFFAOYSA-N cobalt(ii) oxide Chemical class [Co]=O IVMYJDGYRUAWML-UHFFFAOYSA-N 0.000 description 1
- 230000000536 complexating effect Effects 0.000 description 1
- 238000009831 deintercalation Methods 0.000 description 1
- 238000000724 energy-dispersive X-ray spectrum Methods 0.000 description 1
- 239000011888 foil Substances 0.000 description 1
- 230000012010 growth Effects 0.000 description 1
- 239000003864 humus Substances 0.000 description 1
- 125000002887 hydroxy group Chemical group [H]O* 0.000 description 1
- XGZVUEUWXADBQD-UHFFFAOYSA-L lithium carbonate Chemical compound [Li+].[Li+].[O-]C([O-])=O XGZVUEUWXADBQD-UHFFFAOYSA-L 0.000 description 1
- 229910052808 lithium carbonate Inorganic materials 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 239000004570 mortar (masonry) Substances 0.000 description 1
- 231100000252 nontoxic Toxicity 0.000 description 1
- 230000003000 nontoxic effect Effects 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- ISWSIDIOOBJBQZ-UHFFFAOYSA-N phenol group Chemical group C1(=CC=CC=C1)O ISWSIDIOOBJBQZ-UHFFFAOYSA-N 0.000 description 1
- 229920006254 polymer film Polymers 0.000 description 1
- 238000001556 precipitation Methods 0.000 description 1
- 239000002243 precursor Substances 0.000 description 1
- 230000034655 secondary growth Effects 0.000 description 1
- 238000005204 segregation Methods 0.000 description 1
- 238000005245 sintering Methods 0.000 description 1
- 239000007790 solid phase Substances 0.000 description 1
- 238000007614 solvation Methods 0.000 description 1
- 238000001228 spectrum Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01G—COMPOUNDS CONTAINING METALS NOT COVERED BY SUBCLASSES C01D OR C01F
- C01G51/00—Compounds of cobalt
- C01G51/06—Carbonates
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01P—INDEXING SCHEME RELATING TO STRUCTURAL AND PHYSICAL ASPECTS OF SOLID INORGANIC COMPOUNDS
- C01P2002/00—Crystal-structural characteristics
- C01P2002/80—Crystal-structural characteristics defined by measured data other than those specified in group C01P2002/70
- C01P2002/85—Crystal-structural characteristics defined by measured data other than those specified in group C01P2002/70 by XPS, EDX or EDAX data
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01P—INDEXING SCHEME RELATING TO STRUCTURAL AND PHYSICAL ASPECTS OF SOLID INORGANIC COMPOUNDS
- C01P2004/00—Particle morphology
- C01P2004/01—Particle morphology depicted by an image
- C01P2004/03—Particle morphology depicted by an image obtained by SEM
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01P—INDEXING SCHEME RELATING TO STRUCTURAL AND PHYSICAL ASPECTS OF SOLID INORGANIC COMPOUNDS
- C01P2004/00—Particle morphology
- C01P2004/60—Particles characterised by their size
- C01P2004/61—Micrometer sized, i.e. from 1-100 micrometer
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01P—INDEXING SCHEME RELATING TO STRUCTURAL AND PHYSICAL ASPECTS OF SOLID INORGANIC COMPOUNDS
- C01P2004/00—Particle morphology
- C01P2004/80—Particles consisting of a mixture of two or more inorganic phases
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/10—Energy storage using batteries
Definitions
- the invention belongs to the technical field of battery materials, and particularly relates to aluminum-doped cobalt carbonate and a preparation method thereof.
- Lithium cobalt oxide lithium-ion batteries can release higher capacity at high voltages and have unique advantages in energy density.
- lithium cobalt oxide has the problem of unstable bulk structure under high voltage.
- Doping with aluminum can stabilize the layered structure with oxygen as the skeleton and improve the structural stability.
- Cobalt tetroxide is the precursor of lithium cobalt oxide, and its performance is largely determined by the performance of cobalt carbonate. With the increase of aluminum doping, how to achieve uniform distribution of aluminum in cobalt carbonate has become a challenge to be tackled.
- the present invention aims to solve at least one of the technical problems existing in the prior art.
- the present invention proposes an aluminum-doped cobalt carbonate and a preparation method thereof.
- the aluminum-doped cobalt carbonate prepared by the preparation method has a uniform size, few small particles, and a uniform distribution of aluminum elements.
- a preparation method of aluminum-doped cobalt carbonate including the following steps:
- Liquid preparation Dissolve soluble cobalt salt, soluble aluminum salt and dispersant in water to obtain molten metal A. Dissolve soluble cobalt salt and soluble aluminum salt in water to obtain molten metal B. Prepare bicarbonate as the bottom liquid. , prepare carbonate as precipitating agent;
- Reaction I Add the molten metal A and the precipitant into the bottom liquid in parallel flow and react to generate a mixed system containing aluminum-doped cobalt carbonate crystals;
- Reaction II When the D50 of the aluminum-doped cobalt carbonate crystal generated in step (2) grows to 14-15 ⁇ m, stop adding the molten metal A to the mixed system, and simultaneously add the molten metal B and The precipitant is added to the mixed system in parallel flow and reacts. When the D50 of the generated aluminum-doped cobalt carbonate crystal grows to 18-20 ⁇ m, the solid and liquid are separated to obtain the aluminum-doped cobalt carbonate.
- the dispersant is fulvic acid.
- the molar ratio of fulvic acid to aluminum in the molten metal A is 0.01-0.5.
- the molar ratio of fulvic acid to aluminum in the molten metal A is 0.05-0.3.
- the mass ratio of aluminum ions to cobalt ions in the metal liquid A and the metal liquid B is 0.005-0.02.
- the mass ratio of aluminum ions to cobalt ions in the molten metal A and the molten metal B is 0.008-0.0165.
- the cobalt ion concentration in the metal liquid A and the metal liquid B is 0.3-4 mol/L.
- the cobalt ion concentration in the metal liquid A and the metal liquid B is 0.5-3 mol/L.
- the bicarbonate is ammonium bicarbonate.
- the carbonate is ammonium bicarbonate and/or ammonium carbonate, and the concentration of the carbonate is 1-5 mol/L.
- the concentration of the carbonate is 2-3 mol/L.
- the soluble cobalt salt is at least one of cobalt chloride, cobalt sulfate and cobalt nitrate.
- the soluble aluminum salt is aluminum sulfate octadecahydrate.
- the reaction temperature in step (2) is 30-50°C.
- reaction temperature in step (2) is 35-48°C.
- the concentration of the bottom liquid is 0.2-5 mol/L.
- the concentration of the bottom liquid is 0.5-3 mol/L.
- the flow rate of the molten metal A is 5-40 L/h, and the flow rate of the precipitant is controlled so that the molar ratio of the precipitant to the cobalt salt in the molten metal A is 2-4.
- step (2) the flow rate of the molten metal A is 7-35L/h, and the flow rate of the precipitant is controlled at a molar ratio of the precipitant to the cobalt salt in the molten metal A of 2.2- 3.
- the reaction in step (2) is carried out under stirring, and the stirring frequency is 10-30 Hz.
- step (2) is carried out under stirring, and the stirring frequency is 12-28 Hz.
- the reaction in step (3) is carried out under stirring, and the stirring frequency is lower than that in step (3).
- step (3) is carried out under stirring, and the stirring frequency is reduced by 1-3 Hz compared with step (2).
- the flow rate of the molten metal B is 5-40L/h.
- step (3) the flow rate of the molten metal B is 7-35L/h.
- step (3) the solid after solid-liquid separation is also washed and dried to obtain the aluminum-doped cobalt carbonate.
- the washing method is centrifugal washing, and the temperature of the water used for washing is 40-80°C.
- the temperature of water used for washing is 50-70°C.
- the drying temperature is 70-150°C.
- the drying temperature is 90-120°C.
- both reaction I and reaction II are carried out in a reaction kettle, and the bottom liquid volume is 0.3-0.6 times the total volume of the reaction kettle.
- the D50 of the aluminum-doped cobalt carbonate crystal generated in reaction I is half of the length of the kettle when it reaches 9-10 ⁇ m.
- dividing half of the kettle means dividing half of the materials in the reaction kettle into another reaction kettle to continue the reaction.
- the pot is divided into half.
- Aluminum-doped cobalt carbonate is prepared by the preparation method as described above.
- the present invention in order to increase production capacity, is designed to use a larger cobalt salt flow rate to participate in the reaction.
- the size of the aluminum-doped cobalt carbonate particles is small and has a large specific surface area.
- the reaction conditions of large cobalt salt flow rate will bring about the problem of particle agglomeration.
- the present invention A dispersant is added to the metal liquid. The dispersant can effectively change the surface state of the particles and form a polymer film on the surface of the particles to prevent the particles from contacting each other and effectively alleviate particle agglomeration.
- reaction metal liquid is replaced in the later stage of the reaction, and the molten metal A is Switching to the metal liquid B can increase the surface energy of the cobalt carbonate particles, which is conducive to the particle surface capturing metal ions in the reaction system for secondary growth and avoiding the generation of new nuclei.
- the dispersant used is fulvic acid.
- Fulvic acid is a substance extracted from humus. It is safe, non-toxic, and environmentally friendly.
- the fulvic acid structure contains a large number of phenolic hydroxyl groups. , carbonyl and other groups, it can be used as a chelating agent to combine with metal ions, which is beneficial to the uniform distribution of aluminum elements, and can also be used as a dispersant to inhibit particle agglomeration.
- Figure 1 is an SEM image of aluminum-doped cobalt carbonate prepared in Example 1 of the present invention.
- Figure 2 is a cross-sectional SEM image and EDS spectrum of aluminum-doped cobalt carbonate prepared in Example 2 of the present invention
- Figure 3 is an SEM image of aluminum-doped cobalt carbonate prepared in Comparative Example 1 of the present invention.
- Figure 4 is an SEM image and a cross-sectional SEM image of aluminum-doped cobalt carbonate prepared in Comparative Example 2 of the present invention
- Figure 5 is an SEM image of aluminum-doped cobalt carbonate prepared in Comparative Example 3 of the present invention.
- a preparation method of aluminum-doped cobalt carbonate including the following steps:
- Liquid preparation Add cobalt chloride, aluminum sulfate octahydrate, fulvic acid and water to metal liquid preparation tank A to obtain metal liquid A.
- concentration of cobalt ions in metal liquid A is 0.5mol/L, and the concentration of aluminum ions is 0.5mol/L.
- the mass ratio to cobalt ions is 0.008, and the molar ratio of fulvic acid to aluminum ions is 0.05; add cobalt chloride, aluminum sulfate octahydrate and water to metal liquid tank B to obtain metal liquid B.
- Cobalt in metal liquid B The concentration of ions is 0.5mol/L, and the mass ratio of aluminum ions to cobalt ions is 0.008; add precipitant to the precipitant preparation tank.
- the precipitant is ammonium bicarbonate with a concentration of 2mol/L, and the prepared concentration is 0.5mol/L. Ammonium bicarbonate is used as the base liquid;
- Reaction I Add a bottom liquid into the reactor, the volume of the bottom liquid is 0.3 times the total volume of the reactor, add the metal liquid A and the precipitant into the reactor in parallel, wherein the flow rate of the metal liquid A is 7 L/h, the flow rate of the precipitant is controlled so that the molar ratio of the precipitant to the cobalt salt is 2.2, the temperature is raised to 35°C, the stirring speed is 12 Hz, and the reactor is left to stand and evacuate when it is full.
- the D50 of the cobalt aluminate-doped carbonate crystals grows to 9 ⁇ m, half of the reactor is divided, and then the parallel flow reaction is continued;
- Reaction II When the kettle is full, let it stand and drain. When the D50 of the aluminum-doped cobalt carbonate crystal grows to 14 ⁇ m, divide the kettle into half, switch the molten metal A to the molten metal B, and continue to add the molten metal B into the reaction kettle in parallel flow. and precipitant, lower the stirring speed by 1 Hz, and control the reaction temperature and flow rate the same as Reaction I. When the kettle is full, let it stand and drain, until the D50 of the aluminum-doped cobalt carbonate crystal grows to 18 ⁇ m, the reaction ends, and the solid-liquid separation is performed to obtain a solid;
- the SEM image of the aluminum-doped cobalt carbonate prepared in Example 1 is shown in Figure 1. It can be seen from the figure that the size of the aluminum-doped cobalt carbonate particles is uniform, there are almost no small particles, and there is no aluminum segregation on the surface.
- a method for preparing aluminum-doped cobalt carbonate comprises the following steps:
- Liquid preparation Add cobalt sulfate, aluminum sulfate octahydrate, fulvic acid and water to the metal liquid preparation tank A to obtain metal liquid A.
- concentration of cobalt ions in metal liquid A is 3mol/L.
- Aluminum ions and cobalt The mass ratio of ions is 0.0165, and the molar ratio of fulvic acid to aluminum ions is 0.3; add cobalt sulfate, aluminum sulfate octahydrate and water to metal liquid preparation tank B to obtain metal liquid B.
- the concentration of cobalt ions in metal liquid B The mass ratio of aluminum ions to cobalt ions is 0.0165; add precipitant to the precipitant liquid tank.
- the precipitant is ammonium carbonate with a concentration of 3mol/L.
- Reaction I Pour the bottom liquid into the reaction kettle. The volume of the bottom liquid is 0.6 times the total volume of the reaction kettle. Add molten metal A and the precipitant into the reaction kettle in parallel flow. The flow rate of molten metal A is 35L/h. , the flow rate of the precipitant is controlled so that the molar ratio of the precipitant to the cobalt salt is 3, the temperature rises to 48°C, the stirring speed is 28Hz, and the kettle is left to stand and drained when it is full, until the D50 of the aluminum-doped cobalt carbonate crystal grows to 10 ⁇ m. Half, then continue the parallel flow reaction;
- Reaction II When the kettle is full, let it stand and pump out the water until the D50 of the cobalt aluminate-doped carbonate crystals grows to 15 ⁇ m. Half of the kettle is divided, and the metal liquid A is switched to the metal liquid B. The metal liquid B and the precipitant are added to the reactor in parallel. The stirring speed is lowered by 3 Hz. The reaction temperature and flow rate are controlled in the same way as in Reaction I. When the kettle is full, let it stand and pump out the water until the D50 of the cobalt aluminate-doped carbonate crystals grows to 20 ⁇ m. The reaction is terminated and the solid-liquid separation is performed to obtain a solid.
- the SEM image of the aluminum-doped cobalt carbonate prepared in Example 2 is shown in Figure 2. It can be seen from the figure that the interior of the bulk phase of the aluminum-doped cobalt carbonate is smooth and there is no aluminum aggregation, indicating that the aluminum element is evenly distributed in the bulk phase, and at the same time, cross section
- the EDS surface scan obtained the EDS energy spectrum as shown in Figure 2. The test results show that there are metal elements cobalt and aluminum in the cross section, indicating that aluminum has been doped inside the cobalt carbonate.
- a preparation method of aluminum-doped cobalt carbonate including the following steps:
- Liquid preparation Add cobalt nitrate, aluminum sulfate octahydrate, fulvic acid and water to the metal liquid preparation tank A to obtain metal liquid A.
- concentration of cobalt ions in metal liquid A is 2.5 mol/L, and the aluminum ions and The mass ratio of cobalt ions is 0.0137, and the molar ratio of fulvic acid to aluminum ions is 0.2; add cobalt nitrate, aluminum sulfate octahydrate and water to metal liquid preparation tank B to obtain metal liquid B.
- the cobalt ions in metal liquid B are The concentration is 2.5mol/L, and the mass ratio of aluminum ions to cobalt ions is 0.0137; add precipitant to the precipitant preparation tank.
- the precipitant is ammonium carbonate with a concentration of 2.5mol/L, and prepare hydrogen carbonate with a concentration of 1mol/L. Ammonium serves as base liquid;
- Reaction I Pour the bottom liquid into the reaction kettle.
- the volume of the bottom liquid is 0.5 times the total volume of the reaction kettle.
- the kettle is full, it is left to stand and drained until the D50 of the aluminum-doped cobalt carbonate crystal grows to 9.5 ⁇ m. Divide the kettle into half, and then continue the parallel flow reaction;
- Reaction II When the kettle is full, let it stand and drain until the D50 of the aluminum-doped cobalt carbonate crystal grows to 14.5 ⁇ m. Divide the kettle into half, switch the molten metal A to the molten metal B, and continue to add the molten metal into the reaction kettle in parallel flow. B and precipitant, lower the stirring speed by 2 Hz, and control the reaction temperature and flow rate the same as reaction I. When the kettle is full, let it stand and drain out. The reaction ends when the D50 of the aluminum-doped cobalt carbonate crystal grows to 18.5 ⁇ m. The solid-liquid separation is obtained to obtain a solid. thing;
- Washing and drying Use a centrifuge to centrifuge and wash the solid matter, select pure water at 60°C as the washing water, and then dry it in an oven at 110°C to obtain aluminum-doped cobalt carbonate.
- Comparative Example 1 (The difference from Example 1 is that Comparative Example 1 also added a dispersant to the bottom liquid)
- a method for preparing aluminum-doped cobalt carbonate comprises the following steps:
- Liquid preparation Add cobalt chloride, aluminum sulfate octahydrate, fulvic acid and water to metal liquid preparation tank A to obtain metal liquid A.
- concentration of cobalt ions in metal liquid A is 0.5mol/L
- concentration of aluminum ions is 0.5mol/L.
- the mass ratio to cobalt ions is 0.008, and the molar ratio of fulvic acid to aluminum ions is 0.05; add cobalt chloride, aluminum sulfate octahydrate and water to metal liquid tank B to obtain metal liquid B.
- Cobalt in metal liquid B The concentration of ions is 0.5mol/L, and the mass ratio of aluminum ions to cobalt ions is 0.008; add precipitant to the precipitant preparation tank.
- the precipitant is ammonium bicarbonate with a concentration of 2mol/L, and the prepared concentration is 0.5mol/L.
- Ammonium bicarbonate was used as the base liquid, and the base liquid was added with Fulvic acid, and the concentration of fulvic acid in the bottom solution is 5g/L;
- Reaction I Pour the bottom liquid into the reaction kettle. The volume of the bottom liquid is 0.3 times the total volume of the reaction kettle. Add molten metal A and the precipitant into the reaction kettle in parallel flow. The flow rate of molten metal A is 7L/h. , the flow rate of the precipitant is controlled so that the molar ratio of the precipitant to the cobalt salt is 2.2, the temperature rises to 35°C, the stirring speed is 12Hz, and the kettle is left to stand and drained when full, until the D50 of the aluminum-doped cobalt carbonate crystal grows to 9 ⁇ m. The kettle is half full, and then continue the parallel flow reaction;
- Reaction II When the kettle is full, let it stand and drain. When the D50 of the aluminum-doped cobalt carbonate crystal grows to 14 ⁇ m, divide the kettle into half, switch the molten metal A to the molten metal B, and continue to add the molten metal B into the reaction kettle in parallel flow. and precipitant, lower the stirring speed by 1 Hz, and control the reaction temperature and flow rate the same as Reaction I. When the kettle is full, let it stand and drain, until the D50 of the aluminum-doped cobalt carbonate crystal grows to 18 ⁇ m, the reaction ends, and the solid-liquid separation is performed to obtain a solid;
- Comparative Example 2 (The difference from Example 1 is that no dispersant is added to the molten metal A in Comparative Example 2)
- a preparation method of aluminum-doped cobalt carbonate including the following steps:
- Liquid preparation Add cobalt chloride, aluminum sulfate octahydrate and water to the metal liquid preparation tank A to obtain metal liquid A.
- concentration of cobalt ions in metal liquid A is 0.5mol/L.
- Aluminum ions and cobalt ions The mass ratio is 0.008; add cobalt chloride, aluminum sulfate octahydrate and water to the metal liquid preparation tank B to obtain metal liquid B.
- the concentration of cobalt ions in metal liquid B is 0.5mol/L.
- Aluminum ions and cobalt ions The mass ratio is 0.008; add precipitant to the precipitant liquid tank, the precipitant is ammonium bicarbonate with a concentration of 2mol/L, and ammonium bicarbonate with a concentration of 0.5mol/L is prepared as the bottom liquid;
- Reaction I Pour the bottom liquid into the reaction kettle. The volume of the bottom liquid is 0.3 times the total volume of the reaction kettle. Add molten metal A and the precipitant into the reaction kettle in parallel flow. The flow rate of molten metal A is 7L/h. , the flow rate of the precipitant is controlled so that the molar ratio of the precipitant to the cobalt salt is 2.2, the temperature rises to 35°C, the stirring speed is 12Hz, and the kettle is left standing until the D50 of the aluminum-doped cobalt carbonate crystal reaches 9 ⁇ m. Divide the kettle into half, and then continue the parallel flow reaction;
- Reaction II When the kettle is full, let it stand and drain. When the D50 of the aluminum-doped cobalt carbonate crystal grows to 14 ⁇ m, divide the kettle into half, switch the molten metal A to the molten metal B, and continue to add the molten metal B into the reaction kettle in parallel flow. He Shen Precipitation agent, the stirring speed is reduced by 1 Hz, the reaction temperature and flow control are the same as Reaction I, the kettle is left to stand and drained when full, and the reaction is completed when the D50 of the aluminum-doped cobalt carbonate crystal grows to 18 ⁇ m, and the solid-liquid is separated to obtain a solid;
- Comparative Example 3 (The difference from Example 1 is that Comparative Example 3 uses molten metal A throughout the reaction)
- a preparation method of aluminum-doped cobalt carbonate including the following steps:
- Liquid preparation cobalt chloride, aluminum sulfate 18hydrate, fulvic acid and water are added to a metal liquid preparation tank A to obtain a metal liquid A, wherein the concentration of cobalt ions in the metal liquid A is 0.5 mol/L, the mass ratio of aluminum ions to cobalt ions is 0.008, and the molar ratio of fulvic acid to aluminum ions is 0.05; a precipitant is added to a precipitant preparation tank, wherein the precipitant is ammonium bicarbonate with a concentration of 2 mol/L, and ammonium bicarbonate with a concentration of 0.5 mol/L is prepared as a base liquid;
- Reaction I Pour the bottom liquid into the reaction kettle. The volume of the bottom liquid is 0.3 times the total volume of the reaction kettle. Add molten metal A and the precipitant into the reaction kettle in parallel flow. The flow rate of molten metal A is 7L/h. , the flow rate of the precipitant is controlled so that the molar ratio of the precipitant to the cobalt salt is 2.2, the temperature rises to 35°C, the stirring speed is 12Hz, and the kettle is left standing until the D50 of the aluminum-doped cobalt carbonate crystal grows to 9 ⁇ m. Half, then continue the parallel flow reaction;
- Reaction II When the kettle is full, let it stand and drain. When the D50 of the aluminum-doped cobalt carbonate crystal grows to 14 ⁇ m, divide the kettle into half. The molten metal A continues to flow into the reaction kettle together with the precipitant. The stirring speed is reduced by 1 Hz. The reaction The temperature and flow control are the same as in Reaction I. When the kettle is full, let it stand and drain. The reaction ends when the D50 of the aluminum-doped cobalt carbonate crystal grows to 18 ⁇ m. The solid and liquid are separated to obtain a solid;
- the SEM image of the aluminum-doped cobalt carbonate prepared in Comparative Example 3 is shown in Figure 5. It can be seen from the figure that there are small particles of different sizes in the sample, indicating that the nucleation speed of the particles in the later stage of the reaction is greater than the growth rate. As the particle size continues to grow, the participation of dispersants makes the electrostatic repulsion and solvation film on the particle surface more obvious, making it more difficult for metal ions to attach to the particle surface and nucleate alone.
- Comparative Example 4 (The difference from Example 1 is that fulvic acid is replaced by citric acid in the metal liquid A of Comparative Example 4)
- a preparation method of aluminum-doped cobalt carbonate including the following steps:
- Liquid preparation Add cobalt chloride, aluminum sulfate octahydrate, citric acid and water to metal liquid preparation tank A to obtain metal liquid A.
- concentration of cobalt ions in metal liquid A is 0.5mol/L, and the concentration of aluminum ions is 0.5mol/L.
- the mass ratio to cobalt ions is 0.008, and the molar ratio of citric acid to aluminum is 0.05; add cobalt chloride, aluminum sulfate octahydrate and water to metal liquid preparation tank B to obtain metal liquid B.
- Cobalt ions in metal liquid B are The concentration is 0.5mol/L, and the mass ratio of aluminum ions to cobalt ions is 0.008; add precipitant to the precipitant preparation tank.
- the precipitant is ammonium bicarbonate with a concentration of 2mol/L, and the prepared concentration is 0.5mol/L. Ammonium bicarbonate is used as the base liquid;
- Reaction I Pour the bottom liquid into the reaction kettle. The volume of the bottom liquid is 0.3 times the total volume of the reaction kettle. Add molten metal A and the precipitant into the reaction kettle in parallel flow. The flow rate of molten metal A is 7L/h. , the flow rate of the precipitant is controlled at a molar ratio of precipitant to cobalt salt of 2.2, the temperature rises to 35°C, the stirring speed is 12Hz, and the kettle is left to stand and drained when it is full. When the D50 of the aluminum-doped cobalt carbonate crystal grows to 9 ⁇ m, the kettle is half filled. , and then continue the parallel flow reaction;
- Reaction II When the kettle is full, let it stand and drain. When the D50 of the aluminum-doped cobalt carbonate crystal grows to 14 ⁇ m, divide the kettle into half, switch the molten metal A to the molten metal B, and continue to add the molten metal B into the reaction kettle in parallel flow. and precipitant, lower the stirring speed by 1 Hz, and control the reaction temperature and flow rate the same as Reaction I. When the kettle is full, let it stand and drain, until the D50 of the aluminum-doped cobalt carbonate crystal grows to 18 ⁇ m, the reaction ends, and the solid-liquid separation is performed to obtain a solid;
- Example 1 The aluminum-doped cobalt carbonate prepared in Example 1, Comparative Example 2 and Comparative Example 4 were respectively calcined at 700°C for 3 hours to obtain tricobalt tetroxide. Then the obtained tricobalt tetroxide was evenly mixed with lithium carbonate according to the Li:Co molar ratio of 1.05, and placed in a push plate kiln for solid phase sintering at 950°C for 12 hours to obtain lithium cobalt oxide cathode material, and each of the obtained cobalt oxides was Lithium cathode materials are tested for electrochemical performance.
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Inorganic Chemistry (AREA)
- Inorganic Compounds Of Heavy Metals (AREA)
Abstract
L'invention concerne une méthode de préparation de carbonate de cobalt dopé à l'aluminium. La méthode de préparation comprend les étapes suivantes : (1) préparation d'un liquide : dissolution d'un sel de cobalt soluble, d'un sel d'aluminium soluble et d'un agent de dispersion dans de l'eau pour obtenir un métal fondu A, dissolution d'un sel de cobalt soluble et d'un sel d'aluminium soluble dans de l'eau pour obtenir un métal fondu B, préparation de bicarbonate en tant que solution de base, et préparation de carbonate en tant que précipitant ; (2) réaction I : ajout du métal fondu A et du précipitant dans la solution de base en parallèle, et réaction pour générer un système mixte contenant un cristal de carbonate de cobalt dopé à l'aluminium ; et (3) réaction II : arrêt de l'ajout du métal fondu A dans le système mixte lorsque le D50 du cristal de carbonate de cobalt dopé à l'aluminium généré à l'étape (2) atteint jusqu'à 14-15 µm, ajout simultanément du métal fondu B et du précipitant dans le système mixte en parallèle, réaction, et réalisation d'une séparation solide-liquide lorsque le D50 du cristal de carbonate de cobalt dopé à l'aluminium généré atteint jusqu'à 18-20 µm pour obtenir du carbonate de cobalt dopé à l'aluminium. Le carbonate de cobalt dopé à l'aluminium préparé par la méthode de préparation présente une taille uniforme, aucune petite particule et une distribution uniforme d'élément d'aluminium.
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN202211143499.2A CN115477331B (zh) | 2022-09-20 | 2022-09-20 | 一种掺铝碳酸钴及其制备方法 |
CN202211143499.2 | 2022-09-20 |
Publications (1)
Publication Number | Publication Date |
---|---|
WO2024060557A1 true WO2024060557A1 (fr) | 2024-03-28 |
Family
ID=84423473
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/CN2023/083440 WO2024060557A1 (fr) | 2022-09-20 | 2023-03-23 | Carbonate de cobalt dopé à l'aluminium et sa méthode de préparation |
Country Status (2)
Country | Link |
---|---|
CN (1) | CN115477331B (fr) |
WO (1) | WO2024060557A1 (fr) |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN115477331B (zh) * | 2022-09-20 | 2024-06-04 | 广东邦普循环科技有限公司 | 一种掺铝碳酸钴及其制备方法 |
Citations (10)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2003313030A (ja) * | 2002-04-23 | 2003-11-06 | Sumitomo Metal Mining Co Ltd | 高タップ密度塩基性炭酸コバルト粉及びその製造方法 |
CN108011101A (zh) * | 2017-11-28 | 2018-05-08 | 衢州华友钴新材料有限公司 | 一种大粒径均匀掺铝四氧化三钴的制备方法 |
CN108649219A (zh) * | 2018-05-14 | 2018-10-12 | 荆门市格林美新材料有限公司 | 一种大粒径掺铝四氧化三钴的制备方法 |
CN111056575A (zh) * | 2020-01-13 | 2020-04-24 | 衢州华友钴新材料有限公司 | 一种致密晶型小粒径球形碳酸钴的制备方法 |
CN111646519A (zh) * | 2020-07-17 | 2020-09-11 | 衢州华友钴新材料有限公司 | 一种掺铝四氧化三钴的制备方法 |
CN113636604A (zh) * | 2021-08-30 | 2021-11-12 | 衢州华友钴新材料有限公司 | 一种高掺铝小粒径碳酸钴颗粒的制备方法 |
CN113772745A (zh) * | 2021-09-01 | 2021-12-10 | 荆门市格林美新材料有限公司 | 一种铝均匀掺杂的大粒径四氧化三钴的制备方法 |
CN114702081A (zh) * | 2022-04-25 | 2022-07-05 | 广东邦普循环科技有限公司 | 镁钛共掺杂碳酸钴的制备方法及其应用 |
CN114940515A (zh) * | 2022-06-15 | 2022-08-26 | 荆门市格林美新材料有限公司 | 一种铝掺杂的碳酸钴及其制备方法和应用 |
CN115477331A (zh) * | 2022-09-20 | 2022-12-16 | 广东邦普循环科技有限公司 | 一种掺铝碳酸钴及其制备方法 |
Family Cites Families (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP2740534A1 (fr) * | 2012-12-04 | 2014-06-11 | Total Raffinage Marketing | Particules de type envelope-noyau avec une activité catalytique et procédé de préparation. Le procédé de préparation d'un catalyseur Fischer-Tropsch à la base de cettes particules. |
CN110217832B (zh) * | 2019-04-23 | 2021-08-27 | 金川集团股份有限公司 | 一种大颗粒窄分布掺铝四氧化三钴的制备方法 |
CN113830839B (zh) * | 2021-08-18 | 2022-11-15 | 广东邦普循环科技有限公司 | 片状形貌掺铝碳酸钴的制备方法及其应用 |
CN113772746A (zh) * | 2021-09-01 | 2021-12-10 | 荆门市格林美新材料有限公司 | 一种高振实掺铝小粒径四氧化三钴的制备方法 |
-
2022
- 2022-09-20 CN CN202211143499.2A patent/CN115477331B/zh active Active
-
2023
- 2023-03-23 WO PCT/CN2023/083440 patent/WO2024060557A1/fr unknown
Patent Citations (10)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2003313030A (ja) * | 2002-04-23 | 2003-11-06 | Sumitomo Metal Mining Co Ltd | 高タップ密度塩基性炭酸コバルト粉及びその製造方法 |
CN108011101A (zh) * | 2017-11-28 | 2018-05-08 | 衢州华友钴新材料有限公司 | 一种大粒径均匀掺铝四氧化三钴的制备方法 |
CN108649219A (zh) * | 2018-05-14 | 2018-10-12 | 荆门市格林美新材料有限公司 | 一种大粒径掺铝四氧化三钴的制备方法 |
CN111056575A (zh) * | 2020-01-13 | 2020-04-24 | 衢州华友钴新材料有限公司 | 一种致密晶型小粒径球形碳酸钴的制备方法 |
CN111646519A (zh) * | 2020-07-17 | 2020-09-11 | 衢州华友钴新材料有限公司 | 一种掺铝四氧化三钴的制备方法 |
CN113636604A (zh) * | 2021-08-30 | 2021-11-12 | 衢州华友钴新材料有限公司 | 一种高掺铝小粒径碳酸钴颗粒的制备方法 |
CN113772745A (zh) * | 2021-09-01 | 2021-12-10 | 荆门市格林美新材料有限公司 | 一种铝均匀掺杂的大粒径四氧化三钴的制备方法 |
CN114702081A (zh) * | 2022-04-25 | 2022-07-05 | 广东邦普循环科技有限公司 | 镁钛共掺杂碳酸钴的制备方法及其应用 |
CN114940515A (zh) * | 2022-06-15 | 2022-08-26 | 荆门市格林美新材料有限公司 | 一种铝掺杂的碳酸钴及其制备方法和应用 |
CN115477331A (zh) * | 2022-09-20 | 2022-12-16 | 广东邦普循环科技有限公司 | 一种掺铝碳酸钴及其制备方法 |
Also Published As
Publication number | Publication date |
---|---|
CN115477331B (zh) | 2024-06-04 |
CN115477331A (zh) | 2022-12-16 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN111180690B (zh) | 改性镍钴铝酸锂正极材料及其制备方法与应用 | |
CN110048118B (zh) | 一种高镍型镍钴锰酸锂单晶前驱体及其制备方法和高镍型镍钴锰酸锂单晶正极材料 | |
US11345609B2 (en) | High voltage lithium nickel cobalt manganese oxide precursor, method for making the same, and high voltage lithium nickel cobalt manganese oxide cathode material | |
CN110534719B (zh) | 一种掺铝镁镍锰球形四氧化三钴的制备方法 | |
CN112531158B (zh) | 一种高镍三元单晶材料及其制备方法 | |
CN106784790B (zh) | 一种镍钴锰酸锂三元正极材料的制备方法 | |
CN112226820B (zh) | 一种单晶镍钴锰酸锂前驱体及其制备方法和单晶镍钴锰酸锂 | |
WO2023207281A1 (fr) | Méthode de préparation de carbonate de cobalt co-dopé au magnésium-titane et son utilisation | |
CN111180724B (zh) | 一种三元单晶正极材料的制备方法 | |
CN113644272B (zh) | 一种铈铋复合氧化物掺杂锂离子电池正极材料及其制备方法 | |
WO2024066892A1 (fr) | Précurseur d'oxyde riche en manganèse, son procédé de préparation et son utilisation | |
CN109301189B (zh) | 一种类单晶型高镍多元材料的制备方法 | |
WO2024040903A1 (fr) | Méthode de préparation de phosphate de ferromanganèse par coprécipitation et son utilisation | |
WO2024040909A1 (fr) | Particules de carbonate de cobalt dopées à l'aluminium, leur méthode de préparation et leur utilisation | |
WO2022151977A1 (fr) | Procédé de préparation destiné à un matériau d'électrode positive à base d'oxyde de cobalt-lithium nanométrique et utilisation associée | |
WO2023179247A1 (fr) | Précurseur ternaire à ultra-haute teneur en nickel et procédé de préparation associé | |
WO2023179048A1 (fr) | Matériau d'électrode positive en oxyde de cobalt-lithium co-dopé au fluor-aluminium et son procédé de préparation | |
CN108987740B (zh) | 镍钴铝酸锂正极材料、其制备方法及应用其的电池 | |
CN104157843B (zh) | 一种高镍锂离子电池正极材料及其制备方法及包含其的锂离子电池 | |
WO2023207247A1 (fr) | Particule d'oxyde de cobalt sphérique poreuse et procédé pour la préparer | |
CN114436345A (zh) | 一种锂离子电池三元正极材料及其制备方法 | |
CN112928246A (zh) | 一种复合材料、其制备方法及应用 | |
WO2024178793A1 (fr) | Précurseur d'électrode positive de batterie sodium-ion modifiée, sa méthode de préparation et son utilisation | |
WO2024060557A1 (fr) | Carbonate de cobalt dopé à l'aluminium et sa méthode de préparation | |
CN109360948B (zh) | 一种类单晶型高镍多元材料前驱体 |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
121 | Ep: the epo has been informed by wipo that ep was designated in this application |
Ref document number: 23866856 Country of ref document: EP Kind code of ref document: A1 |