WO2023138220A1 - 具有大通道的正极材料前驱体的制备方法及其应用 - Google Patents

具有大通道的正极材料前驱体的制备方法及其应用 Download PDF

Info

Publication number
WO2023138220A1
WO2023138220A1 PCT/CN2022/135660 CN2022135660W WO2023138220A1 WO 2023138220 A1 WO2023138220 A1 WO 2023138220A1 CN 2022135660 W CN2022135660 W CN 2022135660W WO 2023138220 A1 WO2023138220 A1 WO 2023138220A1
Authority
WO
WIPO (PCT)
Prior art keywords
preparation
sodium
cobalt
nickel
concentration
Prior art date
Application number
PCT/CN2022/135660
Other languages
English (en)
French (fr)
Other versions
WO2023138220A9 (zh
Inventor
余海军
谢英豪
李爱霞
张学梅
李长东
Original Assignee
广东邦普循环科技有限公司
湖南邦普循环科技有限公司
湖南邦普汽车循环有限公司
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by 广东邦普循环科技有限公司, 湖南邦普循环科技有限公司, 湖南邦普汽车循环有限公司 filed Critical 广东邦普循环科技有限公司
Priority to GB2314805.9A priority Critical patent/GB2619865A/en
Publication of WO2023138220A1 publication Critical patent/WO2023138220A1/zh
Publication of WO2023138220A9 publication Critical patent/WO2023138220A9/zh

Links

Images

Classifications

    • C—CHEMISTRY; METALLURGY
    • C01—INORGANIC CHEMISTRY
    • C01G—COMPOUNDS CONTAINING METALS NOT COVERED BY SUBCLASSES C01D OR C01F
    • C01G53/00—Compounds of nickel
    • C—CHEMISTRY; METALLURGY
    • C01—INORGANIC CHEMISTRY
    • C01G—COMPOUNDS CONTAINING METALS NOT COVERED BY SUBCLASSES C01D OR C01F
    • C01G53/00—Compounds of nickel
    • C01G53/40—Nickelates
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M10/00—Secondary cells; Manufacture thereof
    • H01M10/05—Accumulators with non-aqueous electrolyte
    • H01M10/052—Li-accumulators
    • H01M10/0525—Rocking-chair batteries, i.e. batteries with lithium insertion or intercalation in both electrodes; Lithium-ion batteries
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00—Electrodes
    • H01M4/02—Electrodes composed of, or comprising, active material
    • H01M4/36—Selection of substances as active materials, active masses, active liquids
    • H01M4/48—Selection of substances as active materials, active masses, active liquids of inorganic oxides or hydroxides
    • H01M4/50—Selection of substances as active materials, active masses, active liquids of inorganic oxides or hydroxides of manganese
    • H01M4/505—Selection of substances as active materials, active masses, active liquids of inorganic oxides or hydroxides of manganese of mixed oxides or hydroxides containing manganese for inserting or intercalating light metals, e.g. LiMn2O4 or LiMn2OxFy
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00—Electrodes
    • H01M4/02—Electrodes composed of, or comprising, active material
    • H01M4/36—Selection of substances as active materials, active masses, active liquids
    • H01M4/48—Selection of substances as active materials, active masses, active liquids of inorganic oxides or hydroxides
    • H01M4/52—Selection of substances as active materials, active masses, active liquids of inorganic oxides or hydroxides of nickel, cobalt or iron
    • H01M4/525—Selection of substances as active materials, active masses, active liquids of inorganic oxides or hydroxides of nickel, cobalt or iron of mixed oxides or hydroxides containing iron, cobalt or nickel for inserting or intercalating light metals, e.g. LiNiO2, LiCoO2 or LiCoOxFy
    • C—CHEMISTRY; METALLURGY
    • C01—INORGANIC CHEMISTRY
    • C01P—INDEXING SCHEME RELATING TO STRUCTURAL AND PHYSICAL ASPECTS OF SOLID INORGANIC COMPOUNDS
    • C01P2004/00—Particle morphology
    • C01P2004/30—Particle morphology extending in three dimensions
    • C01P2004/32—Spheres
    • 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
    • C01P2006/00—Physical properties of inorganic compounds
    • C01P2006/40—Electric properties
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00—Electrodes
    • H01M4/02—Electrodes composed of, or comprising, active material
    • H01M2004/026—Electrodes composed of, or comprising, active material characterised by the polarity
    • H01M2004/028—Positive electrodes
    • 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 application belongs to the technical field of cathode materials for lithium-ion batteries, and in particular relates to a method for preparing a precursor of cathode materials for lithium-ion batteries with large channels.
  • Lithium-ion batteries are widely used in portable electronic products, electric vehicles, and energy storage systems due to their many advantages such as high energy density, low self-discharge, no memory effect, long cycle life, and low environmental pollution.
  • High-performance batteries such as high energy density and the continuous popularization of electric vehicles
  • battery cathode materials has shown a rapid growth trend. Due to the characteristics of high energy density, relatively low cost, and excellent cycle performance, ternary cathode materials are the most potential and most promising materials among the currently mass-produced cathode materials.
  • the positive and negative electrode materials are required to have structural stability during the conduction process and the charging and discharging process. They must not only have ion channels to ensure the smooth migration of Li ions, but also have the ability to deintercalate Li ions to prevent hole collapse, especially when the battery continues to charge and discharge. After continuous heat generation and high temperature conditions.
  • Chemical stability When the temperature and humidity in the battery change, the components of the electrode material still maintain a good shape without affecting the intercalation, deintercalation and transportation of Li ions. Therefore, it is of great significance to prepare lithium battery cathode materials with high physical and chemical stability.
  • NCM lithium-ion ternary material
  • the related art discloses a preparation method of LiV 3 O 8 and LiNi 0.4 Co 0.2 Mn 0.4 O 2 blended modified lithium battery cathode material.
  • the positive electrode materials LiV 3 O 8 and LiNi 0.4 Co 0.2 Mn 0.4 O 2 were mixed in a three-dimensional cone mixer according to the mass ratio of 3:7, pre-sintered at 480-500°C for 2h, sintered at 650-675°C for 4h, sintered at 800-825°C for 6h, and kept for 8h; then naturally cooled in the furnace, crushed, and finally the blend material (LiV 3 O 8 and LiNi 0. 4 Co 0.2 Mn 0.4 O 2 ).
  • a positive electrode material with a high compacted density can be obtained, and the capacity performance can be effectively improved after testing.
  • it uses simple physical mixing, on the one hand, it will destroy the matrix structure of the ternary material, on the other hand, there is no chemical bond between the mixed components, which is not conducive to the construction of lithium ion channels.
  • the present application proposes a preparation method and application of a cathode material precursor with large channels.
  • the precursor prepared by this method has a large ion channel, which is beneficial to the improvement of the performance of the subsequent sintered cathode material.
  • a method for preparing a positive electrode material precursor with a large channel comprising the following steps:
  • S1 Mix sodium hexanitrocobaltate aqueous solution, nickel-manganese mixed salt solution, oxalic acid solution and ammonia water for reaction, control the reaction temperature, pH and ammonia concentration, and when the particle size of the reaction material reaches the target value, separate the reaction material from solid to liquid to obtain a solid material;
  • step S1 the preparation of the aqueous solution of sodium hexanitrocobaltate is as follows: dissolving soluble cobalt salts and sodium nitrite in water, and then adding an oxidizing agent and acetic acid to obtain the aqueous solution of sodium hexanitrocobaltate.
  • the soluble cobalt salt is at least one of nitrate, chloride or sulfate.
  • the reaction equation that adopts cobalt salt and sodium nitrite to prepare sodium hexanitrocobaltate is as follows (oxidant is example with hydrogen peroxide and oxygen):
  • step S1 the molar ratio of cobalt ions in the soluble cobalt salt to sodium ions in the sodium nitrite is 1:(6-8). Further, the molar ratio of acetic acid to cobalt ions in the soluble cobalt salt is (1-1.5):1; the molar concentration of cobalt in the aqueous sodium hexanitrocobaltate solution is 0.01-0.2mol/L.
  • the oxidizing agent is at least one of hydrogen peroxide, oxygen or air.
  • step S1 the total molar concentration of metal ions in the nickel-manganese mixed salt solution is 0.01-2.0 mol/L.
  • the nickel-manganese mixed salt solution is prepared by dissolving soluble salts of nickel and manganese in water, and the soluble salts of nickel and manganese are at least one of nitrate, chloride or sulfate.
  • step S1 the concentration of the oxalic acid is 0.01-0.5 mol/L; the concentration of the ammonia water is 1.0-6.0 mol/L.
  • step S1 the temperature of the reaction is 45-65° C., the pH is 8.1-8.3, and the ammonia concentration is 2.0-5.0 g/L.
  • the molar ratio of the metal elements in the precursor is controlled by controlling the flow rates of the sodium hexanitrocobaltate aqueous solution and the nickel-manganese mixed salt solution.
  • step S1 the particle size reaches a D50 of 2.0-15.0 ⁇ m.
  • step S2 the temperature of the calcination is 200-250°C. Further, the calcination time is 1-4h.
  • the calcining atmosphere is air or oxygen.
  • step S3 the liquid-solid ratio of the water to the calcined material is 5000-8000 L/t.
  • step S3 the soaking time is 1-2 hours.
  • the application also provides the application of the preparation method in the preparation of lithium ion batteries.
  • This application is to prepare anode materials for large-channel lithium-ion batteries, and improve the lithium-ion deintercalation ability of the material during charging and discharging.
  • a large-channel ternary precursor is prepared.
  • the precursor is co-precipitated with nickel-cobalt-manganese and sodium ammonium, and then the sodium ammonium is removed after sintering. Since the radius of the sodium ion is larger than that of the lithium ion, with the removal of the sodium ammonium, a larger ion channel is left in the nickel-cobalt-manganese precursor skeleton, thereby facilitating the deintercalation of lithium ions in the chemically sintered positive electrode material.
  • nickel-cobalt-manganese-sodium-ammonium co-precipitation is made, and the reaction equation is as follows:
  • Ni 2+ +C 2 O 4 2- NiC 2 O 4 ⁇
  • a co-crystal is formed.
  • the ammonium, nitro, and oxalate groups are decomposed into gases to form a nickel-cobalt-manganese-sodium oxide calcined material.
  • the calcined material is soaked in pure water to remove sodium, it is dried, sieved, and demagnetized to obtain a lithium-ion battery cathode material precursor with large channels.
  • FIG. 1 is a SEM image of the precursor of the lithium-ion battery anode material with large channels prepared in Example 1 of the present application.
  • a lithium-ion battery cathode material precursor with a large channel is prepared, and the specific process is as follows:
  • Step 1 dissolving cobalt nitrate and sodium nitrite in pure water according to the molar ratio of 1:6, then adding hydrogen peroxide and acetic acid in an equimolar amount to cobalt ions, to prepare an aqueous solution of sodium hexanitrocobaltate with a cobalt molar concentration of 0.01mol/L;
  • Step 2 select nickel nitrate and manganese nitrate as raw material according to molar ratio 8:1, prepare the nickel-manganese mixed salt solution that the total molar concentration of metal ions is 0.09mol/L;
  • Step 3 preparation concentration is the oxalic acid solution of 0.01mol/L as precipitation agent, preparation concentration is the ammoniacal liquor of 1.0mol/L as complexing agent;
  • Step 4 add pure water to the reactor until it covers the stirring paddle at the bottom, and start stirring;
  • Step 5 add the sodium hexanitrocobaltate aqueous solution prepared in step 1, the nickel-manganese mixed salt solution prepared in step 2, the oxalic acid solution prepared in step 3, and ammonia water into the reactor for reaction. :1;
  • Step 6 when it is detected that the particle size D50 of the material in the reactor reaches 10.5 ⁇ m, stop feeding;
  • Step 7 performing solid-liquid separation on the materials in the kettle to obtain solid materials
  • Step 8 calcining the solid material under an oxygen atmosphere, the calcination temperature is 200° C., and the calcination time is 2 hours, to obtain the calcined material;
  • Step 9 according to the ratio of pure water to calcined material is 8000L/t, soak the calcined material in pure water for 1 hour, separate solid and liquid to obtain wet material, and wash the wet material with pure water;
  • step 10 the wet material is dried, sieved, and demagnetized to obtain a lithium-ion battery cathode material precursor with large channels.
  • Figure 1 is the SEM image of the lithium-ion battery cathode material precursor with large channels prepared in this example. It can be seen from the figure that the shape of the precursor is spherical or spherical particles, which can be used as sintering raw materials for subsequent ternary cathode materials.
  • a lithium-ion battery cathode material precursor with a large channel is prepared, and the specific process is as follows:
  • Step 1 dissolving cobalt sulfate and sodium nitrite in pure water according to the molar ratio of 1:7, then adding hydrogen peroxide and acetic acid equal to the molar amount of cobalt ions to prepare an aqueous solution of sodium hexanitrocobaltate with a cobalt molar concentration of 0.1mol/L;
  • Step 2 selecting nickel sulfate and manganese sulfate as raw materials in a molar ratio of 5:3, preparing a nickel-manganese mixed salt solution with a total molar concentration of metal ions of 0.4mol/L;
  • Step 3 preparation concentration is the oxalic acid solution of 0.1mol/L as precipitation agent, preparation concentration is the ammoniacal liquor of 3.0mol/L as complexing agent;
  • Step 4 add pure water to the reactor until it covers the stirring paddle at the bottom, and start stirring;
  • Step 5 the sodium hexanitrocobaltate aqueous solution prepared in step 1, the nickel-manganese mixed salt solution prepared in step 2, the oxalic acid solution prepared in step 3 and ammonia water are added to the reaction kettle in parallel for reaction, the reaction temperature in the control kettle is 55° C., the pH is 8.1-8.3, the ammonia concentration is 3.0 g/L, and the flow ratio of the sodium hexanitrocobaltate aqueous solution and the nickel-manganese mixed salt solution is controlled to be 1:1.
  • the ratio of oxalic acid to nickel-manganese total metal ions in the oxalic acid solution used is 1:1;
  • Step 6 when it is detected that the D50 of the material in the reactor reaches 5.0 ⁇ m, stop feeding;
  • Step 7 performing solid-liquid separation on the materials in the kettle to obtain solid materials
  • Step 8 calcining the solid material in an oxygen atmosphere, the calcination temperature is 250° C., and the calcination time is 3 hours, to obtain the calcined material;
  • Step 9 according to the ratio of pure water to calcined material is 6000L/t, soak the calcined material in pure water for 2 hours, separate solid and liquid to obtain wet material, and wash the wet material with pure water;
  • step 10 the wet material is dried, sieved, and demagnetized to obtain a lithium-ion battery cathode material precursor with large channels.
  • the chemical formula of the precursor is Ni 0.5 Co 0.2 Mn 0.3 O, and the shape is spherical or quasi-spherical particles, which can be used as sintering raw materials for subsequent ternary cathode materials.
  • a lithium-ion battery cathode material precursor with a large channel is prepared, and the specific process is as follows:
  • Step 1 dissolving cobalt chloride and sodium nitrite in pure water according to the molar ratio of 1:8, then adding hydrogen peroxide and acetic acid equal to the molar amount of cobalt ions to prepare an aqueous solution of sodium hexanitrocobaltate with a cobalt molar concentration of 0.2mol/L;
  • Step 2 selecting nickel chloride and manganese chloride as raw material in a molar ratio of 6:2, preparing the nickel-manganese mixed salt solution of nickel-manganese with a total molar concentration of metal ions of 0.8mol/L;
  • Step 3 preparation concentration is the oxalic acid solution of 0.5mol/L as precipitation agent, preparation concentration is the ammoniacal liquor of 6.0mol/L as complexing agent;
  • Step 4 add pure water to the reactor until it covers the stirring paddle at the bottom, and start stirring;
  • Step 5 Add the sodium hexanitrocobaltate aqueous solution prepared in step 1, the nickel-manganese mixed salt solution prepared in step 2, the oxalic acid solution prepared in step 3, and ammonia water into the reactor for reaction. 1:1;
  • Step 6 when it is detected that the D50 of the material in the reactor reaches 15.0 ⁇ m, stop feeding;
  • Step 7 performing solid-liquid separation on the materials in the kettle to obtain solid materials
  • Step 8 calcining the solid material under an oxygen atmosphere, the calcination temperature is 200° C., and the calcination time is 4 hours, to obtain the calcined material;
  • Step 9 According to the ratio of pure water to calcined material being 5000L/t, soak the calcined material in pure water for 2 hours, separate solid and liquid to obtain wet material, and wash the wet material with pure water;
  • step 10 the wet material is dried, sieved, and demagnetized to obtain a lithium-ion battery cathode material precursor with large channels.
  • the chemical formula of the precursor is Ni 0.6 Co 0.2 Mn 0.2 O, and the shape is spherical or spherical-like particles, which can be used as the sintering raw material of the subsequent ternary cathode material.
  • Example 2 a precursor Ni 0.8 Co 0.1 Mn 0.1 O was prepared. The difference from Example 1 was that an aqueous solution of sodium hexanitrocobaltate was not prepared.
  • the specific process was as follows:
  • Step 1 select nickel nitrate, manganese nitrate, cobalt nitrate as raw material according to molar ratio 8:1:1, prepare the nickel-cobalt-manganese mixed salt solution that the total molar concentration of metal ions is 0.1mol/L;
  • Step 2 preparation concentration is the oxalic acid solution of 0.01mol/L as precipitation agent, preparation concentration is the ammoniacal liquor of 1.0mol/L as complexing agent;
  • Step 3 add pure water to the reactor until it covers the stirring paddle at the bottom, and start stirring;
  • Step 4 adding the oxalic acid solution prepared in step 1 and the oxalic acid solution prepared in step 2 and ammonia water into the reaction kettle in parallel for reaction, controlling the reaction temperature in the kettle to be 45° C., the pH to be 8.1-8.3, and the ammonia concentration to be 2.0 g/L.
  • the ratio of oxalic acid to nickel-manganese total metal ions in the oxalic acid solution used is 1:1;
  • Step 5 when it is detected that the particle size D50 of the material in the reactor reaches 10.5 ⁇ m, stop feeding;
  • Step 6 performing solid-liquid separation on the materials in the kettle to obtain solid materials
  • Step 7 calcining the solid material in an oxygen atmosphere, the calcination temperature is 200°C, and the calcination time is 2h, to obtain the calcined material;
  • Step 8 after sieving and demagnetizing the calcined material, the precursor Ni 0.8 Co 0.1 Mn 0.1 O is obtained.
  • Step 1 select nickel sulfate, manganese sulfate, cobalt sulfate as raw material according to molar ratio 5:2:3, prepare the nickel-cobalt-manganese mixed salt solution that the total molar concentration of metal ions is 0.5mol/L;
  • Step 2 preparing an oxalic acid solution with a concentration of 0.1mol/L as a precipitant, and preparing a concentration of 3.0mol/L ammonia as a complexing agent;
  • Step 3 add pure water to the reactor until it covers the stirring paddle at the bottom, and start stirring;
  • Step 4 adding the nickel-cobalt-manganese mixed salt solution prepared in step 1, the sodium hydroxide solution prepared in step 2, and ammonia water to the reactor for reaction, controlling the reaction temperature in the reactor to be 55°C, the pH to be 8.1-8.3, and the ammonia concentration to be 3.0g/L;
  • Step 5 when it is detected that the particle size D50 of the material in the reactor reaches 5.0 ⁇ m, stop feeding;
  • Step 6 performing solid-liquid separation on the materials in the kettle to obtain solid materials
  • Step 7 calcining the solid material under an oxygen atmosphere, the calcination temperature is 250° C., and the calcination time is 3 hours, to obtain the calcined material;
  • Step 8 after sieving and demagnetizing the calcined material, the precursor Ni 0.5 Co 0.2 Mn 0.3 O is obtained.
  • Step 1 select nickel chloride, manganese chloride, cobalt chloride as raw material according to molar ratio 6:2:2, prepare the nickel-cobalt-manganese mixed salt solution that the total molar concentration of metal ions is 1.0mol/L;
  • Step 2 preparation concentration is the oxalic acid solution of 0.5mol/L as precipitation agent, preparation concentration is the ammoniacal liquor of 6.0mol/L as complexing agent;
  • Step 3 add pure water to the reactor until it covers the stirring paddle at the bottom, and start stirring;
  • Step 4 adding the nickel-cobalt-manganese mixed salt solution prepared in step 1, the sodium hydroxide solution prepared in step 2, and ammonia water into the reaction kettle in parallel for reaction, controlling the reaction temperature in the kettle to be 65° C., the pH to be 8.1-8.3, and the ammonia concentration to be 5.0 g/L;
  • Step 5 when it is detected that the D50 of the material in the reactor reaches 15.0 ⁇ m, stop feeding;
  • Step 6 performing solid-liquid separation on the materials in the kettle to obtain solid materials
  • Step 7 calcining the solid material under an oxygen atmosphere, the calcination temperature is 200° C., and the calcination time is 4 hours, to obtain the calcined material;
  • Step 8 after sieving and demagnetizing the calcined material, the precursor Ni 0.6 Co 0.2 Mn 0.2 O is obtained.
  • Examples 1-3 and Comparative Examples 1-3 were respectively sintered with lithium sources to prepare ternary cathode materials, and the electrochemical performance tests were carried out on the obtained cathode materials. The results are shown in Table 1.
  • the examples have better cycle performance and rate performance. This is because the precursors of the examples co-precipitate with sodium ammonium, and after sintering, the ammonium, nitro and oxalate groups are decomposed into gases to form the oxide calcined material of nickel-cobalt-manganese-sodium. After the calcined material is soaked in pure water to remove sodium, since the radius of the sodium ion is larger than that of lithium ions, a larger ion channel is left in the nickel-cobalt-manganese precursor framework, which widens the lithium ion diffusion channel, thereby facilitating the chemical process. The deintercalation of lithium ions in the sintered cathode material results in a more stable crystal structure, which significantly improves the rate performance and cycle performance of the material.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Electrochemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Inorganic Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Organic Chemistry (AREA)
  • Materials Engineering (AREA)
  • Manufacturing & Machinery (AREA)
  • Battery Electrode And Active Subsutance (AREA)
  • Inorganic Compounds Of Heavy Metals (AREA)

Abstract

本申请提供了一种具有大通道的正极材料前驱体的制备方法及其应用，包括将六硝基合钴酸钠水溶液、镍锰混合盐溶液、草酸溶液和氨水混合反应，将固体料进行煅烧，将煅烧料浸泡于水中，即得具有大通道的正极材料前驱体。本申请通过镍钴锰与钠铵共沉淀，经烧结后再脱除钠铵，由于钠离子的半径大于锂离子，在镍钴锰前驱体骨架中，留下了较大的离子通道，从而利于化学烧结的正极材料锂离子的脱嵌，拓宽了锂离子扩散通道，显著提升材料的倍率性能和循环性能。

Description

具有大通道的正极材料前驱体的制备方法及其应用 技术领域
本申请属于锂离子电池正极材料技术领域，具体涉及一种具有大通道的锂离子电池正极材料前驱体的制备方法。
背景技术
锂离子电池因其能量密度高、自放电小、无记忆效应、循环寿命长、环境污染小等众多优点而被广泛应用在便携式电子产品、电动汽车和储能***等领域。当今，随着市场对高能量密度等高性能电池需求的不断增长以及电动汽车的不断普及，电池正极材料的市场需求已呈现出快速增长态势。三元正极材料由于能量密度高、成本相对较低、循环性能优异等特点，是目前量产的正极材料中潜力最大最有发展前景的一种材料。
由于电池中Li离子的不断嵌入和脱嵌，这就要求正极材料具有较强的物理稳定性与化学稳定性。物理稳定性：要求正极材料与负极材料在导电过程与充放电过程中具有结构稳定，既要具有保证Li离子的顺利迁移的离子通道，又要具备Li离子脱嵌防止空穴塌陷的能力，尤其是当电池持续充放电后产热高温的情况下。化学稳定性：当随着电池内温度与湿度的变化，电极材料的各组分依然保持有较好的形状，而不会影响到Li离子嵌入、脱嵌和运输。因此，制备出具有物理稳定性与化学稳定性高的锂电池正极材料具有重要的意义。
目前三元锂离子电池中提高循环性能的方法较多，如对锂离子三元材料(NCM)正极材料进行掺杂和包覆改进以减缓正极材料在循环过程中晶体结构的恶化。适当的掺杂和包覆材料虽然可以减少正极活性物质与电解液的接触，防止正极材料的溶解，同时还能抑制高电位下电解液的分解，但是不能够改变材料的离子通道，同时，包覆所用的材料多不具备容纳锂离子的能力，过多的包覆反而会降低材料的比容量。
相关技术公开了一种LiV 3O 8和LiNi 0.4Co 0.2Mn 0.4O 2共混改性锂电池正极材料 的制备方法。通过将正极材料LiV 3O 8和LiNi 0.4Co 0.2Mn 0.4O 2按照3:7的质量比在三维锥混机内混合，在480-500℃预烧2h、650-675℃烧结4h、在800-825℃烧结6h，并保温8h；后随炉自然冷却，破碎，最后制得共混材料(LiV 3O 8和LiNi 0.4Co 0.2Mn 0.4O 2)。通过三元材料与LiV 3O 8的共混改性，能够获得高压实密度的正极材料，经检测，可以有效提高容量性能。然而，其采用简单的物理混合，一方面会破坏三元材料基体结构，另一方面混合组分间无化学键产生不利于锂离子通道的构建。
除此之外，三元锂离子电池正极材料的性能60％取决于其前驱体的性能，而目前针对前驱体的合成去提高材料的性能的研究较少。
发明内容
以下是对本文详细描述的主题的概述。本概述并非是为了限制权利要求的保护范围。
本申请提出一种具有大通道的正极材料前驱体的制备方法及其应用，该方法制备得到的前驱体具有较大的离子通道，利于后续烧结正极材料性能的提高。
根据本申请的一个方面，提出了一种具有大通道的正极材料前驱体的制备方法，包括以下步骤：
S1：将六硝基合钴酸钠水溶液、镍锰混合盐溶液、草酸溶液和氨水混合进行反应，控制反应温度、pH和氨浓度，当反应物料的粒度达到目标值，将反应物料进行固液分离得到固体料；
S2：将所述固体料进行煅烧，得到煅烧料；
S3：将所述煅烧料浸泡于水中，再分离出固相，即得所述具有大通道的正极材料前驱体。
在本申请的一些实施方式中，步骤S1中，所述六硝基合钴酸钠水溶液的配制如下：将钴的可溶性盐与亚硝酸钠用水溶解，再加入氧化剂和乙酸，得到所述六硝基合钴酸钠水溶液。进一步地，所述钴的可溶性盐为硝酸盐、氯化盐或硫酸盐中的至少一种。采用钴盐与亚硝酸钠制备六硝基合钴酸钠的反应方程式 如下(氧化剂以双氧水和氧气为例)：
24NaNO 2+4Co(NO 3) 2+2H 2O 2+4HAc＝4Na 3[Co(NO 2) 6]+8NaNO 3+4NaAc+4H 2O；
24NaNO 2+4Co(NO 3) 2+O 2+4HAc＝4Na 3[Co(NO 2) 6]+8NaNO 3+4NaAc+2H 2O。
在本申请的一些实施方式中，步骤S1中，所述钴的可溶性盐中钴离子与所述亚硝酸钠中钠离子的摩尔比为1：(6-8)。进一步地，所述乙酸与所述钴的可溶性盐中钴离子的摩尔比为(1-1.5)：1；所述六硝基合钴酸钠水溶液中钴的摩尔浓度为0.01-0.2mol/L。
在本申请的一些实施方式中，步骤S1中，所述氧化剂为双氧水、氧气或空气中的至少一种。
在本申请的一些实施方式中，步骤S1中，所述镍锰混合盐溶液中金属离子总摩尔浓度为0.01-2.0mol/L。
在本申请的一些实施方式中，步骤S1中，所述镍锰混合盐溶液由镍、锰的可溶性盐溶于水配制得到，镍、锰的可溶性盐为硝酸盐、氯化盐或硫酸盐中的至少一种。
在本申请的一些实施方式中，步骤S1中，所述草酸的浓度为0.01-0.5mol/L；所述氨水的浓度为1.0-6.0mol/L。
在本申请的一些实施方式中，步骤S1中，所述反应的温度为45-65℃，pH为8.1-8.3，氨浓度为2.0-5.0g/L。通过控制六硝基合钴酸钠水溶液和镍锰混合盐溶液的加入流量，来控制前驱体中的金属元素的摩尔比。
在本申请的一些实施方式中，步骤S1中，所述粒度达到D50为2.0-15.0μm。
在本申请的一些实施方式中，步骤S2中，所述煅烧的温度为200-250℃。进一步地，所述煅烧的时间为1-4h。煅烧的气氛为空气或氧气。
在本申请的一些实施方式中，步骤S3中，所述水与所述煅烧料的液固比为5000-8000L/t。
在本申请的一些实施方式中，步骤S3中，所述浸泡的时间为1-2h。
本申请还提供所述的制备方法在制备锂离子电池中的应用。
根据本申请的一种优选的实施方式，至少具有以下有益效果：
1、本申请为制备大通道锂离子电池正极材料，提高材料在充放电时，锂离子的脱嵌能力，在前端工艺中，制备出大通道的三元前驱体，该前驱体通过镍钴锰与钠铵共沉淀，经烧结后再脱除钠铵，由于钠离子的半径大于锂离子，随着钠铵的脱除，在镍钴锰前驱体骨架中，留下了较大的离子通道，从而利于化学烧结的正极材料锂离子的脱嵌。在共沉淀时，使镍钴锰钠铵共沉淀，反应方程式如下：
Na 3[Co(NO 2) 6]+2NH 4 +＝(NH 4) 2Na[Co(NO 2) 6]↓+2Na +
Ni 2++C 2O 4 2-＝NiC 2O 4↓
Mn 2++C 2O 4 2-＝MnC 2O 4↓
通过共沉淀，形成了共晶体，在进一步烧结，使其中的铵根、硝基以及草酸根分解为气体，形成镍钴锰钠的氧化物煅烧料，煅烧料在纯水中浸泡去除钠后，再经干燥、过筛、除磁后即得到具有大通道的锂离子电池正极材料前驱体。
2、通过拓宽锂离子扩散通道，减小了Li/Ni混排程度，得到更稳定的晶体结构，有效抑制了有害相转变的发生，显著提升了材料的倍率性能和循环性能。
在阅读并理解了附图和详细描述后，可以明白其他方面。
附图说明
附图用来提供对本文技术方案的进一步理解，并且构成说明书的一部分，与本申请的实施例一起用于解释本文的技术方案，并不构成对本文技术方案的限制。下面结合附图和实施例对本申请做进一步的说明，其中：
图1为本申请实施例1制备的具有大通道的锂离子电池正极材料前驱体的SEM图。
具体实施方式
以下将结合实施例对本申请的构思及产生的技术效果进行清楚、完整地描述，以充分地理解本申请的目的、特征和效果。显然，所描述的实施例只是本申请的一部分实施例，而不是全部实施例，基于本申请的实施例，本领域的技术人 员在不付出创造性劳动的前提下所获得的其他实施例，均属于本申请保护的范围。
实施例1
本实施例制备了一种具有大通道的锂离子电池正极材料前驱体，具体过程为：
步骤1，将硝酸钴与亚硝酸钠按照摩尔比为1:6用纯水溶解，再加入过氧化氢、与钴离子等摩尔量的乙酸，配制成钴的摩尔浓度为0.01mol/L的六硝基合钴酸钠水溶液；
步骤2，按摩尔比8:1选用硝酸镍、硝酸锰为原料，配制金属离子总摩尔浓度为0.09mol/L的镍锰混合盐溶液；
步骤3，配制浓度为0.01mol/L的草酸溶液作为沉淀剂，配制浓度为1.0mol/L的氨水作为络合剂；
步骤4，向反应釜中加入纯水至漫过底层搅拌桨，启动搅拌；
步骤5，将步骤1配制的六硝基合钴酸钠水溶液、步骤2配制镍锰混合盐溶液、步骤3配制的草酸溶液和氨水并流加入到反应釜中进行反应，控制釜内反应温度为45℃，pH为8.1-8.3，氨浓度为2.0g/L，并控制六硝基合钴酸钠水溶液和镍锰混合盐溶液的流量比为1:1，所用草酸溶液中草酸与镍锰总金属离子之比为1:1；
步骤6，当检测到反应釜内物料的粒度D50达到10.5μm时，停止进料；
步骤7，将釜内物料进行固液分离，得到固体料；
步骤8，将固体料在氧气气氛下进行煅烧，煅烧温度为200℃，煅烧时间为2h，得到煅烧料；
步骤9，按照纯水与煅烧料之比为8000L/t，将煅烧料置于纯水中浸泡1h，固液分离，得到湿料，湿料用纯水洗涤；
步骤10，将湿料进行干燥、过筛、除磁后即得到具有大通道的锂离子电池正极材料前驱体。
该前驱体的化学式为Ni 0.8Co 0.1Mn 0.1O，图1为本实施例制备的具有大通道的 锂离子电池正极材料前驱体的SEM图，从图中可见，前驱体的形貌为球形或类球形颗粒，可用于后续三元正极材料的烧结原料使用。
实施例2
本实施例制备了一种具有大通道的锂离子电池正极材料前驱体，具体过程为：
步骤1，将硫酸钴与亚硝酸钠按照摩尔比为1:7用纯水溶解，再加入过氧化氢、与钴离子等摩尔量的乙酸，配制成钴的摩尔浓度为0.1mol/L的六硝基合钴酸钠水溶液；
步骤2，按摩尔比5:3选用硫酸镍、硫酸锰为原料，配制金属离子总摩尔浓度为0.4mol/L的镍锰混合盐溶液；
步骤3，配制浓度为0.1mol/L的草酸溶液作为沉淀剂，配制浓度为3.0mol/L的氨水作为络合剂；
步骤4，向反应釜中加入纯水至漫过底层搅拌桨，启动搅拌；
步骤5，将步骤1配制的六硝基合钴酸钠水溶液、步骤2配制的镍锰混合盐溶液、步骤3配制的草酸溶液和氨水并流加入到反应釜中进行反应，控制釜内反应温度为55℃，pH为8.1-8.3，氨浓度为3.0g/L，并控制六硝基合钴酸钠水溶液和镍锰混合盐溶液的流量比为1:1，所用草酸溶液中草酸与镍锰总金属离子之比为1:1；
步骤6，当检测到反应釜内物料的D50达到5.0μm时，停止进料；
步骤7，将釜内物料进行固液分离，得到固体料；
步骤8，将固体料在氧气气氛下进行煅烧，煅烧温度为250℃，煅烧时间为3h，得到煅烧料；
步骤9，按照纯水与煅烧料之比为6000L/t，将煅烧料置于纯水中浸泡2h，固液分离，得到湿料，湿料用纯水洗涤；
步骤10，将湿料进行干燥、过筛、除磁后即得到具有大通道的锂离子电池正极材料前驱体。
该前驱体的化学式为Ni 0.5Co 0.2Mn 0.3O，形貌为球形或类球形颗粒，可用于后 续三元正极材料的烧结原料使用。
实施例3
本实施例制备了一种具有大通道的锂离子电池正极材料前驱体，具体过程为：
步骤1，将氯化钴与亚硝酸钠按照摩尔比为1:8用纯水溶解，再加入过氧化氢、与钴离子等摩尔量的乙酸，配制成钴的摩尔浓度为0.2mol/L的六硝基合钴酸钠水溶液；
步骤2，按摩尔比6:2选用氯化镍、氯化锰为原料，配制金属离子总摩尔浓度为0.8mol/L的镍锰的镍锰混合盐溶液；
步骤3，配制浓度为0.5mol/L的草酸溶液作为沉淀剂，配制浓度为6.0mol/L的氨水作为络合剂；
步骤4，向反应釜中加入纯水至漫过底层搅拌桨，启动搅拌；
步骤5，将步骤1配制的六硝基合钴酸钠水溶液、步骤2配制的镍锰混合盐溶液、步骤3配制的草酸溶液和氨水并流加入到反应釜中进行反应，控制釜内反应温度为65℃，pH为8.1-8.3，氨浓度为5.0g/L，并通过控制六硝基合钴酸钠水溶液和镍锰混合盐溶液的流量比为1:1，所用草酸溶液中草酸与镍锰总金属离子之比为1:1；
步骤6，当检测到反应釜内物料的D50达到15.0μm时，停止进料；
步骤7，将釜内物料进行固液分离，得到固体料；
步骤8，将固体料在氧气气氛下进行煅烧，煅烧温度为200℃，煅烧时间为4h，得到煅烧料；
步骤9，按照纯水与煅烧料之比为5000L/t，将煅烧料置于纯水中浸泡2h，固液分离，得到湿料，湿料用纯水洗涤；
步骤10，将湿料进行干燥、过筛、除磁后即得到具有大通道的锂离子电池正极材料前驱体。
该前驱体的化学式为Ni 0.6Co 0.2Mn 0.2O，形貌为球形或类球形颗粒，可用于后续三元正极材料的烧结原料使用。
对比例1
本对比例制备了一种前驱体Ni 0.8Co 0.1Mn 0.1O，与实施例1的区别在于不制备六硝基合钴酸钠水溶液，具体过程为：
步骤1，按摩尔比8:1:1选用硝酸镍、硝酸锰、硝酸钴为原料，配制金属离子总摩尔浓度为0.1mol/L的镍钴锰混合盐溶液；
步骤2，配制浓度为0.01mol/L的草酸溶液作为沉淀剂，配制浓度为1.0mol/L的氨水作为络合剂；
步骤3，向反应釜中加入纯水至漫过底层搅拌桨，启动搅拌；
步骤4，将步骤1配制的、步骤2配制的草酸溶液和氨水并流加入到反应釜中进行反应，控制釜内反应温度为45℃，pH为8.1-8.3，氨浓度为2.0g/L，所用草酸溶液中草酸与镍锰总金属离子之比为1:1；
步骤5，当检测到反应釜内物料的粒度D50达到10.5μm时，停止进料；
步骤6，将釜内物料进行固液分离，得到固体料；
步骤7，将固体料在氧气气氛下进行煅烧，煅烧温度为200℃，煅烧时间为2h，得到煅烧料；
步骤8，将煅烧料进行过筛、除磁后即得前驱体Ni 0.8Co 0.1Mn 0.1O。
对比例2
本对比例制备了一种前驱体Ni 0.5Co 0.2Mn 0.3O，与实施例2的区别在于不制备六硝基合钴酸钠水溶液，具体过程为：
步骤1，按摩尔比5:2:3选用硫酸镍、硫酸锰、硫酸钴为原料，配制金属离子总摩尔浓度为0.5mol/L的镍钴锰混合盐溶液；
步骤2，，配制浓度为0.1mol/L的草酸溶液作为沉淀剂，配制浓度为3.0mol/L的氨水作为络合剂；
步骤3，向反应釜中加入纯水至漫过底层搅拌桨，启动搅拌；
步骤4，将步骤1配制镍钴锰混合盐溶液、步骤2配制的氢氧化钠溶液和氨 水并流加入到反应釜中进行反应，控制釜内反应温度为55℃，pH为8.1-8.3，氨浓度为3.0g/L；
步骤5，当检测到反应釜内物料的粒度D50达到5.0μm时，停止进料；
步骤6，将釜内物料进行固液分离，得到固体料；
步骤7，将固体料在氧气气氛下进行煅烧，煅烧温度为250℃，煅烧时间为3h，得到煅烧料；
步骤8，将煅烧料进行过筛、除磁后即得前驱体Ni 0.5Co 0.2Mn 0.3O。
对比例3
本对比例制备了一种前驱体Ni 0.6Co 0.2Mn 0.2O，与实施例3的区别在于不制备六硝基合钴酸钠水溶液，具体过程为：
步骤1，按摩尔比6:2:2选用氯化镍、氯化锰、氯化钴为原料，配制金属离子总摩尔浓度为1.0mol/L的镍钴锰混合盐溶液；
步骤2，配制浓度为0.5mol/L的草酸溶液作为沉淀剂，配制浓度为6.0mol/L的氨水作为络合剂；
步骤3，向反应釜中加入纯水至漫过底层搅拌桨，启动搅拌；
步骤4，将步骤1配制的镍钴锰混合盐溶液、步骤2配制的氢氧化钠溶液和氨水并流加入到反应釜中进行反应，控制釜内反应温度为65℃，pH为8.1-8.3，氨浓度为5.0g/L；
步骤5，当检测到反应釜内物料的D50达到15.0μm时，停止进料；
步骤6，将釜内物料进行固液分离，得到固体料；
步骤7，将固体料在氧气气氛下进行煅烧，煅烧温度为200℃，煅烧时间为4h，得到煅烧料；
步骤8，将煅烧料进行过筛、除磁后即得前驱体Ni 0.6Co 0.2Mn 0.2O。
试验例
将实施例1-3和对比例1-3所得前驱体材料分别与锂源烧结制备三元正极材 料，并对所得正极材料进行电化学性能测试，所得结果如表1所示。
表1 前驱体的电化学性能对比
Figure PCTCN2022135660-appb-000001
由表1可知，与对比例的前驱体相比，实施例具有较佳的循环性能和倍率性能，这是由于实施例的前驱体与钠铵共沉淀，烧结后使其中的铵根、硝基以及草酸根分解为气体，形成镍钴锰钠的氧化物煅烧料，煅烧料在纯水中浸泡去除钠后，由于钠离子的半径大于锂离子，在镍钴锰前驱体骨架中，留下了较大的离子通道，拓宽了锂离子扩散通道，从而利于化学烧结的正极材料锂离子的脱嵌，得到更稳定的晶体结构，显著提升了材料的倍率性能和循环性能。
上面结合附图对本申请实施例作了详细说明，但是本申请不限于上述实施例，在所属技术领域普通技术人员所具备的知识范围内，还可以在不脱离本申请宗旨的前提下作出各种变化。此外，在不冲突的情况下，本申请的实施例及实施例中的特征可以相互组合。

Claims (13)

  1. 一种具有大通道的正极材料前驱体的制备方法，其中，包括以下步骤：
    S1：将六硝基合钴酸钠水溶液、镍锰混合盐溶液、草酸溶液和氨水混合进行反应，控制反应温度、pH和氨浓度，当反应物料的粒度达到目标值，将反应物料进行固液分离得到固体料；
    S2：将所述固体料进行煅烧，得到煅烧料；
    S3：将所述煅烧料浸泡于水中，再分离出固相，即得所述具有大通道的正极材料前驱体。
  2. 根据权利要求1所述的制备方法，其中，步骤S1中，所述六硝基合钴酸钠水溶液的配制如下：将钴的可溶性盐与亚硝酸钠用水溶解，再加入氧化剂和乙酸，得到所述六硝基合钴酸钠水溶液。
  3. 根据权利要求2所述的制备方法，其中，步骤S1中，所述钴的可溶性盐中钴离子与所述亚硝酸钠中钠离子的摩尔比为1：(6-8)。
  4. 根据权利要求2所述的制备方法，其中，步骤S1中，所述氧化剂为双氧水、氧气或空气中的至少一种。
  5. 根据权利要求2所述的制备方法，其中，步骤S1中，所述乙酸与所述钴的可溶性盐中钴离子的摩尔比为(1-1.5)：1。
  6. 根据权利要求2所述的制备方法，其中，步骤S1中，所述六硝基合钴酸钠水溶液中钴的摩尔浓度为0.01-0.2mol/L。
  7. 根据权利要求1所述的制备方法，其中，步骤S1中，所述镍锰混合盐溶液中金属离子总摩尔浓度为0.01-2.0mol/L。
  8. 根据权利要求1所述的制备方法，其中，步骤S1中，所述草酸的浓度为0.01-0.5mol/L；所述氨水的浓度为1.0-6.0mol/L。
  9. 根据权利要求1所述的制备方法，其中，步骤S1中，所述反应的温度为45-65℃，pH为8.1-8.3，氨浓度为2.0-5.0g/L。
  10. 根据权利要求1所述的制备方法，其中，步骤S1中，所述粒度达到D50 为2.0-15.0其中。
  11. 根据权利要求1所述的制备方法，其中，步骤S2中，所述煅烧的温度为200-250℃。
  12. 根据权利要求1所述的制备方法，其中，步骤S3中，所述水与所述煅烧料的液固比为5000-8000L/t。
  13. 权利要求1-9任一项所述的制备方法在制备锂离子电池中的应用。
PCT/CN2022/135660 2022-01-24 2022-11-30 具有大通道的正极材料前驱体的制备方法及其应用 WO2023138220A1 (zh)

Priority Applications (1)

Application Number Priority Date Filing Date Title
GB2314805.9A GB2619865A (en) 2022-01-24 2022-11-30 Preparation method for positive electrode material precursor having large channel, and application thereof

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
CN202210077149.4 2022-01-24
CN202210077149.4A CN114436344B (zh) 2022-01-24 2022-01-24 具有大通道的正极材料前驱体的制备方法及其应用

Publications (2)

Publication Number Publication Date
WO2023138220A1 true WO2023138220A1 (zh) 2023-07-27
WO2023138220A9 WO2023138220A9 (zh) 2023-08-24

Family

ID=81368779

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/CN2022/135660 WO2023138220A1 (zh) 2022-01-24 2022-11-30 具有大通道的正极材料前驱体的制备方法及其应用

Country Status (3)

Country Link
CN (1) CN114436344B (zh)
GB (1) GB2619865A (zh)
WO (1) WO2023138220A1 (zh)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN114436344B (zh) * 2022-01-24 2023-07-07 广东邦普循环科技有限公司 具有大通道的正极材料前驱体的制备方法及其应用
CN116102087A (zh) * 2023-02-27 2023-05-12 荆门市格林美新材料有限公司 一种镍锰二元前驱体及其制备方法和应用

Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101215011A (zh) * 2008-01-01 2008-07-09 桂林工学院 镍钴锰酸锂的共沉淀-燃烧合成方法
JP2011219354A (ja) * 2010-04-02 2011-11-04 E & D Co Ltd 結晶性マンガン複合酸化物、リチウム二次電池用リチウムマンガン複合酸化物及びその製造方法
CN103956479A (zh) * 2014-05-20 2014-07-30 天津理工大学 一种高容量球形富锂正极材料的制备方法
CN105226264A (zh) * 2014-06-16 2016-01-06 北京理工大学 一种钠离子电池富钠正极材料及其制备方法和钠离子电池
CN108046231A (zh) * 2017-11-13 2018-05-18 中南大学 一种钠离子电池正极材料及其制备方法
CN109686969A (zh) * 2018-12-14 2019-04-26 北京化工大学 一种层状过渡金属氧化物材料的制备及应用该材料的钠离子电池
CN114436344A (zh) * 2022-01-24 2022-05-06 广东邦普循环科技有限公司 具有大通道的正极材料前驱体的制备方法及其应用

Family Cites Families (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS61203566A (ja) * 1985-03-06 1986-09-09 Japan Storage Battery Co Ltd アルカリ蓄電池用カドミウム負極板の製造法
CN102909022B (zh) * 2012-10-25 2014-04-09 常州大学 一种多孔氧化钴催化剂的制备方法
CN103253717B (zh) * 2013-04-23 2015-01-14 宁夏东方钽业股份有限公司 一种小粒径镍钴锰酸锂前躯体的制备方法
CN110729476B (zh) * 2019-10-22 2021-08-17 中国科学院宁波材料技术与工程研究所 一种赝电容复合的高容量锰酸锂正极材料及其制备方法以及一种锂离子电池
CN111646521B (zh) * 2020-06-02 2023-05-12 格林美股份有限公司 一种高分散性高镍三元前驱体材料制备方法
CN111943282A (zh) * 2020-08-10 2020-11-17 浙江帕瓦新能源股份有限公司 一种结构可控的三元前驱体的制备方法
CN112250091A (zh) * 2020-10-30 2021-01-22 浙江帕瓦新能源股份有限公司 一种高镍三元前驱体、正极材料以及制备方法

Patent Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101215011A (zh) * 2008-01-01 2008-07-09 桂林工学院 镍钴锰酸锂的共沉淀-燃烧合成方法
JP2011219354A (ja) * 2010-04-02 2011-11-04 E & D Co Ltd 結晶性マンガン複合酸化物、リチウム二次電池用リチウムマンガン複合酸化物及びその製造方法
CN103956479A (zh) * 2014-05-20 2014-07-30 天津理工大学 一种高容量球形富锂正极材料的制备方法
CN105226264A (zh) * 2014-06-16 2016-01-06 北京理工大学 一种钠离子电池富钠正极材料及其制备方法和钠离子电池
CN108046231A (zh) * 2017-11-13 2018-05-18 中南大学 一种钠离子电池正极材料及其制备方法
CN109686969A (zh) * 2018-12-14 2019-04-26 北京化工大学 一种层状过渡金属氧化物材料的制备及应用该材料的钠离子电池
CN114436344A (zh) * 2022-01-24 2022-05-06 广东邦普循环科技有限公司 具有大通道的正极材料前驱体的制备方法及其应用

Also Published As

Publication number Publication date
CN114436344A (zh) 2022-05-06
CN114436344B (zh) 2023-07-07
GB2619865A (en) 2023-12-20
WO2023138220A9 (zh) 2023-08-24
GB202314805D0 (en) 2023-11-08

Similar Documents

Publication Publication Date Title
WO2021136243A1 (zh) 改性镍钴铝酸锂正极材料及其制备方法与应用
US11855285B2 (en) Full-gradient nickel cobalt manganese positive electrode material, ruthenium oxide coated material and preparation method thereof
CN112750999B (zh) 正极材料及其制备方法和锂离子电池
CN111129463B (zh) 一种mof包覆的单晶三元正极材料及其前驱体的制备方法
WO2023138220A1 (zh) 具有大通道的正极材料前驱体的制备方法及其应用
CN109616664B (zh) 镍钴锰前驱体、镍钴锰三元材料的制备方法及锂离子电池
CN106784790B (zh) 一种镍钴锰酸锂三元正极材料的制备方法
CN113644262B (zh) 一种层状大粒径高镍单晶三元正极材料及其制备方法
WO2015039490A1 (zh) 富锂正极材料及其制备方法
CN109301189B (zh) 一种类单晶型高镍多元材料的制备方法
WO2022188480A1 (zh) 锂电池复合正极材料的前驱体及复合正极材料的制备方法
WO2022134617A1 (zh) 锂离子电池用正极材料及其制备方法和锂离子电池
CN113603154A (zh) 一种高电压镍钴锰三元前驱体及其制备方法
CN112952085B (zh) 梯度高镍单晶三元材料及其制备方法和使用该材料的电池
CN109962234B (zh) 浓度梯度的单晶正极材料及其制备方法
CN114804235B (zh) 一种高电压镍钴锰酸锂正极材料及其制备方法和应用
CN113603153A (zh) 一种钨掺杂高镍无钴前驱体及其制备方法
CN116053444A (zh) 一种掺杂型层状正极材料及其在钠离子电池中的应用
CN109360948B (zh) 一种类单晶型高镍多元材料前驱体
CN114426313A (zh) 一种高能量密度三元正极材料及其制备方法和应用
CN112678883B (zh) 一种表面富钴型低钴正极材料的制备方法
CN112624209A (zh) 一种Na-Ti-Mg共掺杂三元材料及制备方法和应用
WO2023207248A1 (zh) 核壳结构nca正极材料前驱体及其制备方法和应用
WO2023138221A1 (zh) 镍钴锰三元正极材料纳米棒及其应用
CN114560510B (zh) 一种改性7系三元正极材料及其制备方法和应用

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: 22921644

Country of ref document: EP

Kind code of ref document: A1

ENP Entry into the national phase

Ref document number: 202314805

Country of ref document: GB

Kind code of ref document: A

Free format text: PCT FILING DATE = 20221130

WWE Wipo information: entry into national phase

Ref document number: P202390251

Country of ref document: ES