WO2022104899A1 - Preparation method for positive electrode material for lithium ion battery - Google Patents

Preparation method for positive electrode material for lithium ion battery Download PDF

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WO2022104899A1
WO2022104899A1 PCT/CN2020/132627 CN2020132627W WO2022104899A1 WO 2022104899 A1 WO2022104899 A1 WO 2022104899A1 CN 2020132627 W CN2020132627 W CN 2020132627W WO 2022104899 A1 WO2022104899 A1 WO 2022104899A1
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positive electrode
electrode material
preparation
fatty acid
coating
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French (fr)
Chinese (zh)
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李岩
高晗
葛乐
刘铱焓
高宇心
陈乐�
叶余凯
杨宁
阳建中
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深圳澳睿新能源科技有限公司
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    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/02Electrodes composed of, or comprising, active material
    • H01M4/36Selection of substances as active materials, active masses, active liquids
    • H01M4/362Composites
    • H01M4/366Composites as layered products
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M10/00Secondary cells; Manufacture thereof
    • H01M10/05Accumulators with non-aqueous electrolyte
    • H01M10/052Li-accumulators
    • H01M10/0525Rocking-chair batteries, i.e. batteries with lithium insertion or intercalation in both electrodes; Lithium-ion batteries
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M10/00Secondary cells; Manufacture thereof
    • H01M10/42Methods or arrangements for servicing or maintenance of secondary cells or secondary half-cells
    • H01M10/4235Safety or regulating additives or arrangements in electrodes, separators or electrolyte
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/02Electrodes composed of, or comprising, active material
    • H01M4/04Processes of manufacture in general
    • H01M4/0471Processes of manufacture in general involving thermal treatment, e.g. firing, sintering, backing particulate active material, thermal decomposition, pyrolysis
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/02Electrodes composed of, or comprising, active material
    • H01M4/36Selection of substances as active materials, active masses, active liquids
    • H01M4/48Selection of substances as active materials, active masses, active liquids of inorganic oxides or hydroxides
    • H01M4/50Selection of substances as active materials, active masses, active liquids of inorganic oxides or hydroxides of manganese
    • H01M4/505Selection 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
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/02Electrodes composed of, or comprising, active material
    • H01M4/36Selection of substances as active materials, active masses, active liquids
    • H01M4/48Selection of substances as active materials, active masses, active liquids of inorganic oxides or hydroxides
    • H01M4/52Selection of substances as active materials, active masses, active liquids of inorganic oxides or hydroxides of nickel, cobalt or iron
    • H01M4/525Selection 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
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/02Electrodes composed of, or comprising, active material
    • H01M4/62Selection of inactive substances as ingredients for active masses, e.g. binders, fillers
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/02Electrodes composed of, or comprising, active material
    • H01M4/62Selection of inactive substances as ingredients for active masses, e.g. binders, fillers
    • H01M4/628Inhibitors, e.g. gassing inhibitors, corrosion inhibitors
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/02Electrodes composed of, or comprising, active material
    • H01M2004/026Electrodes composed of, or comprising, active material characterised by the polarity
    • H01M2004/028Positive electrodes
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M2220/00Batteries for particular applications
    • H01M2220/20Batteries in motive systems, e.g. vehicle, ship, plane
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/10Energy storage using batteries

Definitions

  • the invention relates to a preparation method of an electrode material, in particular to a preparation method of a positive electrode material of a lithium battery, which further improves various performances of the battery.
  • Lithium-ion batteries as a green energy storage technology with high energy density and good cycle life, are widely used in various energy storage devices.
  • electric vehicles which have been vigorously developed in order to alleviate environmental pollution, have brought broad business opportunities to the lithium-ion battery industry.
  • Large-scale commercial production of lithium-ion batteries with superior performance and low cost requires continuous innovation in advanced production technologies.
  • the innovation in the production process of lithium-ion battery materials will greatly improve the performance of the entire lithium-ion battery and reduce production costs.
  • the production process and cost of cathode materials have always been an important factor restricting the performance and price of lithium-ion batteries.
  • the continuous pursuit of high energy density of lithium-ion batteries in the industry has forced the cycle cut-off voltage of cathode materials to be higher and higher.
  • a higher cycle cut-off voltage will cause greater stress on the interfacial stability of the cathode material.
  • How to realize the stability of the cathode material interface plays an important role in realizing the stability of the cathode material under high cut-off voltage.
  • the widely adopted technical means is to directly modify the surface of the positive electrode material, usually using oxides, fluorides and other non-electrochemical active materials to directly modify or coat the surface of the positive electrode material.
  • Oxides, fluorides and other substances coated on the surface of the positive electrode material are used to avoid direct contact between the surface of the positive electrode material and the electrolyte, thereby reducing the surface reactivity of the positive electrode material, reducing the dissolution of metal ions, and delaying the transformation of the surface of the positive electrode material.
  • the overall cycle life and safety performance of the battery can be improved.
  • the industry uses the gas phase method, the liquid phase method and the solid phase method to coat the cathode material, of which the solid phase method has the lowest production cost and is the most suitable for large-scale production.
  • the solid-phase method often results in poor material coating effect due to the uneven dispersion of the coating in the early stage. How to achieve uniform coating of cathode materials by solid-phase method has always been a difficulty in the industry.
  • CN108172826A discloses a method for coating high nickel ternary material.
  • the technology firstly mixes the coating material lithium iron phosphate nanoparticles with the high nickel ternary material at low speed, and then performs high speed mechanical mixing to fuse and coat the coating material lithium iron phosphate and the high nickel ternary material to complete the coating experiment.
  • the solid-phase coating method provided by this technology requires too much production equipment and is difficult to produce on a large scale.
  • CN108767221A discloses a method for coating the positive electrode material of lithium ion battery. This technology prepares a cathode material coated with an aluminum-titanium alloy by ball-milling the titanium-aluminum mixed oxide and the cathode material and then sintering at a high temperature. Also, the production steps of this technology are complicated and the equipment requirements are too high, which is not conducive to large-scale production.
  • CN111554907A discloses the application of fatty acid in preparing lithium ion battery and the method for preparing electrode material.
  • fatty acid is used as dispersant, and fatty acid is mixed with coating material as coating precursor, and then the coating is used as a coating precursor.
  • the coating precursor is mixed with the electrode material for solid-phase sintering. After high temperature sintering, the fatty acid will turn into a liquid state to help the coating disperse on the surface of the electrode material, thereby forming a uniformly coated electrode material.
  • This technology solves the problem of large-scale production of solid-state coating, but still needs to add a little more than 1% of coating materials such as metal oxides and metal fluorides, and ideal materials for lithium-ion batteries hope to reduce The amount of these coating materials further improves the battery performance.
  • An object of the present invention is to provide a method for preparing a positive electrode material for a lithium ion battery, which reduces the amount of coating material and further improves the performance of the material.
  • Another object of the present invention is to provide a method for preparing a positive electrode material for a lithium ion battery, which improves the energy retention rate of the material and is beneficial to the application in the lithium ion battery.
  • Another object of the present invention is to provide a method for preparing a positive electrode material of a lithium ion battery, which reduces the increase in resistance and is beneficial to the application in the lithium ion battery.
  • a method for preparing a positive electrode material for a lithium ion battery adding metal salts of C10-C34 fatty acids, maintaining the coating uniformity of the electrode material prepared by the solid-phase method, and reducing the amount of the coating material.
  • the fatty acid provided by the present invention contains at least one carboxyl group.
  • the number of single atoms contained in it is greater than 10, especially 10 to 34, such as: 10, 11, 12, 13, 14, 15, 16, 17, 18, 19, 20, 21, 22, 23, 24, 25, 26, 27, 28, 29, 30, 31, 32, 33 and 34.
  • Another specific compound embodiment is a saturated fatty acid, which includes substituents such as, but not limited to, hydroxyl, mercapto, amino, ester, alkane, alkene, and alkyne groups, and the like.
  • Another specific compound embodiment is an unsaturated fatty acid, including at least one saturated double bond or triple bond, and substituents such as, but not limited to, hydroxyl, mercapto, amino, ester, alkane, alkene, and alkyne groups .
  • fatty acids at room temperature contains two states of liquid phase and solid phase, that is, with the increase of the carbon chain length of fatty acids, fatty acids gradually change from liquid phase to solid phase. That is, when the number of carbon atoms of the saturated fatty acid is 10 or more, the fatty acid is in a solid phase at room temperature. Therefore, it can be matched with the method of coating battery materials with solid phase, and has practical feasibility, and can realize more economical and simpler manufacture of electrode materials.
  • Me is a metal ion, such as but not limited to Li, Mg, Zn, Cu, Ca, Fe, Al, Ni, Co, Mn, Ti, Cr, Zr, Nb, W and other metal ions.
  • the above-mentioned metal salt of the fatty acid is used to coat the lithium ion battery material.
  • the fatty acids are volatilized during the heating process, and the metal salts are oxidized at high temperature to form metal oxides (such as but not limited to Li 2 O, MgO, ZnO, CaO, CuO, NiO, CoO, Al 2 O 3 , Fe 2 O 3 , Cr 2 O 3 , MnO 2 , TiO 2 , ZrO 2 , Nb 2 O 5 and WO 3 , etc.), and will not have any effect on lithium-ion battery materials.
  • metal oxides such as but not limited to Li 2 O, MgO, ZnO, CaO, CuO, NiO, CoO, Al 2 O 3 , Fe 2 O 3 , Cr 2 O 3 , MnO 2 , TiO 2 , ZrO 2 , Nb 2 O 5 and WO 3 , etc.
  • the metal salts of the above-mentioned various fatty acids can coat the lithium-ion battery material, and form uniformly distributed oxides on the material, so that the amount of the used coating material is further reduced. , such as: 1% or less, such as: but not limited to 0.5%, also improves the energy retention rate of the material and reduces the resistance growth.
  • NCM622 chemical formula LiNi 0.6 Co 0.2 Mn 0.2 O 2
  • NCM811 chemical formula LiNi 0.8 Co 0.1 Mn 0.1 O 2
  • NCA chemical formula LiNi 0.8 Co 0.15 Al 0.5 O 2 )
  • the metal salts of fatty acids of the present invention are in the form of solid powders, with particle sizes ranging from 10 nm to 2 ⁇ m, particularly powders with particle sizes ranging from 10 nm to 500 nm.
  • the metal salts of fatty acids of the present invention are aluminum stearate and aluminum laurate.
  • the metal salts of fatty acids of the present invention are magnesium stearate and magnesium laurate.
  • the present invention provides a method for preparing a positive electrode material for a lithium ion battery.
  • the metal salt of the fatty acid is mixed with the positive electrode material for the lithium ion battery, and the surface of the electrode material for the lithium ion battery prepared by sintering (eg, at a temperature of 200° C. to 1000° C.) is uniform.
  • Metal oxides are dispersed.
  • the form of the positive electrode material is preferably powder.
  • the present invention provides a preparation method for preparing a lithium ion positive electrode material.
  • the metal salt of fatty acid is mixed with the positive electrode material for lithium battery, and it is prepared by high-temperature solid-phase reaction sintering. °C, the sintering time is such as: but not limited to 1 hour to 24 hours.
  • Another preparation method for preparing a lithium ion positive electrode material is to mix a metal salt of a fatty acid with a positive electrode material for a lithium battery. The temperature is raised to 200°C to 1000°C and sintered for 1 hour to 24 hours, so as to complete the solid-phase reaction between the coating material and the lithium ion battery material. After the sintering reaction is completed, the material is dispersed and sieved to obtain a uniformly coated positive electrode material.
  • the addition amount of the metal salt is correspondingly determined according to the content of the metal oxide in the prepared positive electrode material (for example: 0.6% ⁇ 0.1%).
  • the metal salt of fatty acid is mixed with the positive electrode material for lithium battery, and it is prepared by high-temperature solid-phase reaction sintering, and in the obtained coated positive electrode material, the metal oxide accounts for The mass percentage is: 0.6% ⁇ 0.1%, such as: 0.5%, 0.6% and 0.7%.
  • the temperature is usually raised to 200°C to 1000°C at a rate of 1°C/min to 10°C/min, and then kept for 1 hour to 24 hours.
  • Another preparation method for preparing a lithium ion positive electrode material is that aluminum stearate or aluminum laurate is mixed with a positive electrode material for lithium batteries, and the temperature is raised to 200°C to 1000°C at a rate of 1 to 10°C/min. The temperature is maintained for another 1 to 24 hours, thereby completing the solid-phase reaction between the coating material and the lithium ion battery material. After the sintering reaction is completed, the material is dispersed and sieved to obtain a uniformly coated positive electrode material.
  • the specific sintering temperature and sintering time are determined according to the decomposition temperature of the fatty acid salt used.
  • the present invention can directly carry out uniform coating on the surface of the positive electrode material through high-temperature solid-phase reaction, the operation is simple, the cost is low, and it is very suitable for large-scale industrial production. After the reaction, except for the target coating (such as metal oxide) formed on the surface of the positive electrode material, no impurities will be generated, and the amount of the coating contained in the material is further reduced, so that the performance of the material is further improved.
  • the target coating such as metal oxide
  • the preparation method of the positive electrode material of the lithium battery provided by the present invention can quickly realize the uniform coating of the positive electrode material, enhance the interface stability of the positive electrode material of the lithium ion battery, thereby enhancing the safety stability and cycle life of the material, and at the same time significantly Improve the resistance increase that occurs when the battery material is used.
  • Fig. 1 is magnesium stearate TGA curve figure
  • Fig. 2 is aluminum stearate TGA curve figure
  • Fig. 3 is aluminum laurate TGA curve diagram
  • Fig. 4 is the surface element analysis diagram of comparative example 1;
  • Fig. 5 is the magnesium distribution diagram of the materials prepared in Example 1A, Example 1B and Example 1C;
  • Example 6 is the XRD patterns of Comparative Example 1, Comparative Example 2, Example 1A, Example 1B, Example 1C and Example 2;
  • FIG. 7 is a comparison diagram of charge-discharge curves of materials for battery positive electrodes prepared in Comparative Example 1, Comparative Example 2, Example 1A, Example 1B, Example 1C and Example 2;
  • FIG. 8 is a comparison diagram of DCIR changes during the cycle of materials for battery positive electrodes prepared in Comparative Example 1, Comparative Example 2, Example 1A, Example 1B, Example 1C and Example 2;
  • Fig. 10 is the XRD pattern of comparative example 3, embodiment 3 and embodiment 4;
  • FIG. 11 is a comparison diagram of charge-discharge curves of the materials for battery positive electrodes prepared in Comparative Example 3, Example 3 and Example 4;
  • Fig. 12 is the XRD pattern of comparative example 4, embodiment 5 and embodiment 6;
  • FIG. 13 is a comparison diagram of charge-discharge curves of the materials for battery positive electrodes prepared in Comparative Example 4, Example 5 and Example 6;
  • FIG. 14 is a comparison chart of the cycle performance test of the materials for battery positive electrodes prepared in Comparative Example 4 and Example 5.
  • FIG. 14 is a comparison chart of the cycle performance test of the materials for battery positive electrodes prepared in Comparative Example 4 and Example 5.
  • the test equipment for X-ray diffraction is Bruker D2-XE-T
  • the target material used in this instrument is a copper target
  • the X-ray wavelength is First, weigh 1g to 2g of sample, spread the sample as flat as possible in the center of the sample stage, and then use a glass slide to smooth it to ensure that the sample is flush with the sample groove and that no sample is outside the groove. Finally, put the prepared sample stage into Bruker D2-XE-T for testing.
  • the scanning range of X-ray 2 ⁇ is set to 10° ⁇ 80°, the scanning step is 0.01°, and the X-ray exposure time of each step is is 0.1s.
  • the prepared lithium ion battery cathode material is mixed with a conductive agent (such as: carbon black), a binder (such as: polyvinylidene fluoride) and a solvent (such as: N-methylpyrrolidone) to prepare an electrode slurry, and then It was coated on an aluminum-based current collector, dried to prepare an electrode, and the electrode was assembled into a button battery, and electrochemical tests were carried out using a Neware (CT-4008) battery charge-discharge instrument.
  • the coin cell battery was firstly cycled between 2.75-4.4V with a current of 0.1C for 4 turns, and then the cycle test was performed with a current of 0.2C or 0.5C in the same voltage range.
  • DCIR discharge DC resistance
  • the method for the instrument to calculate the DCIR is: after the charging step is over, the next step is the shelving step, and the voltage (V 1 ) at the last point of the shelving step is recorded. After the shelving step is over, the next step is the discharge step, the battery is discharged with a constant current (I), and the voltage (V 2 ) at the first point of the discharge step is recorded at the same time.
  • Thermogravimetric analysis of the fatty acid salts used was performed on a PerkinElmer-STA-8000 instrument. First, weigh 6 mg to 20 mg of fatty acid salt into the crucible and put the crucible lid on it. Put the crucible containing the fatty acid salt and another empty crucible into the instrument furnace at the same time. Next, oxygen was injected into the furnace as the reaction atmosphere, and argon was used as the protective gas of the furnace body, and the material was heated to 800 degrees Celsius with a heating rate of 5°C/min to conduct a thermogravimetric analysis experiment on the material.
  • the chemical formula of the positive electrode material NCM523 used in this comparative example is LiNi 0.5 Co 0.2 Mn 0.3 O 2 , and the material has not undergone any coating treatment.
  • the comparative samples were characterized by XRD, SEM and EDS, electrochemical cycle life and DCIR tests.
  • the chemical formula of the positive electrode material NCM523 used in this comparative example is LiNi 0.5 Co 0.2 Mn 0.3 O 2 , and stearic acid and nano-alumina (Al 2 O 3 ) are used at the same time, and the Al 2 O 3 particle size is between 20-30 nanometers
  • the mixture of NCM523 was used as the coating material to conduct coating experiments on NCM523.
  • a mixture of 3 g of stearic acid and nano-Al 2 O 3 is prepared, wherein the mass percentage of stearic acid is controlled at 3% to 30%.
  • 10g to 30g of ball milling beads are added to the above mixture for high-speed ball milling, the ball milling time is set to 1 hour to 5 hours, and the ball milling speed is set to 100 to 600 rmp.
  • the mixture of stearic acid and nano-Al 2 O 3 was collected, that is, the coating material.
  • An appropriate amount of NCM523 was taken, and the corresponding coating material (ie a mixture of stearic acid and nano-Al 2 O 3 ) was added to achieve a mass percentage of Al 2 O 3 of 0.5%.
  • the NCM523 and the coating precursor are placed in a mixer and mixed for 1 to 8 hours.
  • the above mixture is heated to 200°C to 1000°C at a rate of 1°C/min to 10°C/min, maintained at this temperature for 1 to 24 hours, and then cooled to room temperature with the furnace to complete the coating process.
  • the comparative samples were tested for electrochemical cycle life and DCIR.
  • the chemical formula of the positive electrode material NCM622 used in this comparative example is LiNi 0.6 Co 0.2 Mn 0.2 O 2 , and the material has not undergone any coating treatment.
  • the comparative samples were characterized by XRD, SEM and EDS, electrochemical cycle life and DCIR tests.
  • the chemical formula of the positive electrode material NCM811 used in this comparative example is LiNi 0.8 Co 0.1 Mn 0.1 O 2 , and the material has not undergone any coating treatment.
  • the comparative samples were characterized by XRD, SEM and EDS, electrochemical cycle life and DCIR tests.
  • the positive electrode material used in this example is the same NCM523 as in Comparative Example 1, its chemical formula is LiNi 0.5 Co 0.2 Mn 0.3 O 2 , and the fatty acid salt used is magnesium stearate (C 36 H 70 MgO 4 ).
  • NCM523 and magnesium stearate are fully mixed.
  • the above mixture was heated to 650°C at a rate of 5°C/min and held for 10 hours. After cooling to room temperature with the furnace, the above-mentioned materials prepared by sintering are dispersed and sieved to obtain the final coated positive electrode material, and the coating experiment is completed.
  • magnesium stearate is equivalent to the content of magnesium oxide in the above-mentioned comparative example and is converted.
  • mass percentages of magnesium oxide-coated NCM523 finally prepared are: 0.5% (marked as: Example 1A), 1% (marked as: Example 1B) and 2% (marked as: Example 1C).
  • the synthesized samples were characterized by XRD, SEM and EDS, electrochemical cycle life and DCIR tests.
  • the positive electrode material used in this example is the same NCM523 as in Comparative Example 1, its chemical formula is LiNi 0.5 Co 0.2 Mn 0.3 O 2 , and the fatty acid salt used is aluminum stearate (C 54 H 105 AlO 6 ).
  • NCM523 and aluminum stearate into a mixer, mix and stir for 8 hours, so that NCM523 and aluminum stearate are fully mixed.
  • the above mixture was heated to 650°C at a rate of 5°C/min and held for 10 hours. After cooling to room temperature with the furnace, the above-mentioned materials prepared by sintering are dispersed and sieved to obtain the final coated positive electrode material, and the coating experiment is completed.
  • the added amount of aluminum stearate is equivalent to the content of aluminum oxide in the above-mentioned comparative example.
  • the mass percentage of alumina-coated NCM523 is finally 0.5%.
  • the synthesized samples were characterized by XRD, SEM and EDS, electrochemical cycle life and DCIR tests.
  • the positive electrode material used in this example is the same NCM622 as in Comparative Example 3, its chemical formula is LiNi 0.6 Co 0.2 Mn 0.2 O 2 , and the fatty acid salt used is aluminum stearate (C 54 H 105 AlO 6 ).
  • NCM622 and aluminum stearate into a mixer, mix and stir for 8 hours, so that NCM622 and aluminum stearate are fully mixed.
  • the above mixture was heated to 650°C at a rate of 5°C/min and held for 10 hours. After cooling to room temperature with the furnace, the above-mentioned materials prepared by sintering are dispersed and sieved to obtain the final coated positive electrode material, and the coating experiment is completed.
  • the added amount of aluminum stearate is equivalent to the content of aluminum oxide in the above-mentioned comparative example.
  • the mass percentage of alumina-coated NCM622 is finally 0.5%.
  • the synthesized samples were characterized by XRD, SEM and EDS, electrochemical cycle life and DCIR tests.
  • the positive electrode material used in this example is the same NCM622 as in Comparative Example 3, its chemical formula is LiNi 0.6 Co 0.2 Mn 0.2 O 2 , and the fatty acid salt used is aluminum laurate (C 36 H 69 AlO 6 ).
  • NCM622 and aluminum laurate into the mixer, mix and stir for 8 hours, so that NCM622 and aluminum laurate are fully mixed.
  • the above mixture was heated to 500°C at a rate of 5°C/min and held for 10 to 24 hours. After cooling to room temperature with the furnace, the above-mentioned materials prepared by sintering are dispersed and sieved to obtain the final coated positive electrode material, and the coating experiment is completed.
  • the added amount of aluminum laurate is equivalent to the content of alumina in the above-mentioned comparative example.
  • the mass percentage of alumina-coated NCM622 is finally 0.5%.
  • the synthesized samples were characterized by XRD, SEM and EDS, electrochemical cycle life and DCIR tests.
  • the positive electrode material used in this example is the same NCM811 as in Comparative Example 4, its chemical formula is LiNi 0.8 Co 0.1 Mn 0.1 O 2 , and the fatty acid salt used is aluminum stearate (C 54 H 105 AlO 6 ).
  • NCM811 and aluminum stearate into the mixer, mix and stir for 8 hours, so that NCM811 and aluminum stearate are fully mixed.
  • the above mixture was heated to 650°C at a rate of 5°C/min and held for 10 hours. After cooling to room temperature with the furnace, the above-mentioned materials prepared by sintering are dispersed and sieved to obtain the final coated positive electrode material, and the coating experiment is completed.
  • the added amount of aluminum stearate is equivalent to the content of aluminum oxide in the above-mentioned comparative example.
  • the mass percentage of alumina-coated NCM811 is finally 0.25%.
  • the synthesized samples were characterized by XRD, SEM and EDS, electrochemical cycle life and DCIR tests.
  • the positive electrode material used in this example is the same NCM811 as in Comparative Example 4, its chemical formula is LiNi 0.8 Co 0.1 Mn 0.1 O 2 , and the fatty acid salt used is magnesium stearate (C 36 H 70 MgO 4 ).
  • the above mixture was heated to 650°C at a rate of 5°C/min and held for 10 hours. After cooling to room temperature with the furnace, the above-mentioned materials prepared by sintering are dispersed and sieved to obtain the final coated positive electrode material, and the coating experiment is completed.
  • magnesium stearate is equivalent to the content of magnesium oxide in the above-mentioned comparative example and is converted.
  • mass percentage of magnesium oxide-coated NCM811 was finally prepared to be 0.25%.
  • the synthesized samples were characterized by XRD, SEM and EDS, electrochemical cycle life and DCIR tests.
  • three fatty acid salts are used as examples, namely: magnesium stearate, aluminum stearate and aluminum laurate.
  • the TGA results for these three fatty acid salts are shown in FIGS. 1 to 3 .
  • thermogravimetric analysis all three fatty acid salts decomposed with the increase of heating temperature.
  • Comparative Example 1 The SEM/EDS characterization of Comparative Example 1 was carried out. As shown in Figure 4, only the main elements nickel, cobalt and manganese of NCM523 were detected in Comparative Example 1, and no other metal elements were detected, indicating that Comparative Example 1 was uncoated NCM523 does not have magnesium.
  • the NCM523 coated with magnesium stearate was subjected to SEM/EDS (i.e., Example 1A, Example 1B and Example 1C), and the main elements nickel, cobalt, and manganese could be found at the same time, and the oxidation after coating could be observed at the same time.
  • the magnesium element in magnesium as shown in Figure 5, wherein the magnesium element in Example 1A, Example 1B and Example 1C are uniformly distributed on the surface of the positive electrode material particles, and with the increase of the amount of coating material, the signal of Mg It is gradually enhanced, which proves that the coating amount of MgO gradually increases.
  • the uncoated NCM523 (ie, Comparative Example 1) is a pure R-3m layered structure.
  • Simultaneously using fatty acid salts to form oxide-coated NCM523 ie, Example 1A, Example 1B, Example 1C, and Example 2), characterized by XRD, it is also a pure R-3m layered structure.
  • the data show that NCM523 coated with fatty acid salts does not generate any impurity phase. Therefore, the use of fatty acid salts will not affect the original positive electrode material due to the introduction of impurity phases during the coating process.
  • the electrochemical performance of uncoated NCM523 and NCM523 coated with fatty acid salts were compared. Since the coating material is an oxide and has no electrochemical activity, the charge-discharge capacity of the positive electrode material will decrease with the increase of the quality of the coating material.
  • the charge-discharge curves of the three examples and Comparative Example 1 are compared as shown in Figure 7. As the content of MgO coating increases, the charge-discharge capacity of NCM523 gradually decreases. The charge-discharge capacity of Example 1A is comparable to that of Comparative Example 1.
  • the MgO-coated NCM523 also showed a smaller increase in resistance during cycling, as shown in Fig. It shows high interface stability.
  • Table 1 summarizes the energy retention rate of each of the above samples. After 50 cycles, all NCM523 coated with magnesium stearate have higher energy retention rate compared with the uncoated NCM523, which is coated with 0.5% MgO. The covered NCM523 has the highest energy retention rate of 94.3%.
  • NCM523 (Example 1A) using magnesium stearate to achieve 0.5% MgO coating is the optimal coating condition. Therefore, the total coating amount of 0.5% oxide is still taken, and NCM523 is coated with aluminum stearate to obtain Example 2. At the same time, NCM523 was coated with stearic acid and alumina to obtain Comparative Example 2.
  • Comparative Example 1, Comparative Example 2 and Example 2 were compared.
  • the XRD test shows that Comparative Example 1, Comparative Example 2 and Example 2 are all pure R-3m layered structures (see FIG. 6 ), and no impurities are found.
  • the electrochemical test of the three shows that Comparative Example 1, Comparative Example 2 and Example 2 all have comparable initial charge and discharge capacities (see Figure 7); among them, Example 2 has the smallest increase in DC resistance (see Figure 8). After 50 cycles, the energy retention rate of Example 2 can reach 95.3%, which is the sample with the highest energy retention rate. As shown in FIG. 9 , comparing the energy retention rates of Example 2 and Comparative Example 2, Example 2 has a better energy retention rate.
  • the uncoated NCM622 (Comparative Example 3) is a pure R-3m layered structure.
  • the data show that NCM622 coated with aluminum stearate and aluminum laurate as fatty acid salts does not produce any impurity phase. Therefore, the use of fatty acid salts will not affect the original positive electrode material due to the introduction of impurity phases during the coating process.
  • Comparative Example 3 The electrochemical performance of Comparative Example 3 was compared with that of Examples 3 and 4. Since the coating material is an oxide and has no electrochemical activity, the charge-discharge capacity of the positive electrode material will decrease with the increase of the quality of the coating material.
  • Figure 11 shows the comparison of the charge-discharge curves of Comparative Example 3, Example 3 and Example 4.
  • the charge-discharge capacity of Example 3 and Example 4 is slightly lower than that of Comparative Example 3.
  • the energy retention rates of Example 3 and Example 4 can reach 92.2% and 90.8%, respectively, which are higher than 89.2% of Comparative Example 3. It can be seen from Table 1 that after 50 cycles, the resistances of Example 3 and Example 4 can reach 25.9 ohm and 30.98 ohm, which are both lower than the 31.76 ohm of Comparative Example 3.
  • the uncoated NCM811 (Comparative Example 4) is a pure R-3m layered structure.
  • NCM811 was coated with 0.25% Al 2 O 3 and MgO to obtain Examples 5 and 6, which were characterized by XRD and were also pure R-3m layered structure.
  • the data show that NCM811 coated with aluminum stearate and magnesium stearate as fatty acid salts does not produce any impurity phase. Therefore, the use of fatty acid salts will not affect the original positive electrode material due to the introduction of impurity phases during the coating process.
  • Comparative Example 4 The electrochemical performance of Comparative Example 4 was compared with that of Examples 5 and 6. Although the coating material is an oxide and has no electrochemical activity, the mass of the coating material of 0.25% has little effect on the charge-discharge capacity of the positive electrode material NCM811. For the comparison of the charge-discharge curves of Comparative Example 4, Example 5 and Example 6, see FIG. 13 . After 50 cycles, the energy retention rates of Example 5 and Example 6 can reach 88.3% and 85.6%, respectively, which are higher than 85.5% of Comparative Example 4, but compared with Example 3 and Example 4, the value is lower, It is shown that it is inferior to Example 3 and Example 4 in terms of energy retention.
  • FIG. 14 compares the discharge capacity of Example 5 and Comparative Example 4, and the discharge capacity retention rate of Example 5 is better than that of Comparative Example 4.

Abstract

A preparation method for a positive electrode material for a lithium ion battery, characterized in that a metal salt of a fatty acid is mixed with the positive electrode material for a lithium battery, and a coated positive electrode material is prepared by high-temperature solid-phase reaction sintering. The preparation method provided by the present invention can quickly realize uniform coating of a positive electrode material, enhancing the interface stability of a positive electrode material for a lithium ion battery, thereby enhancing the safety, stability and cycle life of the material and significantly eliminating resistance rise after the use of the battery material.

Description

锂离子电池正极材料的制取方法Preparation method of positive electrode material for lithium ion battery 技术领域technical field
本发明涉及一种电极材料的制备方法,尤其涉及一种锂电池正极材料的制备方法,进一步提高电池的各项性能。The invention relates to a preparation method of an electrode material, in particular to a preparation method of a positive electrode material of a lithium battery, which further improves various performances of the battery.
背景技术Background technique
锂离子电池作为一种绿色环保,高能量密度,循环寿命良好的储能技术,被广泛应用于各种储能器件。特别是近来,为了缓解环境污染而大力发展的电动汽车,为锂离子电池产业带来广阔商机。大规模商业化生产,性能优越,成本低廉的锂离子电池需要先进生产技术的不断革新。尤其是在锂离子电池材料的生产工艺上的革新,将极大提高整个锂离子电池的性能同时降低生产成本。作为锂离子电池不可或缺的组成部分,正极材料的生产工艺与成本一直是制约锂离子电池性能与价格的重要因素。业界不断追求锂离子电池高能量密度,迫使正极材料的循环截止电压越来越高。较高的循环截止电压对于正极材料的界面稳定性将造成较大压力。如何实现正极材料界面稳定性,对于实现高截止电压下,正极材料的稳定性具有重要作用。目前广泛采取的技术手段就是对正极材料表面进行直接修饰,通常使用氧化物,氟化物等非电化学活性材料对正极材料表面进行直接修饰或者称为包覆。利用包覆在正极材料表面的氧化物,氟化物等物质,避免正极材料表面与电解液直接接触,从而降低正极材料表面反应活性,减少金属离子溶解,延缓正极材料表面结构转变等问题。通过包覆正极材料,可以提高电池整体循环寿命及安全性能。Lithium-ion batteries, as a green energy storage technology with high energy density and good cycle life, are widely used in various energy storage devices. Especially recently, electric vehicles, which have been vigorously developed in order to alleviate environmental pollution, have brought broad business opportunities to the lithium-ion battery industry. Large-scale commercial production of lithium-ion batteries with superior performance and low cost requires continuous innovation in advanced production technologies. In particular, the innovation in the production process of lithium-ion battery materials will greatly improve the performance of the entire lithium-ion battery and reduce production costs. As an indispensable part of lithium-ion batteries, the production process and cost of cathode materials have always been an important factor restricting the performance and price of lithium-ion batteries. The continuous pursuit of high energy density of lithium-ion batteries in the industry has forced the cycle cut-off voltage of cathode materials to be higher and higher. A higher cycle cut-off voltage will cause greater stress on the interfacial stability of the cathode material. How to realize the stability of the cathode material interface plays an important role in realizing the stability of the cathode material under high cut-off voltage. At present, the widely adopted technical means is to directly modify the surface of the positive electrode material, usually using oxides, fluorides and other non-electrochemical active materials to directly modify or coat the surface of the positive electrode material. Oxides, fluorides and other substances coated on the surface of the positive electrode material are used to avoid direct contact between the surface of the positive electrode material and the electrolyte, thereby reducing the surface reactivity of the positive electrode material, reducing the dissolution of metal ions, and delaying the transformation of the surface of the positive electrode material. By coating the positive electrode material, the overall cycle life and safety performance of the battery can be improved.
业界通过气相法,液相法和固相法对于正极材料进行包覆,其中固相法的生产成本最低,最适合进行大规模生产。但固相法往往会因为前期处理包覆物分散不均匀的原因造成材料包覆效果欠佳。如何通过固相法实现正极材料的均匀包覆一直是业界难点。The industry uses the gas phase method, the liquid phase method and the solid phase method to coat the cathode material, of which the solid phase method has the lowest production cost and is the most suitable for large-scale production. However, the solid-phase method often results in poor material coating effect due to the uneven dispersion of the coating in the early stage. How to achieve uniform coating of cathode materials by solid-phase method has always been a difficulty in the industry.
CN108172826A公开了一种包覆高镍三元材料的方法。该技术首先将包覆材料磷酸铁锂纳米颗粒与高镍三元材料进行低速机械混合,而后进行高速机械混合将包覆材料磷酸铁锂与高镍三元材料进行融合包覆完成包覆实验。该技术所提供的固相包覆的方法对于生产设备要求过高,很难大规模生产。CN108172826A discloses a method for coating high nickel ternary material. The technology firstly mixes the coating material lithium iron phosphate nanoparticles with the high nickel ternary material at low speed, and then performs high speed mechanical mixing to fuse and coat the coating material lithium iron phosphate and the high nickel ternary material to complete the coating experiment. The solid-phase coating method provided by this technology requires too much production equipment and is difficult to produce on a large scale.
CN108767221A公开了一种包覆锂离子电池正极材料的方法。该技术通过将钛铝混合氧化物与正极材料通过球磨后,进行高温烧结,从而制备出由铝钛合金包覆的正极材料。同样该技术生产步骤复杂同时对于设备要求过高,不利于大规模生产。CN108767221A discloses a method for coating the positive electrode material of lithium ion battery. This technology prepares a cathode material coated with an aluminum-titanium alloy by ball-milling the titanium-aluminum mixed oxide and the cathode material and then sintering at a high temperature. Also, the production steps of this technology are complicated and the equipment requirements are too high, which is not conducive to large-scale production.
CN111554907A公开了一种脂肪酸在制备锂离子电池中的应用及制取电极材料的方法,该技术通过使用脂肪酸作为分散剂,先将脂肪酸与包覆物质进行混合作为包覆前驱体,而后将该包覆前驱体与电极材料混合进行固相烧结,经过高温烧结,脂肪酸将变为液态有助于包覆物分散到电极材料表面,从而形成均匀包覆的电极材料。该技术很好地解决了固态法包覆大 规模生产的问题,但是仍需加入些许如:1%以上的金属氧化物和金属氟化物等包覆材料,理想的锂离子电池的材料则希望减少这些包覆材料的用量,进一步提高电池性能。CN111554907A discloses the application of fatty acid in preparing lithium ion battery and the method for preparing electrode material. In this technology, fatty acid is used as dispersant, and fatty acid is mixed with coating material as coating precursor, and then the coating is used as a coating precursor. The coating precursor is mixed with the electrode material for solid-phase sintering. After high temperature sintering, the fatty acid will turn into a liquid state to help the coating disperse on the surface of the electrode material, thereby forming a uniformly coated electrode material. This technology solves the problem of large-scale production of solid-state coating, but still needs to add a little more than 1% of coating materials such as metal oxides and metal fluorides, and ideal materials for lithium-ion batteries hope to reduce The amount of these coating materials further improves the battery performance.
发明内容SUMMARY OF THE INVENTION
本发明的一个目的在于提供一种锂离子电池正极材料的制取方法,降低包覆材料的用量,使得材料的性能进一步提高。An object of the present invention is to provide a method for preparing a positive electrode material for a lithium ion battery, which reduces the amount of coating material and further improves the performance of the material.
本发明的另一个目的在于提供一种锂离子电池正极材料的制取方法,提高了材料的能量保持率,利于在锂离子电池中的应用。Another object of the present invention is to provide a method for preparing a positive electrode material for a lithium ion battery, which improves the energy retention rate of the material and is beneficial to the application in the lithium ion battery.
本发明的再一个目的在于提供一种锂离子电池正极材料的制取方法,降低电阻增长,利于在锂离子电池中的应用。Another object of the present invention is to provide a method for preparing a positive electrode material of a lithium ion battery, which reduces the increase in resistance and is beneficial to the application in the lithium ion battery.
一种锂离子电池正极材料的制取方法,加入C10~C34的脂肪酸的金属盐,保持固相法制成的电极材料的包覆均匀性,降低包覆材料的用量。A method for preparing a positive electrode material for a lithium ion battery, adding metal salts of C10-C34 fatty acids, maintaining the coating uniformity of the electrode material prepared by the solid-phase method, and reducing the amount of the coating material.
本发明提供的脂肪酸至少含有一个羧基。比如:但不限于饱和或不饱和一元酸、饱和或不饱和二元酸,以及饱和或不饱和三元酸等,其所含的单原子数量大于10,尤其是10~34,如:10、11、12、13、14、15、16、17、18、19、20、21、22、23、24、25、26、27、28、29、30、31、32、33和34。The fatty acid provided by the present invention contains at least one carboxyl group. For example: but not limited to saturated or unsaturated monobasic acid, saturated or unsaturated dibasic acid, and saturated or unsaturated tribasic acid, etc., the number of single atoms contained in it is greater than 10, especially 10 to 34, such as: 10, 11, 12, 13, 14, 15, 16, 17, 18, 19, 20, 21, 22, 23, 24, 25, 26, 27, 28, 29, 30, 31, 32, 33 and 34.
另一种具体的化合物实施方式为饱和脂肪酸,其上包括取代基如:但不限于羟基、巯基、氨基、酯基、烷烃基、烯烃基和炔烃基等。Another specific compound embodiment is a saturated fatty acid, which includes substituents such as, but not limited to, hydroxyl, mercapto, amino, ester, alkane, alkene, and alkyne groups, and the like.
另一种具体的化合物实施方式为不饱和脂肪酸,至少包括1个饱和双键或三键,以及如:但不限于羟基、巯基、氨基、酯基、烷烃基、烯烃基和炔烃基等取代基。Another specific compound embodiment is an unsaturated fatty acid, including at least one saturated double bond or triple bond, and substituents such as, but not limited to, hydroxyl, mercapto, amino, ester, alkane, alkene, and alkyne groups .
为了使得锂离子电池电极材料拥有更高的热稳定性和循环寿命。利用脂肪酸在室温状态下包含液相和固相两种状态特性,即随着脂肪酸碳链长度的增加,脂肪酸逐渐由液相变为固相。即当饱和脂肪酸的碳原子数大于等于10时,脂肪酸在室温状态下呈固相。因此能够与固相包覆电池材料的方法相配合,且具有实际的可行性,能实现更经济和更简单地制造电极材料。In order to make lithium-ion battery electrode materials have higher thermal stability and cycle life. The use of fatty acids at room temperature contains two states of liquid phase and solid phase, that is, with the increase of the carbon chain length of fatty acids, fatty acids gradually change from liquid phase to solid phase. That is, when the number of carbon atoms of the saturated fatty acid is 10 or more, the fatty acid is in a solid phase at room temperature. Therefore, it can be matched with the method of coating battery materials with solid phase, and has practical feasibility, and can realize more economical and simpler manufacture of electrode materials.
另一种具体的脂肪酸的金属盐实施方式如式Me t+[CH 3(CH 2) nCOO] t所示,n为8至32的整数,如:8、9、10、11、12、13、14、15、16、17、18、19、20、21、22、23、24、25、26、27、28、29、30、31和32。t为1至7的整数,如:1、2、3、4、5、6和7。Me为金属离子,如:但不限于Li,Mg,Zn,Cu,Ca,Fe,Al,Ni,Co,Mn,Ti,Cr,Zr,Nb和W等金属离子。 Another specific embodiment of the metal salt of fatty acid is shown in the formula Me t+ [CH 3 (CH 2 ) n COO] t , where n is an integer from 8 to 32, such as: 8, 9, 10, 11, 12, 13 , 14, 15, 16, 17, 18, 19, 20, 21, 22, 23, 24, 25, 26, 27, 28, 29, 30, 31 and 32. t is an integer from 1 to 7, such as: 1, 2, 3, 4, 5, 6 and 7. Me is a metal ion, such as but not limited to Li, Mg, Zn, Cu, Ca, Fe, Al, Ni, Co, Mn, Ti, Cr, Zr, Nb, W and other metal ions.
在采用固相法制备电极材料时,将上述脂肪酸的金属盐用于包覆锂离子电池材料。其中的脂肪酸在加热过程中挥发,金属盐则在高温下被氧化,形成金属氧化物(如:但不限于Li 2O,MgO,ZnO,CaO,CuO,NiO,CoO,Al 2O 3,Fe 2O 3,Cr 2O 3,MnO 2,TiO 2,ZrO 2,Nb 2O 5和WO 3等),且不会对锂离子电池材料产生任何影响。 When the electrode material is prepared by the solid-phase method, the above-mentioned metal salt of the fatty acid is used to coat the lithium ion battery material. The fatty acids are volatilized during the heating process, and the metal salts are oxidized at high temperature to form metal oxides (such as but not limited to Li 2 O, MgO, ZnO, CaO, CuO, NiO, CoO, Al 2 O 3 , Fe 2 O 3 , Cr 2 O 3 , MnO 2 , TiO 2 , ZrO 2 , Nb 2 O 5 and WO 3 , etc.), and will not have any effect on lithium-ion battery materials.
在采用固相法制备电池材料时,上述各种脂肪酸的金属盐均能对锂离子电池材料实现包覆,并在材料上形成均匀分布的氧化物,使得所采用的包覆材料的用量进一步下降,比如: 1%以下,如:但不限于0.5%,还提高了材料的能量保持率和降低了电阻增长。When the battery material is prepared by the solid-phase method, the metal salts of the above-mentioned various fatty acids can coat the lithium-ion battery material, and form uniformly distributed oxides on the material, so that the amount of the used coating material is further reduced. , such as: 1% or less, such as: but not limited to 0.5%, also improves the energy retention rate of the material and reduces the resistance growth.
如技术人员所知悉,用于制造正极的材料包括:层状结构材料如Li 1±mNi xCo yMn zM 1-x-y-zO 2所示,其中M是微量元素,如:但不限于Cr,Mg,Al,Ti,Zr,Zn,Ca,Nb和W等;m取值范围为0.005到0.2;x、y和z独立选自0到1任意数,且x、y和z之和为0.8~1,比如:但不限于x=0.8,y=0.1,z=0.1或x=0.8,y=0,z=0.15。常见的三元材料如:但不限于NCM622(化学式为LiNi 0.6Co 0.2Mn 0.2O 2)、NCM811(化学式为LiNi 0.8Co 0.1Mn 0.1O 2)和NCA(化学式为LiNi 0.8Co 0.15Al 0.5O 2)等。这些材料单独或组合应用于本发明。 As known to those skilled in the art, the materials used to manufacture the positive electrode include: layered structure materials such as Li 1±m Ni x Co y Mn z M 1-xyz O 2 , where M is a trace element such as: but not limited to Cr , Mg, Al, Ti, Zr, Zn, Ca, Nb and W, etc.; m ranges from 0.005 to 0.2; x, y and z are independently selected from 0 to 1, and the sum of x, y and z is 0.8~1, such as but not limited to: x=0.8, y=0.1, z=0.1 or x=0.8, y=0, z=0.15. Common ternary materials such as: but not limited to NCM622 (chemical formula LiNi 0.6 Co 0.2 Mn 0.2 O 2 ), NCM811 (chemical formula LiNi 0.8 Co 0.1 Mn 0.1 O 2 ) and NCA (chemical formula LiNi 0.8 Co 0.15 Al 0.5 O 2 ) )Wait. These materials are used in the present invention alone or in combination.
本发明的脂肪酸的金属盐,其形态为固体粉末,粒径为10nm~2μm,尤其是粒径10nm~500nm的粉末。The metal salts of fatty acids of the present invention are in the form of solid powders, with particle sizes ranging from 10 nm to 2 μm, particularly powders with particle sizes ranging from 10 nm to 500 nm.
本发明的脂肪酸的金属盐为硬脂酸铝和月桂酸铝。The metal salts of fatty acids of the present invention are aluminum stearate and aluminum laurate.
本发明的脂肪酸的金属盐为硬脂酸镁和月桂酸镁。The metal salts of fatty acids of the present invention are magnesium stearate and magnesium laurate.
本发明提供的锂离子电池正极材料的制取方法,将脂肪酸的金属盐与锂离子电池正极材料混合,经烧结(温度如:200℃~1000℃)而制得的锂离子电池电极材料表面均匀分散着金属氧化物。The present invention provides a method for preparing a positive electrode material for a lithium ion battery. The metal salt of the fatty acid is mixed with the positive electrode material for the lithium ion battery, and the surface of the electrode material for the lithium ion battery prepared by sintering (eg, at a temperature of 200° C. to 1000° C.) is uniform. Metal oxides are dispersed.
应用于本发明制取方法的锂离子电池正极材料,其形态优先选择粉体。For the positive electrode material of the lithium ion battery applied to the preparation method of the present invention, the form of the positive electrode material is preferably powder.
本发明提供的一种制备锂离子正极材料的制备方法,脂肪酸的金属盐与用于锂电池的正极材料进行混合,通过高温固相反应烧结制得,烧结温度如:但不限于200℃~1000℃,烧结时间如:但不限于1小时~24小时。The present invention provides a preparation method for preparing a lithium ion positive electrode material. The metal salt of fatty acid is mixed with the positive electrode material for lithium battery, and it is prepared by high-temperature solid-phase reaction sintering. ℃, the sintering time is such as: but not limited to 1 hour to 24 hours.
另一种制备锂离子正极材料的制取方法,脂肪酸的金属盐与用于锂电池的正极材料进行混合。升温至200℃~1000℃烧结1小时~24小时,从而完成包覆材料与锂离子电池材料的固相反应。待烧结反应结束后,将材料进行分散和过筛,即可得到被均匀包覆的正极材料。Another preparation method for preparing a lithium ion positive electrode material is to mix a metal salt of a fatty acid with a positive electrode material for a lithium battery. The temperature is raised to 200°C to 1000°C and sintered for 1 hour to 24 hours, so as to complete the solid-phase reaction between the coating material and the lithium ion battery material. After the sintering reaction is completed, the material is dispersed and sieved to obtain a uniformly coated positive electrode material.
本发明提供的各种制取方法,依据制得正极材料中金属氧化物的含量(比如:0.6%±0.1%)相应确定金属盐的加入量。In the various preparation methods provided by the present invention, the addition amount of the metal salt is correspondingly determined according to the content of the metal oxide in the prepared positive electrode material (for example: 0.6%±0.1%).
另一种制备锂离子正极材料的制取方法,脂肪酸的金属盐与用于锂电池的正极材料进行混合,通过高温固相反应烧结制得,所得包覆的正极材料中,金属氧化物所占的质量百分比为:0.6%±0.1%,比如:0.5%、0.6%和0.7%。Another preparation method for preparing lithium ion positive electrode material, the metal salt of fatty acid is mixed with the positive electrode material for lithium battery, and it is prepared by high-temperature solid-phase reaction sintering, and in the obtained coated positive electrode material, the metal oxide accounts for The mass percentage is: 0.6% ± 0.1%, such as: 0.5%, 0.6% and 0.7%.
本发明提供的各种制取方法,在烧结过程中,通常按1℃/min~10℃/min的速率升温至200℃~1000℃后,再保温1小时~24小时。In the various preparation methods provided by the present invention, during the sintering process, the temperature is usually raised to 200°C to 1000°C at a rate of 1°C/min to 10°C/min, and then kept for 1 hour to 24 hours.
另一种制备锂离子正极材料的制取方法,硬脂酸铝或月桂酸铝与用于锂电池的正极材料进行混合,按1~10℃/min的速率升温至200℃~1000℃后,再保温1小时~24小时,从而完成包覆材料与锂离子电池材料的固相反应。待烧结反应结束后,将材料进行分散和过筛,即可得到被均匀包覆的正极材料。Another preparation method for preparing a lithium ion positive electrode material is that aluminum stearate or aluminum laurate is mixed with a positive electrode material for lithium batteries, and the temperature is raised to 200°C to 1000°C at a rate of 1 to 10°C/min. The temperature is maintained for another 1 to 24 hours, thereby completing the solid-phase reaction between the coating material and the lithium ion battery material. After the sintering reaction is completed, the material is dispersed and sieved to obtain a uniformly coated positive electrode material.
本发明的制备方法,其具体烧结温度与烧结时间根据所使用的脂肪酸盐的分解温度而定。In the preparation method of the present invention, the specific sintering temperature and sintering time are determined according to the decomposition temperature of the fatty acid salt used.
本发明所带来的有益效果是:The beneficial effects brought by the present invention are:
本发明通过使用脂肪酸的金属盐为包覆材料,通过高温固相反应可以直接在正极材料表 面进行均匀包覆,操作简单,成本低廉,非常适合大规模工业生产。反应结束后,除了在正极材料表面生成目标包覆物(如:金属氧化物)外,不会产生任何杂质,且材料中所含的包覆物量进一步下降,使得材料的性能进一步提高。By using the metal salt of fatty acid as the coating material, the present invention can directly carry out uniform coating on the surface of the positive electrode material through high-temperature solid-phase reaction, the operation is simple, the cost is low, and it is very suitable for large-scale industrial production. After the reaction, except for the target coating (such as metal oxide) formed on the surface of the positive electrode material, no impurities will be generated, and the amount of the coating contained in the material is further reduced, so that the performance of the material is further improved.
本发明提供的锂电池正极材料的制取方法,可以快速实现正极材料的均匀包覆,增强锂离子电池正极材料的界面稳定性,从而增强了材料的安全稳定性和循环寿命,与此同时显著改善电池材料经使用而发生的电阻升高情形。The preparation method of the positive electrode material of the lithium battery provided by the present invention can quickly realize the uniform coating of the positive electrode material, enhance the interface stability of the positive electrode material of the lithium ion battery, thereby enhancing the safety stability and cycle life of the material, and at the same time significantly Improve the resistance increase that occurs when the battery material is used.
附图说明Description of drawings
图1为硬脂酸镁TGA曲线图;Fig. 1 is magnesium stearate TGA curve figure;
图2为硬脂酸铝TGA曲线图;Fig. 2 is aluminum stearate TGA curve figure;
图3为月桂酸铝TGA曲线图;Fig. 3 is aluminum laurate TGA curve diagram;
图4为对比例1表面元素分析图;Fig. 4 is the surface element analysis diagram of comparative example 1;
图5为实施例1A、实施例1B和实施例1C制得材料的镁元素分布图;Fig. 5 is the magnesium distribution diagram of the materials prepared in Example 1A, Example 1B and Example 1C;
图6为对比例1、对比例2、实施例1A、实施例1B、实施例1C和实施例2的XRD图谱;6 is the XRD patterns of Comparative Example 1, Comparative Example 2, Example 1A, Example 1B, Example 1C and Example 2;
图7为对比例1、对比例2、实施例1A、实施例1B、实施例1C和实施例2制备的用于电池正极的材料的充放电曲线对比图;FIG. 7 is a comparison diagram of charge-discharge curves of materials for battery positive electrodes prepared in Comparative Example 1, Comparative Example 2, Example 1A, Example 1B, Example 1C and Example 2;
图8为对比例1、对比例2、实施例1A、实施例1B、实施例1C和实施例2制备的用于电池正极的材料循环过程中的DCIR变化对比图;FIG. 8 is a comparison diagram of DCIR changes during the cycle of materials for battery positive electrodes prepared in Comparative Example 1, Comparative Example 2, Example 1A, Example 1B, Example 1C and Example 2;
图9为对比例1、对比例2、和实施例2制备的用于电池正极的材料的循环性能测试对比图;9 is a comparison chart of the cycle performance test of the materials for battery positive electrodes prepared in Comparative Example 1, Comparative Example 2, and Example 2;
图10为对比例3、实施例3和实施例4的XRD图谱;Fig. 10 is the XRD pattern of comparative example 3, embodiment 3 and embodiment 4;
图11为对比例3、实施例3和实施例4制备的用于电池正极的材料的充放电曲线对比图;FIG. 11 is a comparison diagram of charge-discharge curves of the materials for battery positive electrodes prepared in Comparative Example 3, Example 3 and Example 4;
图12为对比例4、实施例5和实施例6的XRD图谱;Fig. 12 is the XRD pattern of comparative example 4, embodiment 5 and embodiment 6;
图13为对比例4、实施例5和实施例6制备的用于电池正极的材料的充放电曲线对比图;FIG. 13 is a comparison diagram of charge-discharge curves of the materials for battery positive electrodes prepared in Comparative Example 4, Example 5 and Example 6;
图14为对比例4和实施例5制备的用于电池正极的材料的循环性能测试对比图。FIG. 14 is a comparison chart of the cycle performance test of the materials for battery positive electrodes prepared in Comparative Example 4 and Example 5. FIG.
具体实施方式Detailed ways
以下结合附图详细描述本发明的技术方案。本发明实施例仅用以说明本发明的技术方案而非限制,尽管参照较佳实施例对本发明进行了详细说明,本领域的普通技术人员应当理解,可以对本发明的技术方案进行修改或者等同替换,而不脱离本发明技术方案的精神和范围,其均应涵盖在本发明的权利要求范围中。The technical solutions of the present invention are described in detail below with reference to the accompanying drawings. The embodiments of the present invention are only used to illustrate the technical solutions of the present invention and not to limit them. Although the present invention is described in detail with reference to the preferred embodiments, those of ordinary skill in the art should understand that the technical solutions of the present invention can be modified or equivalently replaced. , without departing from the spirit and scope of the technical solutions of the present invention, and should be included in the scope of the claims of the present invention.
本发明以下实施例所用的各项试验方法具体说明如下:The various test methods used in the following examples of the present invention are specifically described as follows:
1)X射线衍射(XRD)结构表征1) X-ray diffraction (XRD) structure characterization
X射线衍射的测试设备为布鲁克D2-XE-T,该仪器使用的靶材为铜靶,其X射线的波长为
Figure PCTCN2020132627-appb-000001
首先称取1g~2g样品,把样品尽量平铺在样品台中央位置,其次使用载玻片抹平,保证样品与样品槽平齐,并且保证无样品在凹槽外。最后将准备好的样品台放入布鲁克D2-XE-T中进行测试,X射线2θ的扫描范围设定为10°~80°,扫描步长为0.01°,并且每一步长的X射线曝光时间为0.1s。
The test equipment for X-ray diffraction is Bruker D2-XE-T, the target material used in this instrument is a copper target, and the X-ray wavelength is
Figure PCTCN2020132627-appb-000001
First, weigh 1g to 2g of sample, spread the sample as flat as possible in the center of the sample stage, and then use a glass slide to smooth it to ensure that the sample is flush with the sample groove and that no sample is outside the groove. Finally, put the prepared sample stage into Bruker D2-XE-T for testing. The scanning range of X-ray 2θ is set to 10°~80°, the scanning step is 0.01°, and the X-ray exposure time of each step is is 0.1s.
2)扫描电子显微镜(SEM)形貌表征2) Scanning electron microscope (SEM) morphology characterization
首先将少量粉末样品粘结至样品台的导电胶带上,保证样品分散均匀无团聚。然后将样品放入日本电子Joel JCM-7000 NeoScope台式扫描电子显微镜中进行观测。采用Joel JED-2300型能谱仪对颗粒截面的元素进行分析,并采集能量色散X射线光谱(EDS)数据。First, a small amount of powder sample is bonded to the conductive tape of the sample stage to ensure that the sample is evenly dispersed without agglomeration. The samples were then placed in a Nippon Electronics Joel JCM-7000 NeoScope desktop scanning electron microscope for observation. The elements of the particle cross section were analyzed by Joel JED-2300 energy dispersive spectrometer, and energy dispersive X-ray spectroscopy (EDS) data were collected.
3)电化学性能测试3) Electrochemical performance test
将制成的锂离子电池正极材料与导电剂(如:炭黑)、粘结剂(如:聚偏氟乙烯)和溶剂(如:N-甲基吡咯烷酮)混合后制备成电极浆料,而后涂布于铝基集流体,干燥后制备成为电极,并将电极组装成为纽扣电池,并使用新威Neware(CT-4008)电池充放电仪进行电化学测试。将纽扣电池首先使用0.1C的电流在2.75-4.4V之间循环4圈化成,之后在相同电压区间内使用0.2C或0.5C的电流进行循环测试。The prepared lithium ion battery cathode material is mixed with a conductive agent (such as: carbon black), a binder (such as: polyvinylidene fluoride) and a solvent (such as: N-methylpyrrolidone) to prepare an electrode slurry, and then It was coated on an aluminum-based current collector, dried to prepare an electrode, and the electrode was assembled into a button battery, and electrochemical tests were carried out using a Neware (CT-4008) battery charge-discharge instrument. The coin cell battery was firstly cycled between 2.75-4.4V with a current of 0.1C for 4 turns, and then the cycle test was performed with a current of 0.2C or 0.5C in the same voltage range.
在对纽扣电池进行循环测试的同时,也同时测试纽扣电池的放电直流电阻(Direct Current Internal Resistance,DCIR)。At the same time as the cyclic test of the button battery, the discharge DC resistance (DCIR) of the button battery is also tested.
仪器计算DCIR的方法为:充电工步结束后,下一个工步为搁置工步,将搁置工步最后一个点的电压(V 1)进行记录。搁置工步结束后,下一个工步为放电工步,使用恒电流(I)对电池进行放电,同时将放电工步第一个点的电压(V 2)进行记录。DCIR计算公式为:DCIR=(V 1-V 2)/I The method for the instrument to calculate the DCIR is: after the charging step is over, the next step is the shelving step, and the voltage (V 1 ) at the last point of the shelving step is recorded. After the shelving step is over, the next step is the discharge step, the battery is discharged with a constant current (I), and the voltage (V 2 ) at the first point of the discharge step is recorded at the same time. The calculation formula of DCIR is: DCIR=(V 1 -V 2 )/I
4)热重分析测试(TGA)4) Thermogravimetric Analysis Test (TGA)
对所使用的脂肪酸盐进行热重分析,测试所使用的仪器为PerkinElmer-STA-8000。首先秤取6mg~20mg脂肪酸盐放入坩埚内并加盖坩埚盖子,将盛有脂肪酸盐的坩埚与另外一个空坩埚同时放入仪器炉内。其次,向炉内冲入氧气作为反应气氛,并且使用氩气作为炉体保护气,使用5℃/min的加热速率加热至800摄氏度对材料进行热重分析实验。Thermogravimetric analysis of the fatty acid salts used was performed on a PerkinElmer-STA-8000 instrument. First, weigh 6 mg to 20 mg of fatty acid salt into the crucible and put the crucible lid on it. Put the crucible containing the fatty acid salt and another empty crucible into the instrument furnace at the same time. Next, oxygen was injected into the furnace as the reaction atmosphere, and argon was used as the protective gas of the furnace body, and the material was heated to 800 degrees Celsius with a heating rate of 5°C/min to conduct a thermogravimetric analysis experiment on the material.
对比例1Comparative Example 1
本对比例所使用的正极材料NCM523的化学式为LiNi 0.5Co 0.2Mn 0.3O 2,该材料没有经过任何包覆处理。 The chemical formula of the positive electrode material NCM523 used in this comparative example is LiNi 0.5 Co 0.2 Mn 0.3 O 2 , and the material has not undergone any coating treatment.
对该对比例样品进行XRD以及SEM与EDS表征,电化学循环寿命以及DCIR的测试。The comparative samples were characterized by XRD, SEM and EDS, electrochemical cycle life and DCIR tests.
对比例2Comparative Example 2
本对比例所使用的正极材料NCM523的化学式为LiNi 0.5Co 0.2Mn 0.3O 2,同时使用硬脂酸和纳米氧化铝(Al 2O 3),Al 2O 3颗粒尺度在20-30纳米之间的混合物作为包覆材料对NCM523进行包覆实验。 The chemical formula of the positive electrode material NCM523 used in this comparative example is LiNi 0.5 Co 0.2 Mn 0.3 O 2 , and stearic acid and nano-alumina (Al 2 O 3 ) are used at the same time, and the Al 2 O 3 particle size is between 20-30 nanometers The mixture of NCM523 was used as the coating material to conduct coating experiments on NCM523.
首先制备3g硬脂酸与纳米Al 2O 3的混合物,其中硬脂酸的质量百分比控制在3%~30%。在上述混合物中再加入10g到30g的球磨珠进行高速球磨,球磨时间设为1小时~5小时,球磨速度设置为100到600rmp。混合结束后,收集硬脂酸和纳米Al 2O 3的混合物,即包覆材料。取用适量NCM523,加入相应的包覆材料(即硬脂酸和纳米Al 2O 3混合物),实现Al 2O 3的质量百分比为0.5%。将NCM523与包覆前驱体放入混合机中,混合1到8个小时。将上述混合物以1℃/min~10℃/min的速率升温至200℃~1000℃,并在该温度保持1小时~24小时然后随炉冷却到室温完成包覆工艺。对该对比例样品进行电化学循环寿命以及DCIR的测试。 First, a mixture of 3 g of stearic acid and nano-Al 2 O 3 is prepared, wherein the mass percentage of stearic acid is controlled at 3% to 30%. 10g to 30g of ball milling beads are added to the above mixture for high-speed ball milling, the ball milling time is set to 1 hour to 5 hours, and the ball milling speed is set to 100 to 600 rmp. After the mixing, the mixture of stearic acid and nano-Al 2 O 3 was collected, that is, the coating material. An appropriate amount of NCM523 was taken, and the corresponding coating material (ie a mixture of stearic acid and nano-Al 2 O 3 ) was added to achieve a mass percentage of Al 2 O 3 of 0.5%. The NCM523 and the coating precursor are placed in a mixer and mixed for 1 to 8 hours. The above mixture is heated to 200°C to 1000°C at a rate of 1°C/min to 10°C/min, maintained at this temperature for 1 to 24 hours, and then cooled to room temperature with the furnace to complete the coating process. The comparative samples were tested for electrochemical cycle life and DCIR.
对比例3Comparative Example 3
本对比例所使用的正极材料NCM622的化学式为LiNi 0.6Co 0.2Mn 0.2O 2,该材料没有经过任何包覆处理。 The chemical formula of the positive electrode material NCM622 used in this comparative example is LiNi 0.6 Co 0.2 Mn 0.2 O 2 , and the material has not undergone any coating treatment.
对该对比例样品进行XRD、SEM和EDS表征,电化学循环寿命以及DCIR的测试。The comparative samples were characterized by XRD, SEM and EDS, electrochemical cycle life and DCIR tests.
对比例4Comparative Example 4
本对比例所使用的正极材料NCM811的化学式为LiNi 0.8Co 0.1Mn 0.1O 2,该材料没有经过任何包覆处理。 The chemical formula of the positive electrode material NCM811 used in this comparative example is LiNi 0.8 Co 0.1 Mn 0.1 O 2 , and the material has not undergone any coating treatment.
对该对比例样品进行XRD以及SEM与EDS表征,电化学循环寿命以及DCIR的测试。The comparative samples were characterized by XRD, SEM and EDS, electrochemical cycle life and DCIR tests.
实施例1Example 1
本实施例中所使用的正极材料为与对比例1相同的NCM523,其化学式为LiNi 0.5Co 0.2Mn 0.3O 2,所使用的脂肪酸盐为硬脂酸镁(C 36H 70MgO 4)。 The positive electrode material used in this example is the same NCM523 as in Comparative Example 1, its chemical formula is LiNi 0.5 Co 0.2 Mn 0.3 O 2 , and the fatty acid salt used is magnesium stearate (C 36 H 70 MgO 4 ).
取适量NCM523和硬脂酸镁放入混合机中,混合搅拌8小时,让NCM523和硬脂酸镁得到充分混合。Put an appropriate amount of NCM523 and magnesium stearate into a mixer, mix and stir for 8 hours, so that NCM523 and magnesium stearate are fully mixed.
将上述混合物以5℃/min的速率升温至650℃,并保持10小时。然后随炉冷却到室温,将烧结制备的上述材料分散和过筛,从而得到最终包覆的正极材料,完成包覆实验。The above mixture was heated to 650°C at a rate of 5°C/min and held for 10 hours. After cooling to room temperature with the furnace, the above-mentioned materials prepared by sintering are dispersed and sieved to obtain the final coated positive electrode material, and the coating experiment is completed.
硬脂酸镁的加入量是相当于上述对比例中氧化镁的含量折算得到。本实施例中最终制备了氧化镁包覆NCM523的质量百分比为:0.5%(标记为:实施例1A),1%(标记为:实施例1B)和2%(标记为:实施例1C)。The addition of magnesium stearate is equivalent to the content of magnesium oxide in the above-mentioned comparative example and is converted. In this example, the mass percentages of magnesium oxide-coated NCM523 finally prepared are: 0.5% (marked as: Example 1A), 1% (marked as: Example 1B) and 2% (marked as: Example 1C).
对制备合成的样品进行XRD、SEM与EDS表征,电化学循环寿命以及DCIR的测试。The synthesized samples were characterized by XRD, SEM and EDS, electrochemical cycle life and DCIR tests.
实施例2Example 2
本实施例中所使用的正极材料为与对比例1相同的NCM523,其化学式为LiNi 0.5Co 0.2Mn 0.3O 2,所使用的脂肪酸盐为硬脂酸铝(C 54H 105AlO 6)。 The positive electrode material used in this example is the same NCM523 as in Comparative Example 1, its chemical formula is LiNi 0.5 Co 0.2 Mn 0.3 O 2 , and the fatty acid salt used is aluminum stearate (C 54 H 105 AlO 6 ).
取适量NCM523和硬脂酸铝放入混合机中,混合搅拌8小时,让NCM523和硬脂酸铝得到充分混合。Put an appropriate amount of NCM523 and aluminum stearate into a mixer, mix and stir for 8 hours, so that NCM523 and aluminum stearate are fully mixed.
将上述混合物以5℃/min的速率升温至650℃,并保持10小时。然后随炉冷却到室温, 将烧结制备的上述材料分散和过筛,从而得到最终包覆的正极材料,完成包覆实验。The above mixture was heated to 650°C at a rate of 5°C/min and held for 10 hours. After cooling to room temperature with the furnace, the above-mentioned materials prepared by sintering are dispersed and sieved to obtain the final coated positive electrode material, and the coating experiment is completed.
硬脂酸铝的加入量是相当于上述对比例中氧化铝的含量折算得到。本实施例中最终制备了氧化铝包覆NCM523的质量百分比为0.5%。The added amount of aluminum stearate is equivalent to the content of aluminum oxide in the above-mentioned comparative example. In this example, the mass percentage of alumina-coated NCM523 is finally 0.5%.
对制备合成的样品进行XRD、SEM与EDS表征,电化学循环寿命以及DCIR的测试。The synthesized samples were characterized by XRD, SEM and EDS, electrochemical cycle life and DCIR tests.
实施例3Example 3
本实施例中所使用的正极材料为与对比例3相同的NCM622,其化学式为LiNi 0.6Co 0.2Mn 0.2O 2,所使用的脂肪酸盐为硬脂酸铝(C 54H 105AlO 6)。 The positive electrode material used in this example is the same NCM622 as in Comparative Example 3, its chemical formula is LiNi 0.6 Co 0.2 Mn 0.2 O 2 , and the fatty acid salt used is aluminum stearate (C 54 H 105 AlO 6 ).
取适量NCM622和硬脂酸铝放入混合机中,混合搅拌8小时,让NCM622和硬脂酸铝得到充分混合。Put an appropriate amount of NCM622 and aluminum stearate into a mixer, mix and stir for 8 hours, so that NCM622 and aluminum stearate are fully mixed.
将上述混合物以5℃/min的速率升温至650℃,并保持10小时。然后随炉冷却到室温,将烧结制备的上述材料分散和过筛,从而得到最终包覆的正极材料,完成包覆实验。The above mixture was heated to 650°C at a rate of 5°C/min and held for 10 hours. After cooling to room temperature with the furnace, the above-mentioned materials prepared by sintering are dispersed and sieved to obtain the final coated positive electrode material, and the coating experiment is completed.
硬脂酸铝的加入量是相当于上述对比例中氧化铝的含量折算得到。本实施例中最终制备了氧化铝包覆NCM622的质量百分比为0.5%。The added amount of aluminum stearate is equivalent to the content of aluminum oxide in the above-mentioned comparative example. In this example, the mass percentage of alumina-coated NCM622 is finally 0.5%.
对制备合成的样品进行XRD、SEM与EDS表征,电化学循环寿命以及DCIR的测试。The synthesized samples were characterized by XRD, SEM and EDS, electrochemical cycle life and DCIR tests.
实施例4Example 4
本实施例中所使用的正极材料为与对比例3相同的NCM622,其化学式为LiNi 0.6Co 0.2Mn 0.2O 2,所使用的脂肪酸盐为月桂酸铝(C 36H 69AlO 6)。 The positive electrode material used in this example is the same NCM622 as in Comparative Example 3, its chemical formula is LiNi 0.6 Co 0.2 Mn 0.2 O 2 , and the fatty acid salt used is aluminum laurate (C 36 H 69 AlO 6 ).
取适量NCM622和月桂酸铝放入混合机中,混合搅拌8小时,让NCM622和月桂酸铝得到充分混合。Put an appropriate amount of NCM622 and aluminum laurate into the mixer, mix and stir for 8 hours, so that NCM622 and aluminum laurate are fully mixed.
将上述混合物以5℃/min的速率升温至500℃,并保持10小时~24小时。然后随炉冷却到室温,将烧结制备的上述材料分散和过筛,从而得到最终包覆的正极材料,完成包覆实验。The above mixture was heated to 500°C at a rate of 5°C/min and held for 10 to 24 hours. After cooling to room temperature with the furnace, the above-mentioned materials prepared by sintering are dispersed and sieved to obtain the final coated positive electrode material, and the coating experiment is completed.
月桂酸铝的加入量是相当于上述对比例中氧化铝的含量折算得到。本实施例中最终制备了氧化铝包覆NCM622的质量百分比为0.5%。The added amount of aluminum laurate is equivalent to the content of alumina in the above-mentioned comparative example. In this example, the mass percentage of alumina-coated NCM622 is finally 0.5%.
对制备合成的样品进行XRD、SEM与EDS表征,电化学循环寿命以及DCIR的测试。The synthesized samples were characterized by XRD, SEM and EDS, electrochemical cycle life and DCIR tests.
实施例5Example 5
本实施例中所使用的正极材料为与对比例4相同的NCM811,其化学式为LiNi 0.8Co 0.1Mn 0.1O 2,所使用的脂肪酸盐为硬脂酸铝(C 54H 105AlO 6)。 The positive electrode material used in this example is the same NCM811 as in Comparative Example 4, its chemical formula is LiNi 0.8 Co 0.1 Mn 0.1 O 2 , and the fatty acid salt used is aluminum stearate (C 54 H 105 AlO 6 ).
取适量NCM811和硬脂酸铝放入混合机中,混合搅拌8小时,让NCM811和硬脂酸铝得到充分混合。Put an appropriate amount of NCM811 and aluminum stearate into the mixer, mix and stir for 8 hours, so that NCM811 and aluminum stearate are fully mixed.
将上述混合物以5℃/min的速率升温至650℃,并保持10小时。然后随炉冷却到室温,将烧结制备的上述材料分散和过筛,从而得到最终包覆的正极材料,完成包覆实验。The above mixture was heated to 650°C at a rate of 5°C/min and held for 10 hours. After cooling to room temperature with the furnace, the above-mentioned materials prepared by sintering are dispersed and sieved to obtain the final coated positive electrode material, and the coating experiment is completed.
硬脂酸铝的加入量是相当于上述对比例中氧化铝的含量折算得到。本实施例中最终制备了氧化铝包覆NCM811的质量百分比为0.25%。The added amount of aluminum stearate is equivalent to the content of aluminum oxide in the above-mentioned comparative example. In this example, the mass percentage of alumina-coated NCM811 is finally 0.25%.
对制备合成的样品进行XRD、SEM与EDS表征,电化学循环寿命以及DCIR的测试。The synthesized samples were characterized by XRD, SEM and EDS, electrochemical cycle life and DCIR tests.
实施例6Example 6
本实施例中所使用的正极材料为与对比例4相同的NCM811,其化学式为LiNi 0.8Co 0.1Mn 0.1O 2,所使用的脂肪酸盐为硬脂酸镁(C 36H 70MgO 4)。 The positive electrode material used in this example is the same NCM811 as in Comparative Example 4, its chemical formula is LiNi 0.8 Co 0.1 Mn 0.1 O 2 , and the fatty acid salt used is magnesium stearate (C 36 H 70 MgO 4 ).
取适量NCM811和硬脂酸镁放入混合机中,混合搅拌8小时,让NCM811和硬脂酸镁得到充分混合。Take an appropriate amount of NCM811 and magnesium stearate into the mixer, mix and stir for 8 hours, so that NCM811 and magnesium stearate are fully mixed.
将上述混合物以5℃/min的速率升温至650℃,并保持10小时。然后随炉冷却到室温,将烧结制备的上述材料分散和过筛,从而得到最终包覆的正极材料,完成包覆实验。The above mixture was heated to 650°C at a rate of 5°C/min and held for 10 hours. After cooling to room temperature with the furnace, the above-mentioned materials prepared by sintering are dispersed and sieved to obtain the final coated positive electrode material, and the coating experiment is completed.
硬脂酸镁的加入量是相当于上述对比例中氧化镁的含量折算得到。本实施例中最终制备了氧化镁包覆NCM811的质量百分比为0.25%。The addition of magnesium stearate is equivalent to the content of magnesium oxide in the above-mentioned comparative example and is converted. In this example, the mass percentage of magnesium oxide-coated NCM811 was finally prepared to be 0.25%.
对制备合成的样品进行XRD、SEM与EDS表征,电化学循环寿命以及DCIR的测试。The synthesized samples were characterized by XRD, SEM and EDS, electrochemical cycle life and DCIR tests.
本发明上述实施例中,使用了三种脂肪酸盐作为示例,分别为:硬脂酸镁,硬脂酸铝和月桂酸铝。对这三种脂肪酸盐的TGA结果如图1~图3所示。三种脂肪酸盐在热重分析的实验中,都会随着加热温度的升高而进行分解。当加热温度足够高时,脂肪酸盐的重量将保持不变,经过计算所有脂肪酸盐都会最终转变成为对应的金属氧化物:当温度大于650℃时,硬脂酸镁将最终变成氧化镁(如图1所示),硬脂酸铝将最终变成氧化铝(如图2所示);当温度大于500℃时,月桂酸铝将最终变成氧化铝(如图3所示)。通过热重分析可以得知使用脂肪酸盐进行固相反应包覆正极材料所需要的反应温度。In the above embodiments of the present invention, three fatty acid salts are used as examples, namely: magnesium stearate, aluminum stearate and aluminum laurate. The TGA results for these three fatty acid salts are shown in FIGS. 1 to 3 . In the experiment of thermogravimetric analysis, all three fatty acid salts decomposed with the increase of heating temperature. When the heating temperature is high enough, the weight of the fatty acid salt will remain unchanged, and all fatty acid salts will eventually be converted into the corresponding metal oxides after calculation: when the temperature is greater than 650 ℃, magnesium stearate will eventually become magnesium oxide (as shown in Figure 1), aluminum stearate will eventually become alumina (as shown in Figure 2); when the temperature is greater than 500 °C, aluminum laurate will eventually become alumina (as shown in Figure 3). Through thermogravimetric analysis, the reaction temperature required for the solid-phase reaction coating of the positive electrode material with the fatty acid salt can be known.
将对比例1进行SEM/EDS表征,如图4所示,对比例1中只检测到NCM523的主量元素镍、钴和锰,未检测到其他金属元素,表明对比例1为未包覆的NCM523不具有镁元素。将使用硬脂酸镁包覆的NCM523进行SEM/EDS(即实施例1A,实施例1B和实施例1C),同时可以发现主量元素镍,钴,锰,同时可以观测到包覆后的氧化镁中的镁元素,如图5所示,其中实施例1A,实施例1B和实施例1C中的镁元素都均匀分布在正极材料颗粒表面,并且随着包覆材料用量的增多,Mg的信号逐渐增强,证明MgO的包覆量逐渐增多。The SEM/EDS characterization of Comparative Example 1 was carried out. As shown in Figure 4, only the main elements nickel, cobalt and manganese of NCM523 were detected in Comparative Example 1, and no other metal elements were detected, indicating that Comparative Example 1 was uncoated NCM523 does not have magnesium. The NCM523 coated with magnesium stearate was subjected to SEM/EDS (i.e., Example 1A, Example 1B and Example 1C), and the main elements nickel, cobalt, and manganese could be found at the same time, and the oxidation after coating could be observed at the same time. The magnesium element in magnesium, as shown in Figure 5, wherein the magnesium element in Example 1A, Example 1B and Example 1C are uniformly distributed on the surface of the positive electrode material particles, and with the increase of the amount of coating material, the signal of Mg It is gradually enhanced, which proves that the coating amount of MgO gradually increases.
如图6XRD数据所示,未包覆的NCM523(即对比例1)是纯R-3m层状结构。同时使用脂肪酸盐从而形成氧化物包覆的NCM523(即实施例1A、实施例1B、实施例1C和实施例2)经XRD表征,也是纯R-3m层状结构。数据表明使用脂肪酸盐进行包覆的NCM523不会产生任何杂相。因此使用脂肪酸盐在包覆的过程中不会因为引入杂相,而对原有正极材料产生影响。As shown in the XRD data of Figure 6, the uncoated NCM523 (ie, Comparative Example 1) is a pure R-3m layered structure. Simultaneously using fatty acid salts to form oxide-coated NCM523 (ie, Example 1A, Example 1B, Example 1C, and Example 2), characterized by XRD, it is also a pure R-3m layered structure. The data show that NCM523 coated with fatty acid salts does not generate any impurity phase. Therefore, the use of fatty acid salts will not affect the original positive electrode material due to the introduction of impurity phases during the coating process.
将未包覆的NCM523以及使用脂肪酸盐包覆NCM523的电化学性能进行对比。由于包覆材料为氧化物没有电化学活性,所以随着包覆物质量的增加,正极材料的充放电容量将有所下降。将三个实施例与对比例1的充放电曲线比对如图7所示,随着包覆MgO含量的增多,NCM523的充放电容量在逐渐下降。其中实施例1A的充放电容量与对比例1相当。同时MgO包覆的NCM523与未包覆的NCM523相比,在循环过程中也表现出较小的电阻增长,如图8所示,证明使用脂肪酸盐包覆的正极材料,在电化学测试中体现出较高的界面稳定性。表格 1汇总了上述各个样品的能量保持率,经过50个循环,所有使用硬脂酸镁包覆的NCM523跟未包覆的NCM523相比都拥有较高的能量保持率,其中以0.5%MgO包覆的NCM523,拥有最高的能量保持率94.3%。通过对比初始充放电容量,直流电阻增长状况以及能量保持率,使用硬脂酸镁实现0.5%MgO包覆的NCM523(实施例1A)为最优的包覆条件。因此依然采取0.5%氧化物的包覆总量,使用硬脂酸铝对NCM523进行包覆得到实施例2。同时将使用硬脂酸和氧化铝对NCM523进行包覆得到对比例2。The electrochemical performance of uncoated NCM523 and NCM523 coated with fatty acid salts were compared. Since the coating material is an oxide and has no electrochemical activity, the charge-discharge capacity of the positive electrode material will decrease with the increase of the quality of the coating material. The charge-discharge curves of the three examples and Comparative Example 1 are compared as shown in Figure 7. As the content of MgO coating increases, the charge-discharge capacity of NCM523 gradually decreases. The charge-discharge capacity of Example 1A is comparable to that of Comparative Example 1. At the same time, compared with the uncoated NCM523, the MgO-coated NCM523 also showed a smaller increase in resistance during cycling, as shown in Fig. It shows high interface stability. Table 1 summarizes the energy retention rate of each of the above samples. After 50 cycles, all NCM523 coated with magnesium stearate have higher energy retention rate compared with the uncoated NCM523, which is coated with 0.5% MgO. The covered NCM523 has the highest energy retention rate of 94.3%. By comparing the initial charge-discharge capacity, DC resistance growth and energy retention rate, NCM523 (Example 1A) using magnesium stearate to achieve 0.5% MgO coating is the optimal coating condition. Therefore, the total coating amount of 0.5% oxide is still taken, and NCM523 is coated with aluminum stearate to obtain Example 2. At the same time, NCM523 was coated with stearic acid and alumina to obtain Comparative Example 2.
将对比例1,对比例2以及实施例2进行对比。经XRD检测可知,对比例1,对比例2以及实施例2均为纯R-3m层状结构(参见图6),未发现任何杂质。对三者进行电化学测试可知,对比例1,对比例2以及实施例2都拥有相当的初始充放电容量(参见图7);其中实施例2的直流电阻增长增幅最小(参见图8)。在循环50次后,实施例2的能量保持率可以达到95.3%,为其中能量保持率最高的样品。如图9所示,将实施例2与对比例2的能量保持率进行对比,实施例2拥有更好的能量保持率。从正极材料电阻增长幅度以及能量保持率的对比可知,使用硬脂酸铝对NCM523直接进行包覆与使用硬脂酸和氧化铝对NCM523进行包覆的效果对比来看,直接使用脂肪酸铝对正极材料进行包覆的效果更好,并实现了进一步降低包覆材料用量的目的。Comparative Example 1, Comparative Example 2 and Example 2 were compared. The XRD test shows that Comparative Example 1, Comparative Example 2 and Example 2 are all pure R-3m layered structures (see FIG. 6 ), and no impurities are found. The electrochemical test of the three shows that Comparative Example 1, Comparative Example 2 and Example 2 all have comparable initial charge and discharge capacities (see Figure 7); among them, Example 2 has the smallest increase in DC resistance (see Figure 8). After 50 cycles, the energy retention rate of Example 2 can reach 95.3%, which is the sample with the highest energy retention rate. As shown in FIG. 9 , comparing the energy retention rates of Example 2 and Comparative Example 2, Example 2 has a better energy retention rate. From the comparison of the resistance growth rate and the energy retention rate of the positive electrode material, it can be seen from the comparison of the effect of using aluminum stearate to directly coat NCM523 and using stearic acid and aluminum oxide to coat NCM523 directly. The effect of coating the material is better, and the purpose of further reducing the amount of coating material is achieved.
如图10中的XRD数据所示,未包覆的NCM622(对比例3)是纯R-3m层状结构。使用硬脂酸铝和月桂酸铝作为脂肪酸盐对于NCM622进行0.5%Al 2O 3包覆得到实施例3和实施例4,经XRD表征,同样也是纯R-3m层状结构。数据表明使用硬脂酸铝和月桂酸铝作为脂肪酸盐进行包覆的NCM622不会产生任何杂相。因此使用脂肪酸盐在包覆的过程中不会因为引入杂相,而对原有正极材料产生影响。 As shown by the XRD data in Figure 10, the uncoated NCM622 (Comparative Example 3) is a pure R-3m layered structure. Using aluminum stearate and aluminum laurate as fatty acid salts to carry out 0.5% Al 2 O 3 coating on NCM622 to obtain Example 3 and Example 4, which are also pure R-3m layered structure through XRD characterization. The data show that NCM622 coated with aluminum stearate and aluminum laurate as fatty acid salts does not produce any impurity phase. Therefore, the use of fatty acid salts will not affect the original positive electrode material due to the introduction of impurity phases during the coating process.
将对比例3与实施例3和实施例4的电化学性能进行对比。由于包覆材料为氧化物没有电化学活性,所以随着包覆物质量的增加,正极材料的充放电容量将有所下降。对比例3、实施例3和实施例4的充放电曲线对比情况参见图11,实施例3和实施例4的充放电容量相对于对比例3有小幅下降。循环50次后,实施例3与实施例4的能量保持率分别可以达到92.2%和90.8%,均高于对比例3的89.2%。由表1可知,循环50次后,实施例3与实施例4的电阻可以达到25.9ohm和30.98ohm,均低于对比例3的31.76ohm。The electrochemical performance of Comparative Example 3 was compared with that of Examples 3 and 4. Since the coating material is an oxide and has no electrochemical activity, the charge-discharge capacity of the positive electrode material will decrease with the increase of the quality of the coating material. Figure 11 shows the comparison of the charge-discharge curves of Comparative Example 3, Example 3 and Example 4. The charge-discharge capacity of Example 3 and Example 4 is slightly lower than that of Comparative Example 3. After 50 cycles, the energy retention rates of Example 3 and Example 4 can reach 92.2% and 90.8%, respectively, which are higher than 89.2% of Comparative Example 3. It can be seen from Table 1 that after 50 cycles, the resistances of Example 3 and Example 4 can reach 25.9 ohm and 30.98 ohm, which are both lower than the 31.76 ohm of Comparative Example 3.
如图12中的XRD数据所示,未包覆的NCM811(对比例4)是纯R-3m层状结构。并且使用硬脂酸铝和硬脂酸镁作为脂肪酸盐对于NCM811进行0.25%Al 2O 3和MgO包覆得到实施例5和实施例6,经XRD表征,同样也是纯R-3m层状结构。数据表明使用硬脂酸铝和硬脂酸镁作为脂肪酸盐进行包覆的NCM811不会产生任何杂相。因此使用脂肪酸盐在包覆的过程中不会因为引入杂相,而对原有正极材料产生影响。 As shown by the XRD data in Figure 12, the uncoated NCM811 (Comparative Example 4) is a pure R-3m layered structure. And using aluminum stearate and magnesium stearate as fatty acid salts, NCM811 was coated with 0.25% Al 2 O 3 and MgO to obtain Examples 5 and 6, which were characterized by XRD and were also pure R-3m layered structure. . The data show that NCM811 coated with aluminum stearate and magnesium stearate as fatty acid salts does not produce any impurity phase. Therefore, the use of fatty acid salts will not affect the original positive electrode material due to the introduction of impurity phases during the coating process.
将对比例4与实施例5和实施例6的电化学性能进行对比。虽然包覆材料为氧化物没有电化学活性,但是0.25%的包覆物质量,对于正极材料NCM811的充放电容量几乎没有影响。对比例4,实施例5和实施例6的充放电曲线对比参见图13。经过50个循环,实施例5与实施例6的能量保持率分别可以达到88.3%和85.6%,均高于对比例4的85.5%,但与实施例3和实施例4相比,数值降低,表明在能量保持率方面,不及实施例3和实施例4。图14将实施例5与对比例4的放电容量进行对比,实施例5的放电容量保持率优于对比例4。The electrochemical performance of Comparative Example 4 was compared with that of Examples 5 and 6. Although the coating material is an oxide and has no electrochemical activity, the mass of the coating material of 0.25% has little effect on the charge-discharge capacity of the positive electrode material NCM811. For the comparison of the charge-discharge curves of Comparative Example 4, Example 5 and Example 6, see FIG. 13 . After 50 cycles, the energy retention rates of Example 5 and Example 6 can reach 88.3% and 85.6%, respectively, which are higher than 85.5% of Comparative Example 4, but compared with Example 3 and Example 4, the value is lower, It is shown that it is inferior to Example 3 and Example 4 in terms of energy retention. FIG. 14 compares the discharge capacity of Example 5 and Comparative Example 4, and the discharge capacity retention rate of Example 5 is better than that of Comparative Example 4.
表1 各种经包覆与未包覆正极材料循环50圈后能量保持率Table 1 Energy retention rate of various coated and uncoated cathode materials after 50 cycles
Figure PCTCN2020132627-appb-000002
Figure PCTCN2020132627-appb-000002

Claims (10)

  1. 一种锂离子电池正极材料的制取方法,其特征在于采用脂肪酸的金属盐与用于锂电池正极材料相混,通过高温固相反应烧结制得经包覆的正极材料,所述的脂肪酸的金属盐如式Me t+[CH 3(CH 2) nCOO] t所示,其中,n为8至32的整数,t为1至7的整数,Me为金属离子。 A method for preparing a positive electrode material for a lithium ion battery, which is characterized in that a metal salt of a fatty acid is mixed with a positive electrode material for a lithium battery, and a coated positive electrode material is obtained by high-temperature solid-phase reaction sintering. The metal salt is represented by the formula Me t+ [CH 3 (CH 2 ) n COO] t , wherein n is an integer from 8 to 32, t is an integer from 1 to 7, and Me is a metal ion.
  2. 根据权利要求1所述的制取方法,其特征在于所述的所述的n为8、9、10、11、12、13、14、15、16、17、18、19、20、21、22、23、24、25、26、27、28、29、30、31或32。The preparation method according to claim 1, wherein said n is 8, 9, 10, 11, 12, 13, 14, 15, 16, 17, 18, 19, 20, 21, 22, 23, 24, 25, 26, 27, 28, 29, 30, 31 or 32.
  3. 根据权利要求1所述的制取方法,其特征在于所述的金属离子选自于Li,Mg,Zn,Cu,Ca,Fe,Al,Ni,Co,Mn,Ti,Cr,Zr,Nb和W之一种或几种金属所成的离子。The preparation method according to claim 1, wherein the metal ions are selected from Li, Mg, Zn, Cu, Ca, Fe, Al, Ni, Co, Mn, Ti, Cr, Zr, Nb and An ion composed of one or more metals of W.
  4. 根据权利要求1所述的制取方法,其特征在于所述的脂肪酸在加热过程中挥发,所述的金属盐则在高温下被氧化,形成金属氧化物,所述包覆的正极材料中,所述的金属氧化物所占的质量百分比为0.6%±0.1%。The preparation method according to claim 1, wherein the fatty acid is volatilized during the heating process, and the metal salt is oxidized at high temperature to form a metal oxide, and in the coated positive electrode material, The mass percentage of the metal oxide is 0.6%±0.1%.
  5. 根据权利要求1所述的制取方法,其特征在于所述的脂肪酸的金属盐选自于硬脂酸铝和月桂酸铝。The preparation method according to claim 1, wherein the metal salt of the fatty acid is selected from aluminum stearate and aluminum laurate.
  6. 根据权利要求1所述的制取方法,其特征在于所述的脂肪酸的金属盐选自于硬脂酸镁和月桂酸镁。The preparation method according to claim 1, wherein the metal salt of the fatty acid is selected from magnesium stearate and magnesium laurate.
  7. 根据权利要求1所述的制取方法,其特征在于所述的固相反应升温至200℃~1000℃烧结1小时~24小时。The preparation method according to claim 1, wherein the solid-phase reaction is heated to 200°C to 1000°C and sintered for 1 hour to 24 hours.
  8. 根据权利要求1所述的制取方法,其特征在于所述的固相反应按1℃/min~10℃/min的速率升温至200℃~1000℃后,再保温1小时~24小时。The preparation method according to claim 1, wherein the solid-phase reaction is heated to 200°C to 1000°C at a rate of 1°C/min to 10°C/min, and then incubated for 1 hour to 24 hours.
  9. 根据权利要求1所述的制取方法,其特征在于所述的脂肪酸的金属盐,其形态为固体粉末,粒径为10nm~2μm。The preparation method according to claim 1, wherein the metal salt of the fatty acid is in the form of a solid powder, and the particle size is 10 nm to 2 μm.
  10. 根据权利要求1所述的制取方法,其特征在于所述的用于锂电池正极材料选自于NCM622、NCM811和NCA之一种或几种。The preparation method according to claim 1, wherein the cathode material for lithium battery is selected from one or more of NCM622, NCM811 and NCA.
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