WO2024011754A1 - 基于改性正极材料的破碎方法、改性正极材料及其制备方法 - Google Patents

基于改性正极材料的破碎方法、改性正极材料及其制备方法 Download PDF

Info

Publication number
WO2024011754A1
WO2024011754A1 PCT/CN2022/121028 CN2022121028W WO2024011754A1 WO 2024011754 A1 WO2024011754 A1 WO 2024011754A1 CN 2022121028 W CN2022121028 W CN 2022121028W WO 2024011754 A1 WO2024011754 A1 WO 2024011754A1
Authority
WO
WIPO (PCT)
Prior art keywords
crushing
crusher
cathode material
calcined
modified
Prior art date
Application number
PCT/CN2022/121028
Other languages
English (en)
French (fr)
Inventor
余海军
李爱霞
谢英豪
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
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 filed Critical 广东邦普循环科技有限公司
Publication of WO2024011754A1 publication Critical patent/WO2024011754A1/zh

Links

Images

Classifications

    • 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
    • H01M4/13—Electrodes for accumulators with non-aqueous electrolyte, e.g. for lithium-accumulators; Processes of manufacture thereof
    • H01M4/131—Electrodes based on mixed oxides or hydroxides, or on mixtures of oxides or hydroxides, e.g. LiCoOx
    • 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
    • H01M4/362—Composites
    • H01M4/366—Composites as layered products
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B02—CRUSHING, PULVERISING, OR DISINTEGRATING; PREPARATORY TREATMENT OF GRAIN FOR MILLING
    • B02C—CRUSHING, PULVERISING, OR DISINTEGRATING IN GENERAL; MILLING GRAIN
    • B02C21/00—Disintegrating plant with or without drying of the material
    • 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
    • H01M4/13—Electrodes for accumulators with non-aqueous electrolyte, e.g. for lithium-accumulators; Processes of manufacture thereof
    • H01M4/139—Processes of manufacture
    • H01M4/1391—Processes of manufacture of electrodes based on mixed oxides or hydroxides, or on mixtures of oxides or hydroxides, e.g. LiCoOx
    • 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
    • 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
    • H01M4/62—Selection of inactive substances as ingredients for active masses, e.g. binders, fillers
    • 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 present invention relates to the technical field of cathode material preparation, and in particular to a crushing method based on modified cathode material, modified cathode material and its preparation method.
  • Lithium-ion battery cathode materials are an important part of secondary lithium-ion batteries. They not only participate in electrochemical reactions as electrode materials, but also serve as a lithium ion source. Therefore, how to improve the performance of cathode materials has always been a research and development hotspot in the field of lithium-ion batteries.
  • Improving the performance of cathode materials mostly involves modifying the cathode material, and one of the common cathode material modification strategies is to coat the cathode material. Furthermore, for the coating modification of cathode materials, it is usually used in the liquid phase. Modification, but it can easily lead to the agglomeration of the cathode material in the liquid phase, affecting the electrochemical performance of the cathode material. Furthermore, in order to reduce the degradation of the performance of the cathode material modified in the liquid phase, solid phase coating modification has been developed.
  • Gas feeding the reaction powders includes gas feeding the cathode materials that need to be modified. Especially when it comes to solid-phase reactions, it is necessary to add cathode materials and various solid powders and other materials into the reactor.
  • the inner wall of the pipeline will be worn and the service life of the pipeline will be shortened.
  • the transportation pipeline is usually made of metal.
  • the inner wall wears the transportation will be damaged.
  • Metal impurities mixed in the material especially the presence of elemental iron, can cause battery short circuit or even battery failure.
  • the transportation pipeline is long and the inner wall is severely worn, a large amount of metal impurities will be mixed in the material.
  • the materials need to be pre-stirred so that the materials are mixed relatively evenly before the cathode material can be modified.
  • the purpose of the present invention is to at least overcome any shortcomings in the prior art and provide a crushing method based on modified cathode materials that can reduce the wear of the pipe wall by the material during transportation and reduce the content of metal impurities in the material.
  • Modified cathode material and preparation method thereof are provided.
  • a crushing method based on modified cathode material including the following steps:
  • the second crushed material is transported to a crusher for crushing operation.
  • the mass parts of the talc powder and the calcined product are respectively 8-15 parts and 85-92 parts, respectively.
  • the talc includes SiO 2 , MgO, Al 2 O 3 and impurities.
  • the talc powder includes the following components by mass:
  • the particle size D50 of the talc powder is 3 ⁇ m to 20 ⁇ m.
  • the particle size D90 of the talc powder is 6 ⁇ m to 15 ⁇ m.
  • the particle size of the calcined material is 30 mm to 100 mm.
  • the particle size of the first crushed material is 2 mm to 10 mm.
  • the particle size of the second pulverized material ranges from 1 ⁇ m to 50 ⁇ m.
  • the cathode material is cathode material NCM811.
  • the second pulverized material is transported to a pulverizer through a 3m-5m pipeline for pulverizing operation.
  • a method for preparing a modified cathode material including the crushing method based on the modified cathode material described in any of the above embodiments.
  • a modified cathode material is prepared by using the preparation method based on the modified cathode material described in any of the above embodiments.
  • the present invention at least has the following advantages:
  • the crushing method based on the modified cathode material of the present invention allows talcum powder to be added when crushing the calcined cathode material. Since the particles of the calcined cathode material in the jaw crusher and roller crusher The particle size is larger, and the talc powder can better adhere to the jaw crusher and the roller crusher, thereby making the talc powder better reduce the contact between the calcined material and the inner wall of the jaw crusher and the inner wall of the roller crusher respectively. Friction, that is, the wear of the positive electrode material on the inner wall of the jaw crusher and the inner wall of the roller crusher is reduced, thereby better ensuring the service life of the inner wall of the jaw crusher and the roller crusher, and better reducing the cost of modification.
  • the content of metal substances in the cathode material is stable; in addition, the particle size of the calcined material can be reduced after passing through the jaw crusher and roller crusher, thereby making the jaw crusher and roller crusher When used with a pulverizer, it is better to ensure that the required crushing particle size of the calcined material is quickly reached, and because the talc powder is mixed in, the calcined material has better fluidity, thereby reducing the friction and collision between the calcined material and the inner wall of the pulverizer.
  • the content of metal substances in the modified cathode material is further reduced;
  • talc powder can play a modified coating or doping role in the modification of the cathode material, that is, the talc powder is added to the calcined material of the cathode material to assist. After crushing and pulverizing, it will not become an impurity in the cathode material, and talcum powder, as a modified substance, is fully mixed with the cathode material during the crushing and pulverization of the cathode material, and is then added when the calcined product of the cathode material is crushed. Talcum powder can eliminate the pre-stirring and mixing process of modified substances and cathode materials in the preparation process of modified cathode materials, effectively speed up the preparation efficiency of modified cathode materials, and improve the performance of cathode materials.
  • Figure 1 is a flow chart of a crushing method based on modified cathode materials in one embodiment of the present invention.
  • This application also provides a crushing method based on modified cathode materials.
  • the crushing method based on the modified cathode material of the present application is further explained below:
  • the talc powder reduces the direct collision friction between the calcined material and the inner wall of the roller crusher during the crushing process, and reduces the wear of the positive material on the inner wall of the roller crusher respectively, thereby better ensuring the stability of the roller crusher. service life, and better reduces the content of metal substances in the modified cathode material.
  • the above-mentioned crushing method based on modified cathode material requires adding talcum powder when crushing the calcined cathode material. Since the particle size of the calcined cathode material in the jaw crusher and roller crusher is relatively small, Large, and the talc powder can better adhere to the jaw crusher and the roller crusher, so that the talc powder can better reduce the friction between the calcined material and the inner wall of the jaw crusher and the inner wall of the roller crusher respectively, that is, The wear of the cathode material on the inner wall of the jaw crusher and the inner wall of the roller crusher is reduced, thereby better ensuring the service life of the inner wall of the jaw crusher and the roller crusher, and better reducing the wear and tear of the modified cathode material.
  • the content of metal substances in the material in addition, the particle size of the calcined material can be reduced after passing through the jaw crusher and the roller crusher, so that the jaw crusher and the roller crusher can be combined with the crusher Use, that is, it is better to ensure that the required crushing particle size of the calcined product is quickly reached, and because the mixture of talc powder makes the calcined product have better fluidity, thereby reducing the friction and collision between the calcined product and the inner wall of the pulverizer, it is further better It greatly reduces the content of metal substances in the modified cathode material; and because talc powder can play a modified coating or doping role in the modification of the cathode material, that is, talc powder is added to the calcined material of the cathode material to assist After crushing and pulverizing, it will not become an impurity in the cathode material, and talcum powder, as a modified substance, is fully mixed with the cathode material during the crushing and pulverization of the
  • the talc powder is mixed with the calcined material, not only because the talc powder has better fluidity, it can better assist grinding or reduce the collision intensity of the calcined material on the jaw crusher and roller crusher during collision, and the talc
  • the hygroscopicity of the powder is poor, which avoids the increase of moisture in the cathode material. It is also because the talcum powder will quickly adhere to the inner wall of the jaw crusher or roller crusher after entering the jaw crusher or roller crusher.
  • talc powder 8 to 15 parts by mass of talc powder and 85 to 92 parts by mass of the calcined product are obtained. It can be understood that when the calcined product is doped with too much powder, the powder will break the calcined product. Therefore, it is better to ensure that the talc powder is 8 to 15 parts and the calcined product is 85 to 92 parts.
  • the particle size of the calcined material is rapidly reduced, and the indirect friction between the talc powder and the calcined material in the jaw crusher and the roller crusher is better ensured, thereby better ensuring the friction and collision between the calcined material and the inner wall of the crusher.
  • the reduction has better achieved the reduction of the content of metal substances in the modified cathode material.
  • 10 to 12 parts by mass of talc powder and 88 to 90 parts by mass of the calcined product are obtained. It can be understood that when the talcum powder is 10 to 12 parts and the calcined product is 88 to 90 parts, it is better to ensure that the particle size of the calcined product decreases rapidly, and it is better to ensure that the calcined product and the pulverizer are The reduction of friction and collision on the inner wall can better achieve the reduction of the content of metal substances in the modified cathode material.
  • the talc powder includes SiO 2 , MgO, Al 2 O 3 and impurities, which better realizes the modified coating or doping role that the talc powder can play in the modification of the cathode material.
  • the talc powder includes the following components by mass: 50 to 70 parts of SiO 2 ; 8 to 35 parts of MgO; 0 to 1 part of Al 2 O 3 ; 4 to 10 parts of impurities,
  • the modified coating or doping role that talc powder can play in the modification of cathode materials is better realized, and the adhesion of talc powder to the inner walls of the jaw crusher and roller crusher is better ensured.
  • the adhesion of talc powder to the inner walls of the jaw crusher and roller crusher is better ensured.
  • the content of metal substances in modified cathode materials is reduced.
  • the impurities include bound water, CaO, and Fe 2 O 3 , ensuring that the properties of the cathode material are less affected.
  • the ignition loss rate of impurities is 4.5% to 6%, ensuring that the properties of the cathode material have little impact.
  • the particle size D50 of the talc powder is 3 ⁇ m to 20 ⁇ m, which can better achieve the effective adhesion of the talc powder to the inner walls of the jaw crusher and the roller crusher, and ensure the full mixing of the talc powder and the calcined material. Doping modification or coating modification.
  • the particle size D90 of the talc powder is 6 ⁇ m to 15 ⁇ m, which further achieves the effective adhesion of the talc powder to the inner walls of the jaw crusher and the roller crusher, and ensures sufficient adhesion between the talc powder and the calcined material.
  • Mixed doping modification or coating modification is 6 ⁇ m to 15 ⁇ m, which further achieves the effective adhesion of the talc powder to the inner walls of the jaw crusher and the roller crusher, and ensures sufficient adhesion between the talc powder and the calcined material.
  • the particle size D50 of the talc powder is 7 ⁇ m to 12 ⁇ m, which further better achieves the effective adhesion of the talc powder to the inner walls of the jaw crusher and the roller crusher, and ensures sufficient adhesion between the talc powder and the calcined material.
  • Mixed doping modification or coating modification is 7 ⁇ m to 12 ⁇ m, which further better achieves the effective adhesion of the talc powder to the inner walls of the jaw crusher and the roller crusher, and ensures sufficient adhesion between the talc powder and the calcined material.
  • the particle size D90 of the talc powder is 8 ⁇ m to 10 ⁇ m, which further better achieves the effective adhesion of the talc powder to the inner walls of the jaw crusher and the roller crusher, and ensures sufficient adhesion between the talc powder and the calcined material.
  • Mixed doping modification or coating modification is 8 ⁇ m to 10 ⁇ m, which further better achieves the effective adhesion of the talc powder to the inner walls of the jaw crusher and the roller crusher, and ensures sufficient adhesion between the talc powder and the calcined material.
  • the particle size of the calcined material is 30 mm ⁇ 100 mm.
  • the particle size D50 of the talc powder is 3 ⁇ m ⁇ 20 ⁇ m
  • the particle size of the calcined material is 30 mm ⁇ 100 mm, which can better form a particle gradation. , which better improves the fluidity of the powder, reduces the friction on the inner walls of the jaw crusher and roller crusher, and further reduces the content of metal substances in the modified cathode material.
  • the particle size of the calcined material is 30 mm to 98.7 mm, which better matches the particle size D50 of the talc powder to 3 ⁇ m to 20 ⁇ m to form a particle gradation, which better improves the fluidity of the powder and reduces the impact on the
  • the friction between the inner walls of the jaw crusher and the roller crusher further reduces the content of metal substances in the modified cathode material.
  • the particle size of the calcined material is 72.1 mm to 85.6 mm, which better matches the particle size D50 of the talc powder to 3 ⁇ m to 20 ⁇ m to form a particle gradation, which better improves the fluidity of the powder and reduces the The friction against the inner walls of the jaw crusher and roller crusher further reduces the content of metal substances in the modified cathode material.
  • the particle size of the first pulverized material is 2 mm to 10 mm. Cooperating with the subsequent roller crusher ensures rapid crushing of the first pulverized material.
  • the particle size of the first pulverized material is 2 mm to 8 mm, which better cooperates with the subsequent roller crusher to ensure rapid crushing of the first pulverized material.
  • the particle size of the first pulverized material is 3 mm to 8 mm, which better cooperates with the subsequent roller crusher to ensure rapid crushing of the first pulverized material.
  • the particle size of the second pulverized material is 1 ⁇ m to 50 ⁇ m. Cooperating with a subsequent pulverizer ensures rapid pulverization of the second pulverized material.
  • the particle size of the second pulverized material is 9 ⁇ m to 47 ⁇ m, which better cooperates with the subsequent pulverizer to ensure rapid pulverization of the second pulverized material.
  • the particle size of the second pulverized material is 1 ⁇ m to 12 ⁇ m, which better cooperates with the subsequent pulverizer to ensure rapid pulverization of the second pulverized material.
  • the particle size of the second pulverized material is 7 ⁇ m to 33 ⁇ m, which better cooperates with the subsequent pulverizer to ensure rapid pulverization of the second pulverized material.
  • the particle size of the second pulverized material is 11 ⁇ m to 47 ⁇ m, which better cooperates with the subsequent pulverizer to ensure rapid pulverization of the second pulverized material.
  • the cathode material is cathode material NCM811. It can be understood that the cathode material NCM811 is a high-nickel ternary cathode material.
  • the crushing method also includes the following steps: vibrating the jaw crusher and the roller crusher so that the talcum powder attached to the jaw crusher and the roller crusher in layers is separated from the jaw crusher and the roller crusher. . It can be understood that the calcined materials are added directly in the jaw crusher and roller crusher, and the loss of talc powder is mostly due to the talc powder attached to the inner walls of the jaw crusher and roller crusher.
  • the talc powder in the machine and roller crusher is easier to collect through vibration, which better realizes the controllability of the talc powder content in the calcined product, which is beneficial to the doping modification and coating modification of the cathode material.
  • the second crushed material is transported to the crusher through a 3m-5m pipeline for crushing operation. It can be understood that the loss of talc powder in the jaw crusher and roller crusher is easier to control, and when the second crushed material is transported to the crusher, it is usually transported by belt or pipeline, so that the loss of talc powder is It is difficult to control by vibration and other means.
  • the second crushed material is transported to the crusher through a 3m to 5m pipeline for crushing operation, that is, By controlling the loss of talc powder through the distance of the transportation line, the content of talc powder in the cathode material can be effectively controlled, which is beneficial to the doping modification and coating modification of the cathode material.
  • the pulverizer is a jet pulverizer or a mechanical pulverizer, which facilitates further effective pulverization of the second pulverized material and ensures the pulverization effect of the calcined material.
  • the second pulverized material is pneumatically transported to an airflow pulverizer through a 3m-5m pipeline for pulverizing operation. It can be understood that pneumatic transportation can reduce the residue of talc powder and cathode materials in the pipeline, thereby reducing the waste of talc powder and cathode materials.
  • the second pulverized material is pneumatically transported to a mechanical pulverizer through a 3m-5m pipeline for pulverizing operation.
  • the second crushed material is transported to a mechanical crusher through a 3m to 5m belt pipe for crushing operation. It can be understood that although pneumatic transportation can better reduce the waste of talcum powder and cathode materials in pipelines, the transportation efficiency of the second crushed material through pneumatic transportation is low. In order to further improve the transportation efficiency of the second crushed material, belt transportation is used. The second crushing material is transported in this way.
  • the second pulverized material is transported to an airflow pulverizer through a 3 m to 5 m belt pipe for pulverizing operation.
  • the second pulverized material is transported to the pulverizer for crushing operation through a combination of pneumatic transportation and belt transportation, which reduces the waste of talcum powder and cathode materials and improves the transportation efficiency of the second pulverized material.
  • This application also provides a preparation method of modified cathode material.
  • One embodiment of the preparation method of the modified cathode material includes the crushing method based on the modified cathode material in any of the above embodiments.
  • the preparation method of modified cathode material includes some or all of the following steps:
  • the mixed raw materials are subjected to a sintering operation to obtain a calcined product of the positive electrode material;
  • the calcined product is crushed using the crushing method based on the modified cathode material of any of the above embodiments;
  • the calcined material after demagnetization treatment is subjected to solid phase coating treatment to obtain a modified cathode material.
  • talcum powder is added when the calcined product of the cathode material is crushed, which reduces the collision friction between the calcined product and the machine during crushing and causes more chlorine to be incorporated into the cathode material.
  • the problem of metal substances requires that the incorporation of metal substances be dealt with in the previous steps that may cause the incorporation of more metal substances, that is, the talcum powder can be better adhered to the jaw crusher and roller crusher.
  • the metal substances in the positive electrode material such as iron and copper, especially copper, need to be combined with more complex equipment in the subsequent demagnetization process, but even so, it is still difficult to achieve good demagnetization of the positive electrode material.
  • the increase of metal substances is not effectively controlled during the preparation process of the cathode material, it will be difficult to achieve the removal of metal substances in the cathode material even if a large number of processes are added later. The content of metal substances in the cathode material is effectively reduced.
  • the metal substances are controlled when the calcined product of the cathode material is crushed, that is, the talcum powder is mixed and crushed together with the calcined product, which effectively reduces The collision and friction of the jaw crusher, roller crusher and pulverizer during crushing are eliminated, thereby better reducing the content of metal substances in the modified cathode material.
  • the solid phase coating treatment on the calcined material after demagnetization treatment is specifically: adding the calcined material after demagnetization treatment into the ball milling tank of the ball mill, and then adding twice the material mass into the ball milling tank.
  • a method for preparing the modified cathode material it also includes the following steps: drying the calcined material after demagnetization treatment, which is beneficial to the solid phase coating modification of the positive electrode material.
  • the preparation method of the modified cathode material further includes the following steps: washing the calcined material after the solid-phase coating process Drying process.
  • the method for preparing the modified cathode material further includes the following steps: crushing, classifying, and batching the washed and dried calcined material. Mixed packaging.
  • the calcined material after crushing is transported to a magnetic separator through a 3m to 5m pipeline for demagnetization treatment, which better ensures the controllability of the talc powder content.
  • the operation of transporting the calcined material to the magnetic separator is the same as the operation of transporting the second pulverized material to the pulverizer.
  • This application also provides a modified cathode material, which is prepared by using the preparation method based on the modified cathode material in any of the above embodiments.
  • the present invention at least has the following advantages:
  • the crushing method based on the modified cathode material of the present invention allows talcum powder to be added when crushing the calcined cathode material. Since the particles of the calcined cathode material in the jaw crusher and roller crusher The particle size is larger, and the talc powder can better adhere to the jaw crusher and the roller crusher, thereby making the talc powder better reduce the contact between the calcined material and the inner wall of the jaw crusher and the inner wall of the roller crusher respectively. Friction, that is, the wear of the positive electrode material on the inner wall of the jaw crusher and the inner wall of the roller crusher is reduced, thereby better ensuring the service life of the inner wall of the jaw crusher and the roller crusher, and better reducing the cost of modification.
  • the content of metal substances in the cathode material is stable; in addition, the particle size of the calcined material can be reduced after passing through the jaw crusher and roller crusher, thereby making the jaw crusher and roller crusher When used with a pulverizer, it is better to ensure that the required crushing particle size of the calcined material is quickly reached, and because the talc powder is mixed in, the calcined material has better fluidity, thereby reducing the friction and collision between the calcined material and the inner wall of the pulverizer.
  • the content of metal substances in the modified cathode material is further reduced;
  • talc powder can play a modified coating or doping role in the modification of the cathode material, that is, the talc powder is added to the calcined material of the cathode material to assist. After crushing and pulverizing, it will not become an impurity in the cathode material, and talcum powder, as a modified substance, is fully mixed with the cathode material during the crushing and pulverization of the cathode material, and is then added when the calcined product of the cathode material is crushed. Talcum powder can eliminate the pre-stirring and mixing process of modified substances and cathode materials in the preparation process of modified cathode materials, effectively speed up the preparation efficiency of modified cathode materials, and improve the performance of cathode materials.
  • the devices used for crushing are jaw crushers, roller crushers and jet pulverizers.
  • the discharge port of the jaw crusher is set above the feed port of the roller crusher, and the output end of the roller crusher It is transported with the jet crusher through a pipeline with a belt length of 3.2m.
  • the calcined material and talcum powder are put into the jaw crusher for crushing to form the first crushed material, and then enter the roller crusher for crushing to form the second crushed material.
  • the pipeline is transported to the airflow pulverizer for crushing.
  • the output end of the airflow pulverizer is connected to a cyclone separator and a dust collector in sequence to collect the crushed materials, and then transported to the magnetic separator through the pipeline for magnetic separation, and then enters the solid phase coating process.
  • the solid phase coating process includes: adding the above materials into the ball mill tank of the ball mill, then adding grinding balls with twice the mass of the materials, ball milling at 200r/min for 2 hours and then taking them out; sintering the ball-milled materials at 800°C, and then Cool in the furnace; the cooled material is crushed with a crusher to obtain talc powder solid-phase coated NCM811 with a particle size D50 of 10 ⁇ m; after the coating is completed, the coated NCM811 is washed, dried and other processes to prepare the finished product.
  • the above-mentioned talc powder addition amount is 8%.
  • the talc powder components include 52g SiO 2 , 8g MgO and 5g unavoidable impurity components (including bound water, CaO and Fe 2 O 3 , the ignition loss rate is 5.1%).
  • the particle size of the calcined material is 72.1 mm; the particle size of the first pulverized material is 10 mm, and the particle size of the second pulverized material is 47 ⁇ m.
  • the devices used for crushing are jaw crushers, roller crushers and mechanical crushers.
  • the discharge port of the jaw crusher is set above the feed port of the roller crusher, and the output end of the roller crusher It is transported with the mechanical crusher through the pipeline by belt and pneumatic.
  • the pipeline length is 3.8m.
  • the calcined material and talcum powder are put into the jaw crusher for crushing to form the first crushed material, and then enter the roller crusher for crushing to form the second crushed material. , then the pipeline is transported to the mechanical pulverizer for crushing.
  • the output end of the mechanical pulverizer is connected to a cyclone separator and a dust collector in turn to collect the crushed materials, and then transport them to the magnetic separator through the pipeline for magnetic separation, and then enter the solid phase Coating process
  • the solid phase coating process includes: adding the above materials into the ball mill tank of the ball mill, then adding grinding balls with twice the mass of the materials, ball milling at a speed of 210r/min for 2 hours and then taking them out; the ball-milled materials are heated at 810°C Sintering, and then cooling in the furnace; the cooled material is crushed with a crusher to obtain talc powder solid-phase coated NCM811 with a particle size D50 of 10 ⁇ m; after the coating is completed, the coated NCM811 is washed, dried and other processes to prepare the finished product.
  • the above-mentioned talc powder addition amount is 10%.
  • the talc powder components include 70g SiO 2 , 34g MgO and 8g unavoidable impurity components (including bound water, CaO and Fe 2 O 3 , ignition loss rate is 4.5%).
  • the particle size of the calcined material is 75 mm; the particle size of the first pulverized material is 6 mm, and the particle size of the second pulverized material is 9 ⁇ m.
  • the devices used for crushing are jaw crushers, roller crushers and mechanical crushers.
  • the discharge port of the jaw crusher is set above the feed port of the roller crusher, and the output end of the roller crusher It is transported with the mechanical crusher through the pipeline by belt and pneumatic.
  • the pipeline length is 4.0m.
  • the calcined material and talcum powder are put into the jaw crusher for crushing to form the first crushed material, and then enter the roller crusher for crushing to form the second crushed material. , then the pipeline is transported to the mechanical pulverizer for crushing.
  • the output end of the mechanical pulverizer is connected to a cyclone separator and a dust collector in turn to collect the crushed materials, and then transport them to the magnetic separator through the pipeline for magnetic separation, and then enter the solid phase Coating process
  • the solid phase coating process includes: adding the above materials into the ball mill tank of the ball mill, then adding grinding balls with twice the mass of the materials, ball milling at a speed of 210r/min for 2 hours and then taking them out; the ball-milled materials are heated at 790°C Sintering, and then cooling in the furnace; the cooled material is crushed with a crusher to obtain talc powder solid-phase coated NCM811 with a particle size D50 of 8 ⁇ m; after the coating is completed, the coated NCM811 is washed, dried and other processes to prepare the finished product.
  • the above-mentioned talc powder addition amount is 12%.
  • the talc powder components include 67g SiO 2 , 29g MgO, 1g Al 2 O 3 and 8g inevitable impurity components (including bound water, CaO and Fe 2 O 3 .
  • the particle size of the calcined material is 72.1 mm; the particle size of the first pulverized material is 8 mm, and the particle size of the second pulverized material is 33 ⁇ m.
  • the devices used for crushing are jaw crushers, roller crushers and mechanical crushers.
  • the discharge port of the jaw crusher is set above the feed port of the roller crusher, and the output end of the roller crusher It is transported pneumatically through a pipeline with a mechanical crusher.
  • the length of the pipeline is 4.5m.
  • the calcined material and talcum powder are put into the jaw crusher for crushing to form the first crushed material, and then enter the roller crusher for crushing to form the second crushed material.
  • the pipeline is transported to the mechanical pulverizer for crushing.
  • the output end of the mechanical pulverizer is connected to a cyclone separator and a dust collector in sequence to collect the crushed materials, and then transported to the magnetic separator through the pipeline for magnetic separation, and then enters the solid phase coating
  • the solid phase coating process includes: adding the above materials into the ball mill tank of the ball mill, then adding grinding balls with twice the mass of the materials, ball milling at a speed of 205r/min for 2 hours and then taking them out; sintering the ball-milled materials at 815°C , and then cooled in the furnace; the cooled material was crushed with a crusher to obtain talc powder solid-phase coated NCM811 with a particle size D50 of 10 ⁇ m; after the coating was completed, the coated NCM811 was washed, dried and other processes to prepare the finished product.
  • the above-mentioned talc powder addition amount is 10%.
  • the talc powder components include 51g SiO 2 , 8g MgO, 1g Al 2 O 3 and 10g inevitable impurity components (including bound water, CaO and Fe 2 O 3 .
  • the particle size of the calcined material is 100 mm; the particle size of the first pulverized material is 8 mm, and the particle size of the second pulverized material is 25 ⁇ m.
  • the devices used for crushing are jaw crushers, roller crushers and mechanical crushers.
  • the discharge port of the jaw crusher is set above the feed port of the roller crusher, and the output end of the roller crusher It is transported with the mechanical crusher through the pipeline by belt and pneumatic.
  • the pipeline length is 3.8m.
  • the calcined material is put into the jaw crusher for crushing to form the first crushed material, and then enters the roller crusher for crushing to form the second crushed material.
  • the pipeline It is transported to the mechanical pulverizer for crushing.
  • the output end of the mechanical pulverizer is connected to a cyclone separator and a dust collector in sequence to collect the crushed materials, and then transport them to the magnetic separator through pipelines for magnetic separation, and then enter the solid phase coating process.
  • the solid phase coating process includes: premixing the above materials and talcum powder, then adding them to the ball mill tank of the ball mill, then adding grinding balls twice the mass of the materials, ball milling at a speed of 210r/min for 2 hours and then taking them out; The final material is sintered at 810°C and then cooled in the furnace; the cooled material is crushed with a crusher to obtain talc powder solid-phase coated NCM811 with a particle size D50 of 10 ⁇ m; after the coating is completed, the coated NCM811 is washed, dried, etc. The process is prepared to obtain the finished product.
  • talc powder commonly available on the market.
  • the added amount of talc powder is 10%.
  • the particle size of the calcined material is 75 mm; the particle size of the first pulverized material is 6 mm, and the particle size of the second pulverized material is 9 ⁇ m.
  • the devices used for crushing are jaw crushers, roller crushers and mechanical crushers.
  • the discharge port of the jaw crusher is set above the feed port of the roller crusher, and the output end of the roller crusher It is transported with the mechanical crusher through the pipeline by belt and pneumatic.
  • the pipeline length is 3.8m.
  • the calcined material is put into the jaw crusher for crushing to form the first crushed material, and then enters the roller crusher for crushing to form the second crushed material.
  • the pipeline It is transported to the mechanical pulverizer for crushing.
  • the output end of the mechanical pulverizer is connected to a cyclone separator and a dust collector in sequence to collect the crushed materials, and then transport them to the magnetic separator through pipelines for magnetic separation, and then enter the solid phase coating process.
  • the talc powder is solid-phase coated with NCM811; after the coating is completed, the coated NCM811 is washed, dried and other processes to prepare the finished product.
  • the particle size of the calcined material is 75 mm; the particle size of the first pulverized material is 6 mm, and the particle size of the second pulverized material is 9 ⁇ m.
  • the modified cathode materials of Examples 1 to 4 and the modified cathode materials of Comparative Examples 1 to 2 are tested below, and relevant test data are recorded in the process of preparing the modified cathode materials. Please see Table 1 below. In each test, After completion, the pipeline is cleaned by air blowing to prevent material residue from affecting the test data.
  • the talc content is detected by detecting the MgO content, and then converting it into the proportion of MgO in the originally added talc.
  • the MgO content in the discharged material is detected as a%
  • the MgO content in the added talc powder is b%
  • the converted talc powder content in the discharged material is a%/b%.
  • the talc powder is crushed During the process, demagnetization is performed before being put into the jaw crusher together with the calcined material.
  • the capacity retention rate is the capacity retention rate after 200 discharge cycles at 1C at room temperature of 25°C.
  • the qualitative detection method of copper is general copper color detection. During the detection process, the color change is used to determine whether copper is contained.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Electrochemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Inorganic Chemistry (AREA)
  • Materials Engineering (AREA)
  • Manufacturing & Machinery (AREA)
  • Composite Materials (AREA)
  • Food Science & Technology (AREA)
  • Battery Electrode And Active Subsutance (AREA)

Abstract

本申请提供一种基于改性正极材料的破碎方法、改性正极材料及其制备方法。上述的基于改性正极材料的破碎方法包括如下步骤：获取滑石粉和正极材料的煅烧物；将滑石粉和煅烧物投入颚式破碎机中进行第一破碎操作，得到第一粉碎料；将第一粉碎料投入辊式破碎机进行第二破碎操作，得到第二粉碎料；将第二粉碎料运输至粉碎机进行粉碎操作。上述的基于改性正极材料的破碎方法能减少输送中物料对管壁的磨损和能减少物料中金属杂质的含量。

Description

基于改性正极材料的破碎方法、改性正极材料及其制备方法 技术领域
本发明涉及正极材料制备的技术领域，特别是涉及一种基于改性正极材料的破碎方法、改性正极材料及其制备方法。
背景技术
随着能源危机以及环境问题的日益突出，锂离子电池以其自身的安全性高、无污染等众多性能优点备受关注。锂离子电池正极材料是二次锂离子电池的重要组成部分，不仅作为电极材料参与电化学反应，还需要作为锂离子源。因此，如何提升正极材料的性能，一直是锂离子电池领域的研发热点。
提升正极材料的性能大多为对正极材料进行改性，而通常的正极材料改性策略之一为对正极材料进行包覆，进一步地，对于正极材料的包覆改性，通常采用在液相中的改性，但易导致正极材料在液相中发生团聚现象，影响正极材料的电化学性能，进一步地，为了减少正极材料在液相中改性的性能的降低，发展出固相包覆改性，又或对正极材料进行掺杂改性，通常也包括固相中的掺杂和液相中的掺杂，而无论是包覆改性或者掺杂改性，在具体工艺中，均需要对反应粉料进行气送，其中包括对需要进行改性的正极材料进行气送，尤其涉及到固相反应时，需要向反应器中投加正极材料和多种固体粉料等物料。
然而，在物料输送过程中，由于物料颗粒对输送管道内部的碰撞，均会对管道内壁造成磨损，缩短管道使用寿命；同时，输送管道通常由金属制成，当内壁磨损时，会使运送的物料中混入金属杂质，特别是单质铁的存在，会导致电池短路甚至电池失效，尤其是当输送管道较长时，若内壁磨损严重，物料中会掺杂大量的金属杂质。此外，在物料投加进入反应器后，还需要对物料进行预搅拌，使得物料混合的相对均匀后进行正极材料的改性。
发明内容
本发明的目的是至少克服现有技术中的任一不足之处，提供一种能减少输送中物料对管壁的磨损和能减少物料中金属杂质的含量的基于改性正极材料的破碎方法、改性正极材料及其制备方法。
本发明的目的是通过以下技术方案来实现的：
一种基于改性正极材料的破碎方法，包括如下步骤：
获取滑石粉和正极材料的煅烧物；
将所述滑石粉和所述煅烧物投入颚式破碎机中进行第一破碎操作，得到第一粉碎料；
将所述第一粉碎料投入辊式破碎机进行第二破碎操作，得到第二粉碎料；
将所述第二粉碎料运输至粉碎机进行粉碎操作。
在其中一个实施例中，获取质量份分别为8份～15份的所述滑石粉以及85份～92份的所述煅烧物。
在其中一个实施例中，所述滑石粉包括SiO 2、MgO、Al 2O 3和杂质。
在其中一个实施例中，所述滑石粉包括如下质量份的各组分：
Figure PCTCN2022121028-appb-000001
在其中一个实施例中，所述滑石粉的粒度D50为3μm～20μm。
在其中一个实施例中，所述滑石粉的粒度D90为6μm～15μm。
在其中一个实施例中，所述煅烧物的粒径为30mm～100mm。
在其中一个实施例中，所述第一粉碎料粒度为2mm～10mm。
在其中一个实施例中，所述第二粉碎料粒度为1μm～50μm。
在其中一个实施例中，所述正极材料为正极材料NCM811。
在其中一个实施例中，将所述第二粉碎料通过3m～5m的管道运输至粉碎机进行粉碎操作。
一种改性正极材料的制备方法，包括上述任一实施例所述的基于改性正极材料的破碎方法。
一种改性正极材料，采用上述任一实施例所述的基于改性正极材料的制备方法制备得到。
与现有技术相比，本发明至少具有以下优点：
1、本发明的基于改性正极材料的破碎方法，使得在对正极材料的煅烧物进行破碎时即加入滑石粉，由于在颚式破碎机和辊式破碎机中的正极材料的煅烧物的颗粒粒径较大，而滑石粉能较好地附着在颚式破碎机和辊式破碎机中，进而使得滑石粉较好地减少了煅烧物分别与颚式破碎机内壁和辊式破碎机内壁的摩擦，即减少了正极材料分别对颚式破碎机内壁和辊式破碎机内壁的磨损，进而较好地确保了颚式破碎机内壁和辊式破碎机的使用寿命，且较好地降低了改性正极材料中金属物质的含量；此外，使得煅烧物经过颚式破碎机和辊式破碎机后即可较好地确保煅烧物的粒径的降低，进而使得颚式破碎机和辊式破碎机配合粉碎机使用，即较好地确保了快速达到煅烧物的需要粉碎粒径，且由于混有滑石粉使 得煅烧物具有较好的流动性，进而降低了煅烧物与粉碎机内壁的摩擦碰撞，进一步较好地降低了改性正极材料中金属物质的含量；
2、本发明的基于改性正极材料的破碎方法，由于滑石粉在正极材料改性中可起到改性包覆或掺杂的作用，即滑石粉在加入至正极材料的煅烧物中进行辅助破碎和粉碎后并不会成为正极材料的杂质，并且滑石粉作为改性物质在正极材料的破碎和粉碎中即实现了与正极材料的充分混合，进而在对正极材料的煅烧物进行破碎时加入滑石粉，实现了改性正极材料的制备过程中改性物质与正极材料的预搅拌混合工序的减除，有效地加快了改性正极材料的制备效率，并且实现了正极材料的性能的提升。
附图说明
为了更清楚地说明本发明实施例的技术方案，下面将对实施例中所需要使用的附图作简单地介绍，应当理解，以下附图仅示出了本发明的某些实施例，因此不应被看作是对范围的限定，对于本领域普通技术人员来讲，在不付出创造性劳动的前提下，还可以根据这些附图获得其他相关的附图。
图1为本发明一实施例中基于改性正极材料的破碎方法的流程图。
具体实施方式
为了便于理解本发明，下面将参照相关附图对本发明进行更全面的描述。附图中给出了本发明的较佳实施方式。但是，本发明可以以许多不同的形式来实现，并不限于本文所描述的实施方式。相反地，提供这些实施方式的目的是使对本发明的公开内容理解的更加透彻全面。
需要说明的是，当元件被称为“固定于”另一个元件，它可以直接在另一个元件上或者也可以存在居中的元件。当一个元件被认为是“连接”另一个元件，它可以是直接连接到另一个元件或者可能同时存在居中元件。本文所使用的术语“垂直的”、“水平的”、“左”、“右”以及类似的表述只是为了说明的目的，并不表示是唯一的实施方式。
除非另有定义，本文所使用的所有的技术和科学术语与属于本发明的技术领域的技术人员通常理解的含义相同。本文中在本发明的说明书中所使用的术语只是为了描述具体的实施方式的目的，不是旨在于限制本发明。本文所使用的术语“及/或”包括一个或多个相关的所列项目的任意的和所有的组合。
本申请还提供一种基于改性正极材料的破碎方法。为更好地理解本申请的基于改性正极材料的破碎方法，以下对本申请的基于改性正极材料的破碎方法做进一步地解释说明：
基于改性正极材料的破碎方法的一实施方式包括如下步骤的部分或全部：
S100、获取滑石粉和正极材料的煅烧物。可以理解，由于滑石粉在正极材料改性中可起到改性包覆或掺杂的作用，使得获取滑石粉和正极材料的煅烧物进行混合破碎和粉碎， 有效地实现了改性物质和正极材料的预搅拌混合，进而实现了改性正极材料的制备过程中改性物质与正极材料的预搅拌混合工序的减除，有效地加快了改性正极材料的制备效率，并且实现了正极材料的性能的提升。
S200、将滑石粉和煅烧物投入颚式破碎机中进行第一破碎操作，得到第一粉碎料。可以理解，由于滑石粉具有较好的流动性和较好的附着性，进而将滑石粉和煅烧物投入颚式破碎机中进行第一破碎操作，即使得滑石粉和煅烧物一并于颚式破碎机中破碎，进而使得滑石粉快速附着于颚式破碎机内壁上，即使得滑石粉减少了破碎过程中煅烧物和颚式破碎机内壁的直接碰撞摩擦，减少了正极材料分别对颚式破碎机内壁的磨损，进而较好地确保了颚式破碎机内壁的使用寿命，且较好地降低了改性正极材料中金属物质的含量。
S300、将第一粉碎料投入辊式破碎机进行第二破碎操作，得到第二粉碎料。可以理解，为了更好地确保煅烧物的有效破碎，并且为了减少煅烧物在破碎过程中的损耗，使得煅烧物在投入颚式破碎机中以将颗粒较大的煅烧物破碎后，接着投入辊式破碎机中进行较细致的破碎，有效且快速地实现了煅烧物的粒度D90的快速减小；此外，第一粉碎料进入辊式破碎机时，滑石粉会快速附着于辊式破碎机的内壁上，即使得滑石粉减少了破碎过程中煅烧物和辊式破碎机内壁的直接碰撞摩擦，减少了正极材料分别对辊式破碎机内壁的磨损，进而较好地确保了辊式破碎机的使用寿命，且较好地降低了改性正极材料中金属物质的含量。
S400、将第二粉碎料运输至粉碎机进行粉碎操作。可以理解，使得煅烧物经过颚式破碎机和辊式破碎机后即可较好地确保煅烧物的粒径的降低，进而使得颚式破碎机和辊式破碎机配合粉碎机使用，即较好地确保了快速达到煅烧物的需要粉碎粒径，且由于混有滑石粉使得煅烧物具有较好的流动性，进而降低了煅烧物与粉碎机内壁的摩擦碰撞，进一步较好地降低了改性正极材料中金属物质的含量；此外，由于滑石粉在正极材料改性中可起到改性包覆或掺杂的作用，即滑石粉在加入至正极材料的煅烧物中进行辅助破碎和粉碎后并不会成为正极材料的杂质，并且滑石粉作为改性物质在正极材料的破碎和粉碎中即实现了与正极材料的充分混合，进而在对正极材料的煅烧物进行破碎时加入滑石粉，实现了改性正极材料的制备过程中改性物质与正极材料的预搅拌混合工序的减除，有效地加快了改性正极材料的制备效率，并且实现了正极材料的性能的提升。
上述的基于改性正极材料的破碎方法，使得在对正极材料的煅烧物进行破碎时即加入滑石粉，由于在颚式破碎机和辊式破碎机中的正极材料的煅烧物的颗粒粒径较大，而滑石粉能较好地附着在颚式破碎机和辊式破碎机中，进而使得滑石粉较好地减少了煅烧物分别与颚式破碎机内壁和辊式破碎机内壁的摩擦，即减少了正极材料分别对颚式破碎机内壁和辊式破碎机内壁的磨损，进而较好地确保了颚式破碎机内壁和辊式破碎机的使用寿命，且较好地降低了改性正极材料中金属物质的含量；此外，使得煅烧物经过颚式破碎机和辊式 破碎机后即可较好地确保煅烧物的粒径的降低，进而使得颚式破碎机和辊式破碎机配合粉碎机使用，即较好地确保了快速达到煅烧物的需要粉碎粒径，且由于混有滑石粉使得煅烧物具有较好的流动性，进而降低了煅烧物与粉碎机内壁的摩擦碰撞，进一步较好地降低了改性正极材料中金属物质的含量；以及由于滑石粉在正极材料改性中可起到改性包覆或掺杂的作用，即滑石粉在加入至正极材料的煅烧物中进行辅助破碎和粉碎后并不会成为正极材料的杂质，并且滑石粉作为改性物质在正极材料的破碎和粉碎中即实现了与正极材料的充分混合，进而在对正极材料的煅烧物进行破碎时加入滑石粉，实现了改性正极材料的制备过程中改性物质与正极材料的预搅拌混合工序的减除，有效地加快了改性正极材料的制备效率，并且实现了正极材料的性能的提升。
需要说明的是，若前期仅仅增加粉剂或润滑剂混合于煅烧物中，则粉剂或润滑剂较多地掺杂于煅烧物中，更多在于助磨或减少煅烧物在碰撞时对颚式破碎机和辊式破碎机的碰撞强度，但煅烧物依旧会较多地分别与颚式破碎机和辊式破碎机摩擦碰撞，进而较难实现正极材料中金属物质的有效去除，因此，在本申请中，使得滑石粉与煅烧物混合，不仅由于滑石粉具有较好的流动性，能较好地助磨或减少煅烧物在碰撞时对颚式破碎机和辊式破碎机的碰撞强度，以及滑石粉的吸湿性较差，避免了正极材料中水份的增多，还由于滑石粉在进入颚式破碎机或辊式破碎机后会快速地附着于颚式破碎机或辊式破碎机的内壁上，进而使得煅烧物更多间接与颚式破碎机或辊式破碎机的内壁摩擦碰撞，进而较好地降低了煅烧物与粉碎机内壁的摩擦碰撞，进一步降低了改性正极材料中金属物质的含量。
在其中一个实施例中，获取质量份分别为8份～15份的滑石粉以及85份～92份的煅烧物。可以理解，煅烧物中掺杂过多的粉体时，粉体会煅烧物的破碎，因此，使得滑石粉为8份～15份，且使得煅烧物为85份～92份，较好地确保了煅烧物的粒度的快速下降，并且较好地确保了滑石粉对颚式破碎机和辊式破碎机分别与煅烧物的间接摩擦，进而较好地确保了煅烧物与粉碎机内壁的摩擦碰撞的降低，较好地实现了改性正极材料中金属物质的含量的降低。
在其中一个实施例中，获取质量份分别为10份～12份的滑石粉以及88份～90份的煅烧物。可以理解，当使得滑石粉为10份～12份，且使得煅烧物为88份～90份时，更好地确保了煅烧物的粒度的快速下降，并且较好地确保了煅烧物与粉碎机内壁的摩擦碰撞的降低，较好地实现了改性正极材料中金属物质的含量的降低。
在其中一个实施例中，滑石粉包括SiO 2、MgO、Al 2O 3和杂质，较好地实现了滑石粉在正极材料改性中可起到的改性包覆或掺杂的作用。
在其中一个实施例中，滑石粉包括如下质量份的各组分：SiO 2 50份～70份；MgO 8份～35份；Al 2O 3 0份～1份；杂质4份～10份，较好地实现了滑石粉在正极材料改性中可起到的改性包覆或掺杂的作用，并且较好地确保了滑石粉对颚式破碎机和辊式破碎机的内壁的 附着作用，进而较好地确保了滑石粉对颚式破碎机和辊式破碎机分别与煅烧物的间接摩擦，进而较好地确保了煅烧物与粉碎机内壁的摩擦碰撞的降低，较好地实现了改性正极材料中金属物质的含量的降低。
在其中一个实施例中，杂质包括结合水、CaO和Fe 2O 3，确保了对正极材料的性质影响较小。
在其中一个实施例中，杂质的烧失率为4.5％～6％，确保了正极材料的性质影响较小。
在其中一个实施例中，滑石粉的粒度D50为3μm～20μm，较好地实现滑石粉对颚式破碎机和辊式破碎机的内壁的有效附着，并且确保了滑石粉与煅烧物的充分混合掺杂改性或包覆改性。
在其中一个实施例中，滑石粉的粒度D90为6μm～15μm，进一步较好地实现滑石粉对颚式破碎机和辊式破碎机的内壁的有效附着，并且确保了滑石粉与煅烧物的充分混合掺杂改性或包覆改性。
在其中一个实施例中，滑石粉的粒度D50为7μm～12μm，进一步较好地实现滑石粉对颚式破碎机和辊式破碎机的内壁的有效附着，并且确保了滑石粉与煅烧物的充分混合掺杂改性或包覆改性。
在其中一个实施例中，滑石粉的粒度D90为8μm～10μm，进一步较好地实现滑石粉对颚式破碎机和辊式破碎机的内壁的有效附着，并且确保了滑石粉与煅烧物的充分混合掺杂改性或包覆改性。
在其中一个实施例中，煅烧物的粒径为30mm～100mm，在滑石粉的粒度D50为3μm～20μm的情况下，配合使得煅烧物的粒径为30mm～100mm，较好地形成颗粒级配，较好地提高了粉体流动性，降低了对颚式破碎机和辊式破碎机的内壁的摩擦，进一步降低了改性正极材料中金属物质的含量。
在其中一个实施例中，煅烧物的粒径为30mm～98.7mm，更好地配合滑石粉的粒度D50为3μm～20μm以形成颗粒级配，更好地提高了粉体流动性，降低了对颚式破碎机和辊式破碎机的内壁的摩擦，进一步降低了改性正极材料中金属物质的含量。
在其中一个实施例中，煅烧物的粒径为72.1mm～85.6mm，更好地配合滑石粉的粒度D50为3μm～20μm以形成颗粒级配，更好地提高了粉体流动性，降低了对颚式破碎机和辊式破碎机的内壁的摩擦，进一步降低了改性正极材料中金属物质的含量。
在其中一个实施例中，第一粉碎料粒度为2mm～10mm，配合后续辊式破碎机，确保了对第一粉碎料的快速破碎。
在其中一个实施例中，第一粉碎料粒度为2mm～8mm，更好地配合后续辊式破碎机，确保了对第一粉碎料的快速破碎。
在其中一个实施例中，第一粉碎料粒度为3mm～8mm，更好地配合后续辊式破碎机，确保了对第一粉碎料的快速破碎。
在其中一个实施例中，第二粉碎料粒度为1μm～50μm，配合后续粉碎机，确保了对第二粉碎料的快速粉碎。
在其中一个实施例中，第二粉碎料粒度为9μm～47μm，更好地配合后续粉碎机，确保了对第二粉碎料的快速粉碎。
在其中一个实施例中，第二粉碎料粒度为1μm～12μm，更好地配合后续粉碎机，确保了对第二粉碎料的快速粉碎。
在其中一个实施例中，第二粉碎料粒度为7μm～33μm，更好地配合后续粉碎机，确保了对第二粉碎料的快速粉碎。
在其中一个实施例中，第二粉碎料粒度为11μm～47μm，更好地配合后续粉碎机，确保了对第二粉碎料的快速粉碎。
在其中一个实施例中，正极材料为正极材料NCM811。可以理解，正极材料NCM811即为高镍三元正极材料。
在其中一个实施例中，在将第二粉碎料运输至粉碎机进行粉碎操作的步骤之前，且在将第一粉碎料投入辊式破碎机进行第二破碎操作的步骤之后，基于改性正极材料的破碎方法还包括如下步骤：对颚式破碎机和辊式破碎机进行震动处理，以使层叠设置在颚式破碎机和辊式破碎机上附着的滑石粉脱离颚式破碎机和辊式破碎机。可以理解，在颚式破碎机和辊式破碎机中煅烧物均为直接投加，滑石粉的损耗较多在于颚式破碎机和辊式破碎机内壁附着的滑石粉，因此，在颚式破碎机和辊式破碎机中的滑石粉较容易通过震动收集，较好地实现了煅烧物中滑石粉的含量的可控性，进而有利于正极材料的掺杂改性和包覆改性。
在其中一个实施例中，将第二粉碎料通过3m～5m的管道运输至粉碎机进行粉碎操作。可以理解，在颚式破碎机和辊式破碎机中的滑石粉的损耗量较容易控制，而在第二粉碎物运输至粉碎机中，一般通过皮带运输或管道运输，使得滑石粉的损耗量较难通过震动等手段进行控制，因此，本申请中，为了确保了正极材料中滑石粉的含量的可控性，使得第二粉碎料通过3m～5m的管道运输至粉碎机进行粉碎操作，即通过运输线的距离对滑石粉的损耗进行控制，较好地实现了正极材料中滑石粉的含量的有效控制，有利于正极材料的掺杂改性和包覆改性。
在其中一个实施例中，粉碎机为气流粉碎机或机械粉碎机，有利于第二粉碎料的进一步有效粉碎，确保了煅烧物的粉碎效果。
在其中一个实施例中，将第二粉碎料通过3m～5m的管道气力运输至气流粉碎机进行 粉碎操作。可以理解，气力运输可减少滑石粉和正极材料在管道的残留，进而减少了滑石粉和正极材料的浪费。
在其中一个实施例中，将第二粉碎料通过3m～5m的管道气力运输至机械粉碎机进行粉碎操作。
在其中一个实施例中，将第二粉碎料通过3m～5m的皮带管道运输至机械粉碎机进行粉碎操作。可以理解，气力运输虽然能较好地减少管道中滑石粉和正极材料的浪费，但通过气力运输第二破碎料的运输效率较低，为了进一步提高第二破碎料的运输效率，使用皮带运输的方式对第二破碎料进行运输。
在其中一个实施例中，将第二粉碎料通过3m～5m的皮带管道运输至气流粉碎机进行粉碎操作。
在其中一个实施例中，通过气力运输和皮带运输运送结合将第二粉碎料运送至粉碎机进行粉碎操作，即减少了滑石粉和正极材料的浪费，又提高了第二粉碎料运输效率。
本申请还提供一种改性正极材料的制备方法。改性正极材料的制备方法的一实施方式包括上述任一实施例的基于改性正极材料的破碎方法。
在其中一个实施例中，改性正极材料的制备方法包括如下步骤的部分或全部：
获取正极材料的原料；
对原料进行混合处理；
混合处理后的原料进行烧结操作，得到正极材料的煅烧物；
采用上述任一实施例的基于改性正极材料的破碎方法对煅烧物进行破碎处理；
对破碎处理后的煅烧物进行除磁处理；
对除磁处理后的煅烧物进行固相包覆处理，得到改性正极材料。
上述的改性正极材料的制备方法中，在对正极材料的煅烧物进行破碎时加入滑石粉，减轻了煅烧物在破碎时与机械产生较多的碰撞摩擦而使得正极材料中掺入较多的金属物质的问题，使得在前序可能造成较多的金属物质掺入的步骤中对金属物质的掺入做了处理，即使得滑石粉较好地附着在颚式破碎机和辊式破碎机中，减少了煅烧物分别与颚式破碎机内壁和辊式破碎机内壁的摩擦，进而较好地降低了改性正极材料中金属物质的含量，接着进一步对破碎处理后的煅烧物进行除磁处理，进一步减少了煅烧物中磁性物质的含量；此外，实现了改性正极材料的制备过程中改性物质与正极材料的预搅拌混合工序的减除，即在破碎的过程中即已完成滑石粉和正极材料的混合，有效地加快了改性正极材料的制备效率，且较好地确保了正极材料的性能。
需要说明的是，正极材料中的金属物质，如铁和铜等，尤其是铜，在后续的除磁处理中需要配合较复杂的器械实现，但即使如此，依旧较难较好地实现正极材料中金属物质的 除去效果，也就是说，若在正极材料的制备过程中未对金属物质的增加进行有效的控制，即使后期增加大量的工序对正极材料中的金属物质进行去除，也较难实现正极材料中金属物质的含量的有效降低，因此，在本申请中，在对正极材料的煅烧物进行破碎时即对金属物质进行控制，即将滑石粉一并与煅烧物进行混合破碎，有效地减少了破碎中对颚式破碎机、辊式破碎机和粉碎机的碰撞摩擦，进而较好地降低了改性正极材料中金属物质的含量。
在其中一个实施例中，对除磁处理后的煅烧物进行固相包覆处理具体为：将除磁处理后的煅烧物加入球磨机的球磨罐内，接着先球磨罐中加入两倍物料质量的磨球，以200r/min～210r/min的转速球磨1.5h±0.5h后取出磨球；将球磨后的煅烧物在800℃±15℃下烧结，之后随炉冷却；冷却后的煅烧物用破碎机破碎制得粒度D50为8μm～12μm的滑石粉固相包覆正极材料，有效地实现了正极材料的滑石粉包覆改性。
在其中一个实施例中，在对除磁处理后的煅烧物进行固相包覆处理的步骤之前，且在对破碎处理后的煅烧物进行除磁处理的步骤之后，改性正极材料的制备方法还包括如下步骤：对除磁处理后的煅烧物进行干燥处理，有利于正极材料的固相包覆改性。
在其中一个实施例中，在对除磁处理后的煅烧物进行固相包覆处理的步骤之后，改性正极材料的制备方法还包括如下步骤：对固相包覆处理后的煅烧物进行洗涤干燥处理。
在其中一个实施例中，在对固相包覆处理的煅烧物进行洗涤干燥处理的步骤之后，改性正极材料的制备方法还包括如下步骤：对洗涤干燥处理后的煅烧物进行粉碎分级、批混和包装。
在其中一个实施例中，对破碎处理后的煅烧物通过3m～5m的管道运输至磁选机进行除磁处理，较好地确保了滑石粉的含量可控性。
在其中一个实施例中，将煅烧物运输至磁选机的操作与将第二粉碎料运输至粉碎机的操作相同。
本申请还提供一种改性正极材料，采用上述任一实施例的基于改性正极材料的制备方法制备得到。
与现有技术相比，本发明至少具有以下优点：
1、本发明的基于改性正极材料的破碎方法，使得在对正极材料的煅烧物进行破碎时即加入滑石粉，由于在颚式破碎机和辊式破碎机中的正极材料的煅烧物的颗粒粒径较大，而滑石粉能较好地附着在颚式破碎机和辊式破碎机中，进而使得滑石粉较好地减少了煅烧物分别与颚式破碎机内壁和辊式破碎机内壁的摩擦，即减少了正极材料分别对颚式破碎机内壁和辊式破碎机内壁的磨损，进而较好地确保了颚式破碎机内壁和辊式破碎机的使用寿命，且较好地降低了改性正极材料中金属物质的含量；此外，使得煅烧物经过颚式破碎机和辊式破碎机后即可较好地确保煅烧物的粒径的降低，进而使得颚式破碎机和辊式破碎机 配合粉碎机使用，即较好地确保了快速达到煅烧物的需要粉碎粒径，且由于混有滑石粉使得煅烧物具有较好的流动性，进而降低了煅烧物与粉碎机内壁的摩擦碰撞，进一步较好地降低了改性正极材料中金属物质的含量；
2、本发明的基于改性正极材料的破碎方法，由于滑石粉在正极材料改性中可起到改性包覆或掺杂的作用，即滑石粉在加入至正极材料的煅烧物中进行辅助破碎和粉碎后并不会成为正极材料的杂质，并且滑石粉作为改性物质在正极材料的破碎和粉碎中即实现了与正极材料的充分混合，进而在对正极材料的煅烧物进行破碎时加入滑石粉，实现了改性正极材料的制备过程中改性物质与正极材料的预搅拌混合工序的减除，有效地加快了改性正极材料的制备效率，并且实现了正极材料的性能的提升。
以下列举一些实施例，但需注意的是，下列实施例并没有穷举所有可能的情况，并且下述实施例中所用的材料如无特殊说明，均可从商业途径得到。
实施例1
破碎所使用的装置为颚式破碎机、辊式破碎机和气流粉碎机，其中，颚式破碎机的出料口设置于辊式破碎机的进料口的上方，辊式破碎机的输出端与气流粉碎机通过管道以皮带运输，管道长度为3.2m，将煅烧物和滑石粉投入颚式破碎机进行破碎形成第一粉碎料，然后进入辊式破碎机进行破碎形成第二破碎料，接着管道运输至气流粉碎机进行粉碎，气流粉碎机的输出端依次连接有旋风分离器及收尘器，收集粉碎后的物料，再通过管道输送至磁选机进行磁选，再进入固相包覆工序。
固相包覆工序包括：将上述物料加入球磨机的球磨罐内，然后加入两倍物料质量的磨球，以200r/min的转速球磨2h后取出；将球磨后的物料在800℃下烧结，之后随炉冷却；冷却后的物料用破碎机破碎制得粒度D50为10μm的滑石粉固相包覆NCM811；包覆结束后对包覆NCM811进行洗涤、干燥等工序制备得到成品。
上述的滑石粉添加量为8％，滑石粉组分包括52g SiO 2、8g MgO以及5g不可避免的杂质组分(包括结合水、CaO和Fe 2O 3，烧失率为5.1％)，滑石粉的粒度D50＝4μm，D90＝8μm。
煅烧物的粒度为72.1mm；第一粉碎料粒度为10mm，第二粉碎料粒度为47μm。
实施例2
破碎所使用的装置为颚式破碎机、辊式破碎机和机械粉碎机，其中，颚式破碎机的出料口设置于辊式破碎机的进料口的上方，辊式破碎机的输出端与机械粉碎机通过管道以皮带和气力运输，管道长度为3.8m，将煅烧物和滑石粉投入颚式破碎机进行破碎形成第一粉碎料，然后进入辊式破碎机进行破碎形成第二破碎料，接着管道运输至机械粉碎机进行粉碎，机械粉碎机的输出端依次连接有旋风分离器及收尘器，收集粉碎后的物料，再通过管道输送至磁选机进行磁选，再进入固相包覆工序，固相包覆工序包括：将上述物料加入球 磨机的球磨罐内，然后加入两倍物料质量的磨球，以210r/min的转速球磨2h后取出；将球磨后的物料在810℃下烧结，之后随炉冷却；冷却后的物料用破碎机破碎制得粒度D50为10μm的滑石粉固相包覆NCM811；包覆结束后对包覆NCM811进行洗涤、干燥等工序制备得到成品。
上述的滑石粉添加量为10％，滑石粉组分包括70g SiO 2、34g MgO以及8g不可避免的杂质组分(包括结合水、CaO和Fe 2O 3，烧失率为4.5％)，滑石粉的粒度D50＝10μm，D90＝15μm。
煅烧物的粒度为75mm；第一粉碎料粒度为6mm，第二粉碎料粒度为9μm。
实施例3
破碎所使用的装置为颚式破碎机、辊式破碎机和机械粉碎机，其中，颚式破碎机的出料口设置于辊式破碎机的进料口的上方，辊式破碎机的输出端与机械粉碎机通过管道以皮带和气力运输，管道长度为4.0m，将煅烧物和滑石粉投入颚式破碎机进行破碎形成第一粉碎料，然后进入辊式破碎机进行破碎形成第二破碎料，接着管道运输至机械粉碎机进行粉碎，机械粉碎机的输出端依次连接有旋风分离器及收尘器，收集粉碎后的物料，再通过管道输送至磁选机进行磁选，再进入固相包覆工序，固相包覆工序包括：将上述物料加入球磨机的球磨罐内，然后加入两倍物料质量的磨球，以210r/min的转速球磨2h后取出；将球磨后的物料在790℃下烧结，之后随炉冷却；冷却后的物料用破碎机破碎制得粒度D50为8μm的滑石粉固相包覆NCM811；包覆结束后对包覆NCM811进行洗涤、干燥等工序制备得到成品。
上述的滑石粉添加量为12％，滑石粉组分包括67g SiO 2、29g MgO、1g Al 2O 3以及8g不可避免的杂质组分(包括结合水、CaO和Fe 2O 3，烧失率为6％)，滑石粉的粒度D50＝8μm，D90＝11μm。
煅烧物的粒度为72.1mm；第一粉碎料粒度为8mm，第二粉碎料粒度为33μm。
实施例4
破碎所使用的装置为颚式破碎机、辊式破碎机和机械粉碎机，其中，颚式破碎机的出料口设置于辊式破碎机的进料口的上方，辊式破碎机的输出端与机械粉碎机通过管道以气力运输，管道长度为4.5m，将煅烧物和滑石粉投入颚式破碎机进行破碎形成第一粉碎料，然后进入辊式破碎机进行破碎形成第二破碎料，接着管道运输至机械粉碎机进行粉碎，机械粉碎机的输出端依次连接有旋风分离器及收尘器，收集粉碎后的物料，再通过管道输送至磁选机进行磁选，再进入固相包覆工序，固相包覆工序包括：将上述物料加入球磨机的球磨罐内，然后加入两倍物料质量的磨球，以205r/min的转速球磨2h后取出；将球磨后的物料在815℃下烧结，之后随炉冷却；冷却后的物料用破碎机破碎制得粒度D50为10μm 的滑石粉固相包覆NCM811；包覆结束后对包覆NCM811进行洗涤、干燥等工序制备得到成品。
上述的滑石粉添加量为10％，滑石粉组分包括51g SiO 2、8g MgO、1g Al 2O 3以及10g不可避免的杂质组分(包括结合水、CaO和Fe 2O 3，烧失率为4.5％)，滑石粉的粒度D50＝5μm，D90＝9μm。
煅烧物的粒度为100mm；第一粉碎料粒度为8mm，第二粉碎料粒度为25μm。
对比例1
破碎所使用的装置为颚式破碎机、辊式破碎机和机械粉碎机，其中，颚式破碎机的出料口设置于辊式破碎机的进料口的上方，辊式破碎机的输出端与机械粉碎机通过管道以皮带和气力运输，管道长度为3.8m，将煅烧物投入颚式破碎机进行破碎形成第一粉碎料，然后进入辊式破碎机进行破碎形成第二破碎料，接着管道运输至机械粉碎机进行粉碎，机械粉碎机的输出端依次连接有旋风分离器及收尘器，收集粉碎后的物料，再通过管道输送至磁选机进行磁选，再进入固相包覆工序，固相包覆工序包括：将上述物料和滑石粉进行预混合，接着，加入球磨机的球磨罐内，然后加入两倍物料质量的磨球，以210r/min的转速球磨2h后取出；将球磨后的物料在810℃下烧结，之后随炉冷却；冷却后的物料用破碎机破碎制得粒度D50为10μm的滑石粉固相包覆NCM811；包覆结束后对包覆NCM811进行洗涤、干燥等工序制备得到成品。
上述的滑石粉为一般市面上的滑石粉，滑石粉的添加量为10％，滑石粉的粒度D50＝10μm，D90＝15μm。
煅烧物的粒度为75mm；第一粉碎料粒度为6mm，第二粉碎料粒度为9μm。
对比例2
破碎所使用的装置为颚式破碎机、辊式破碎机和机械粉碎机，其中，颚式破碎机的出料口设置于辊式破碎机的进料口的上方，辊式破碎机的输出端与机械粉碎机通过管道以皮带和气力运输，管道长度为3.8m，将煅烧物投入颚式破碎机进行破碎形成第一粉碎料，然后进入辊式破碎机进行破碎形成第二破碎料，接着管道运输至机械粉碎机进行粉碎，机械粉碎机的输出端依次连接有旋风分离器及收尘器，收集粉碎后的物料，再通过管道输送至磁选机进行磁选，再进入固相包覆工序，固相包覆工序包括：将上述物料和70g SiO 2、34g MgO进行预混合，其中，SiO 2、MgO的粒度为：D50＝10μm，D90＝15μm；接着，加入球磨机的球磨罐内，然后加入两倍物料质量的磨球，以210r/min的转速球磨2h后取出；将球磨后的物料在810℃下烧结，之后随炉冷却；冷却后的物料用破碎机破碎制得粒度D50为10μm的滑石粉固相包覆NCM811；包覆结束后对包覆NCM811进行洗涤、干燥等工序制备得到成品。
煅烧物的粒度为75mm；第一粉碎料粒度为6mm，第二粉碎料粒度为9μm。
以下对实施例1～4的改性正极材料和对比例1～2的改性正极材料进行检测，在制备改性正极材料过程中记录相关试验数据，请见下表1，其中，每次试验结束后，对管道进行气吹清理，避免材料残留影响试验数据。
表1：实施例及对比例中相应组分的含量
Figure PCTCN2022121028-appb-000002
[注]样品中随机抽取十份进行铜的定性检测。
需要说明的是，滑石粉含量检测通过检测MgO含量，再结合原始投加的滑石粉中MgO的含量占比换算得到。例如：检测得到出料中的MgO含量为a％；投加的滑石粉中MgO的含量为b％，则换算得到出料中的滑石粉含量为a％/b％，此外，滑石粉在破碎过程中，即在与所述煅烧物一并投入颚式破碎机前会进行除磁。容量保持率为在常温25℃下以1C放电循环200次后的容量保持率。铜的定性检测方法为一般的铜显色检测，检测过程中通过颜色变化判断是否含有铜。
从表1可知，使得滑石粉在正极材料破碎时同步加入，有效地减少改性正极材料中铁和铜的含量，尤其是实施例2至3，并且滑石粉可控性较高，在滑石粉和正极材料一并破碎后即进行固相包覆，得到的滑石粉固相包覆NCM811具有较好的比容量和容量保持率，尤其是实施例2至3，而对比例2的正极材料的比容量和容量保持率相较于实施例1-4的正极材料的较差，可能在于：1、滑石粉中的某些杂质具有积极效果；2、物料中的磁性物质去除不够彻底；3、铜的影响。
以上所述实施例仅表达了本发明的几种实施方式，其描述较为具体和详细，但并不能因此而理解为对发明专利范围的限制。应当指出的是，对于本领域的普通技术人员来说，在不脱离本发明构思的前提下，还可以做出若干变形和改进，这些都属于本发明的保护范 围。因此，本发明专利的保护范围应以所附权利要求为准。

Claims (10)

  1. 一种基于改性正极材料的破碎方法，其特征在于，包括如下步骤：
    获取滑石粉和正极材料的煅烧物；
    将所述滑石粉和所述煅烧物投入颚式破碎机中进行第一破碎操作，得到第一粉碎料；
    将所述第一粉碎料投入辊式破碎机进行第二破碎操作，得到第二粉碎料；
    将所述第二粉碎料运输至粉碎机进行粉碎操作。
  2. 根据权利要求1所述的基于改性正极材料的破碎方法，其特征在于，获取质量份分别为8份～15份的所述滑石粉以及85份～92份的所述煅烧物。
  3. 根据权利要求1所述的基于改性正极材料的破碎方法，其特征在于，所述滑石粉包括SiO 2、MgO、Al 2O 3和杂质。
  4. 根据权利要求1所述的基于改性正极材料的破碎方法，其特征在于，所述滑石粉包括如下质量份的各组分：
    Figure PCTCN2022121028-appb-100001
  5. 根据权利要求1所述的基于改性正极材料的破碎方法，其特征在于，所述滑石粉的粒度D50为3μm～20μm；及/或，
    所述滑石粉的粒度D90为6μm～15μm。
  6. 根据权利要求1所述的基于改性正极材料的破碎方法，其特征在于，所述煅烧物的粒径为30mm～100mm；及/或，
    所述第一粉碎料粒度为2mm～10mm；及/或，
    所述第二粉碎料粒度为1μm～50μm。
  7. 根据权利要求1所述的基于改性正极材料的破碎方法，其特征在于，所述正极材料为正极材料NCM811。
  8. 根据权利要求1至7中任一项所述的基于改性正极材料的破碎方法，其特征在于，将所述第二粉碎料通过3m～5m的管道运输至粉碎机进行粉碎操作。
  9. 一种改性正极材料的制备方法，其特征在于，包括权利要求1至8中任一项所述的基于改性正极材料的破碎方法。
  10. 一种改性正极材料，其特征在于，采用权利要求9所述的基于改性正极材料的制 备方法制备得到。
PCT/CN2022/121028 2022-07-15 2022-09-23 基于改性正极材料的破碎方法、改性正极材料及其制备方法 WO2024011754A1 (zh)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
CN202210832497.8 2022-07-15
CN202210832497.8A CN115347159A (zh) 2022-07-15 2022-07-15 基于改性正极材料的破碎方法、改性正极材料及其制备方法

Publications (1)

Publication Number Publication Date
WO2024011754A1 true WO2024011754A1 (zh) 2024-01-18

Family

ID=83948296

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/CN2022/121028 WO2024011754A1 (zh) 2022-07-15 2022-09-23 基于改性正极材料的破碎方法、改性正极材料及其制备方法

Country Status (3)

Country Link
CN (1) CN115347159A (zh)
FR (1) FR3138008A1 (zh)
WO (1) WO2024011754A1 (zh)

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101519198A (zh) * 2009-04-16 2009-09-02 丁建民 一种正极材料磷酸铁锂的制备方法
CN105540574A (zh) * 2016-01-28 2016-05-04 成都新柯力化工科技有限公司 一种利用对喷式气流粉碎机制备石墨烯微片的方法
CN109346706A (zh) * 2018-11-13 2019-02-15 安徽卓越新能源材料有限公司 一种高容量低成本三元正极材料的生产方法
CN109411727A (zh) * 2018-10-22 2019-03-01 成都新柯力化工科技有限公司 一种提高锂电池正极材料流动性的方法
CN111313024A (zh) * 2020-02-24 2020-06-19 江门市科恒实业股份有限公司 一种纳米硅酸镁锂包覆高镍正极材料及其制备方法与应用
CN112838205A (zh) * 2021-01-11 2021-05-25 厦门厦钨新能源材料股份有限公司 一种锂离子电池正极材料细粉的回收方法

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101519198A (zh) * 2009-04-16 2009-09-02 丁建民 一种正极材料磷酸铁锂的制备方法
CN105540574A (zh) * 2016-01-28 2016-05-04 成都新柯力化工科技有限公司 一种利用对喷式气流粉碎机制备石墨烯微片的方法
CN109411727A (zh) * 2018-10-22 2019-03-01 成都新柯力化工科技有限公司 一种提高锂电池正极材料流动性的方法
CN109346706A (zh) * 2018-11-13 2019-02-15 安徽卓越新能源材料有限公司 一种高容量低成本三元正极材料的生产方法
CN111313024A (zh) * 2020-02-24 2020-06-19 江门市科恒实业股份有限公司 一种纳米硅酸镁锂包覆高镍正极材料及其制备方法与应用
CN112838205A (zh) * 2021-01-11 2021-05-25 厦门厦钨新能源材料股份有限公司 一种锂离子电池正极材料细粉的回收方法

Also Published As

Publication number Publication date
CN115347159A (zh) 2022-11-15
FR3138008A1 (fr) 2024-01-19

Similar Documents

Publication Publication Date Title
JP5890410B2 (ja) リチウム金属酸素化合物中の磁性および／または酸化不純物を削減する方法
AU2020101491A4 (en) A Method for Removing Iron from Steel Slag in Real Time Circularly from Steel Slag
CN110788114B (zh) 一种钢渣实时循环除铁和粉磨方法
US11482737B2 (en) Method for recovering valuable material from lithium ion secondary battery
CN110752415A (zh) 一种退役磷酸铁锂电池正极材料分选利用的工艺及装置
CN106099238A (zh) 一种废旧二次电池铁的回收方法
CN107185655A (zh) 一种新型管磨机
WO2024011754A1 (zh) 基于改性正极材料的破碎方法、改性正极材料及其制备方法
CN110721977B (zh) 一种利用熔融还原炉产生的炉渣直接制取活性铁粉的方法
JP6676124B1 (ja) リチウムイオン二次電池からの有価物の回収方法
CN109985713A (zh) 一种用于筛选废旧电池中黑粉的装置及其工艺
CN110767897A (zh) 一种三元正极材料制备工艺
CN109985712A (zh) 一种用于筛选废旧电池中铜铝材料的装置及其工艺
JP2015124413A (ja) 銅製錬における電気・電子部品屑の処理方法
CN209997756U (zh) 一种用于筛选废旧电池中黑粉的装置
CN207839121U (zh) 一种新型管磨机
CN108232196B (zh) 一种改性锂离子电池正极材料及其制备方法
WO2023050130A1 (zh) 一种锂电池正极材料的加工方法及生产线
WO2022060207A1 (ko) 고상합성에 의한 양극 활물질 및 그 제조 방법
JPH0781941A (ja) フェライトの製造方法
CN215919458U (zh) 一种烧结焊剂制备系统
CN115893524B (zh) 二次电池正极材料及其制备方法和应用
JP7176707B1 (ja) 再生正極材前駆体、再生正極材およびそれらの製造方法、並びに再生リチウムイオン二次電池
CN210535781U (zh) 锂电池正极材料回收利用的装置
WO2023243385A1 (ja) 再生正極材およびその製造方法、ならびに再生正極材の使用方法、再生正極、およびリチウムイオン二次電池

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: 22950865

Country of ref document: EP

Kind code of ref document: A1