WO2021077586A1 - 一种用于电极材料的硅氧颗粒及其制备方法和应用 - Google Patents
一种用于电极材料的硅氧颗粒及其制备方法和应用 Download PDFInfo
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- WO2021077586A1 WO2021077586A1 PCT/CN2019/126660 CN2019126660W WO2021077586A1 WO 2021077586 A1 WO2021077586 A1 WO 2021077586A1 CN 2019126660 W CN2019126660 W CN 2019126660W WO 2021077586 A1 WO2021077586 A1 WO 2021077586A1
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- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01P—INDEXING SCHEME RELATING TO STRUCTURAL AND PHYSICAL ASPECTS OF SOLID INORGANIC COMPOUNDS
- C01P2006/00—Physical properties of inorganic compounds
- C01P2006/12—Surface area
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- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01P—INDEXING SCHEME RELATING TO STRUCTURAL AND PHYSICAL ASPECTS OF SOLID INORGANIC COMPOUNDS
- C01P2006/00—Physical properties of inorganic compounds
- C01P2006/60—Optical properties, e.g. expressed in CIELAB-values
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- 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
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M4/00—Electrodes
- H01M4/02—Electrodes composed of, or comprising, active material
- H01M2004/021—Physical characteristics, e.g. porosity, surface area
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M4/00—Electrodes
- H01M4/02—Electrodes composed of, or comprising, active material
- H01M2004/026—Electrodes composed of, or comprising, active material characterised by the polarity
- H01M2004/027—Negative electrodes
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/10—Energy storage using batteries
Definitions
- the invention relates to the field of batteries, in particular to a silicon oxide particle used for lithium ion electrode materials, and a preparation method and application thereof.
- the negative electrode material of commercial lithium-ion batteries is mainly graphite, but due to the low theoretical capacity, it limits the further improvement of the energy density of lithium-ion batteries. Due to the high capacity advantages of silicon anode materials that other anode materials cannot match, it has become a research and development hotspot in recent years, and has gradually moved from laboratory research and development to commercial applications.
- the elemental silicon anode material has a serious volume effect in the process of lithium insertion and removal, and the volume change rate is about 300%, which will cause powdering of the electrode material and separation of the electrode material from the current collector.
- the new SEI film will be formed when the fresh interface is exposed to the electrolyte, which will continue to consume the electrolyte and reduce the cycle performance of the electrode material. .
- One of the objectives of the present invention is to provide a silicon-oxygen composite material with high capacity, high coulombic efficiency, long cycle life, and low expansion rate for lithium ion batteries and a preparation method thereof in view of the deficiencies of the prior art.
- the present invention provides a silica particle for electrode material, which has a dense structure and no pores above sub-micrometer level; it is characterized in that the silica particle includes:
- the general formula of the silicon oxide particles is SiOx; the silicon oxide particles are derived from, for example, amorphous silicon oxide powder raw materials through disproportionation reaction to form silicon nano-crystal grains/amorphous nano-crystals existing in the SiOx matrix Cluster
- each silicon oxide particle is a secondary particle formed by a composite of a plurality of silicon oxide particles and a carbon film, and there is no single silicon oxide primary particle or a silicon oxide primary particle coated with a carbon film.
- the carbon layer material is composed of glucose, sucrose, chitosan, starch, citric acid, gelatin, alginic acid, carboxymethyl cellulose, coal pitch, petroleum pitch, phenolic resin, tar, naphthalene oil, anthracene oil, Combination of one or more precursor materials of polyacrylic acid, polyacrylate, polystyrene, polyvinylpyrrolidone, polyethylene oxide, polyvinyl alcohol, epoxy resin, polyacrylonitrile, polymethyl methacrylate Obtained by carbonization treatment.
- the silicon oxide particles 0.5 ⁇ x ⁇ 1.5, preferably 0.8 ⁇ x ⁇ 1.2. More preferably, 0.9 ⁇ x ⁇ 1.1.
- the mass ratio of the silica particles to the silica particles is 80-99.9% by weight, preferably 90-99.5% by weight. More preferably, the mass ratio of the silica particles to the silica particles is 94-98 wt%.
- the silica particles may further include conductive additives uniformly dispersed in the inner and/or outer surface carbon layer of the silica particles.
- the conductive additive may be selected from one or a combination of Super P, Ketjen black, vapor-grown carbon fiber, acetylene black, conductive graphite, carbon nanotube, and graphene.
- the conductive additive accounts for 0.01-10 wt% of the silica particles, preferably 0.03-5 wt%.
- the silica particles further include one or more additional carbon layers coated on the outer surface of the silica particles, preferably one layer.
- the additional carbon layer is obtained by carbonizing a combination of one or more precursor materials selected from coal pitch, petroleum pitch, polyvinyl alcohol, epoxy resin, polyacrylonitrile, and polymethyl methacrylate.
- the additional carbon layer is composed of any one of methane, ethane, ethylene, acetylene, propane, propylene, butane, butene, butadiene, benzene, toluene, xylene, styrene or phenol, or Various combinations are obtained by chemical vapor deposition.
- the mass ratio of the additional carbon layer to the silicon-oxygen particles is 0.1-10 wt%, preferably 0.3-6 wt%.
- the D50 of the silica particles is 1-40 ⁇ m, preferably 3-20 ⁇ m.
- the specific surface area of the silica particles is 0.1-10 m 2 /g, more preferably 0.3-6 m 2 /g.
- the tap density of the silica particles is ⁇ 0.6 g/cm 3 , preferably ⁇ 0.8 g/cm 3 .
- the present invention also proposes the application of the silicon-oxygen particles as described above in electrode materials.
- the present invention also provides a negative electrode material, which includes any of the aforementioned silicon oxide particles.
- the negative electrode material is prepared by mixing silicon oxide particles and carbon-based powder materials, and the carbon-based powder materials can be selected from natural graphite, artificial graphite, surface-modified natural graphite, hard carbon, soft carbon or mesocarbon micro Any combination of one or more of the balls.
- the present invention also proposes a pole piece or battery including any of the foregoing negative electrode materials. Specifically, it may be a lithium ion battery.
- the present invention also proposes a method for preparing silicon oxide particles as described above, which includes: mixing the silicon oxide particles with the carbon layer precursor material and then performing carbonization in a non-oxidizing atmosphere, and the carbonized product is dispersed , Sieving, demagnetization treatment.
- the method for preparing silicon oxide particles as described above may also include the addition of conductive additives.
- the silicon oxide particles, conductive additives, and carbon layer precursor materials are mixed and granulated in a non-oxidizing atmosphere. Carbonization is carried out in the process, and the carbonized product is broken up, sieved, and demagnetized.
- the aforementioned method further includes the step of coating one or more additional carbon layers, preferably one layer.
- the granulation equipment can optionally have both heating and stirring functions, including but not limited to a VC mixer, a mechanical fusion machine, a coating kettle or a reaction kettle.
- the linear velocity at the maximum diameter of the stirring component in the VC mixer, mechanical fusion machine, coating kettle or reaction kettle is 1-30m/s; the temperature can be selected from 100-1050°C, and the time is 0.5-10 hours, and protected by an inert atmosphere.
- the carbon precursor material is softened and uniformly coated on the surface of the silicon oxide particles during the continuous high-speed stirring process.
- the multiple silicon oxide primary particles coated with the carbon precursor are bonded and agglomerated with each other.
- silicon oxide/carbon precursor composite secondary particles Form a certain size of silicon oxide/carbon precursor composite secondary particles.
- the above-mentioned secondary particles will become denser under long-term and high-frequency shearing, extrusion, and collision in VC mixer, mechanical fusion machine, coating kettle or reaction kettle, and at the same time, the carbon precursor will be partially removed under heating conditions.
- the molecular volatiles are partially cross-linked and carbonized, so that the secondary particles are shaped.
- the granulation equipment may also be a spray drying equipment.
- the spray drying equipment processes the slurry containing silicon oxide particles and carbon precursors
- the nozzle of the equipment atomizes the slurry into small droplets, and the solvent in the droplets acts on the hot air at a certain temperature in the equipment
- the lower evaporates rapidly, and is collected by a cyclone to obtain dry silicon oxide/carbon precursor composite secondary particles.
- the carbonization equipment includes a tube furnace, an atmosphere box furnace, a pusher kiln, a roller kiln or a rotary kiln.
- the temperature of the carbonization reaction is 600-1200°C, and the time is 0.5-24 hours;
- the non-oxidizing atmosphere is provided by at least one of the following gases: nitrogen, argon, hydrogen, and helium.
- the dispersing equipment includes any one of a jet mill, a ball mill, a turbo mill, a Raymond mill, a coulter mill, and a toothed disk mill.
- the equipment for coating the additional carbon layer can optionally have both heating and stirring functions, including but not limited to any one of a mechanical fusion machine, a VC mixer, a high-speed disperser, a coating kettle or a reaction kettle.
- the coating additional carbon layer may be selected from a chemical vapor deposition method, which includes the step of: performing chemical vapor deposition in an organic gas and/or steam at a temperature of 700°C to 1050°C.
- the present invention has the following advantages:
- the silicon oxide particles are tightly connected through the carbon layer to form aggregated particles, which reduces the proportion of primary particles of small size while not increasing the secondary particles of large size too much, and obtains secondary particles with a narrower particle size distribution. Due to the preparation process of the secondary particles, the applicable range of the raw material of the silicon oxide particles is increased, and the technical solution of the present invention also greatly reduces the specific surface area of the material, thereby reducing the material in the battery, such as lithium ion secondary battery. The contact area between the electrolyte and the electrolyte reduces the loss of lithium ions caused by the continuous generation of SEI on the surface of the electrolyte during each charge and discharge process, which makes the battery coulombic efficiency higher and cycle performance better.
- the carbon layer connection and coating provide excellent electron and lithium ion transmission channels at the same time, ensuring that the silicon oxide inside the particles fully participates in the electrochemical reaction, reducing the polarization of the battery, and improving the rate performance; when the interior and surface of the secondary particles are dispersed When there are conductive additives, the conductivity of the material is further mentioned, and the rate performance of the battery is better.
- the capacity and expansion rate of the silicon-oxygen composite material are higher than that of the carbon-based negative electrode mixed with it, after the battery pole piece is made, the micro-area where the usual silicon-oxygen composite material is located has a higher meeting capacity and larger expansion.
- the particles prepared by the present invention have a narrower particle size distribution and a smaller proportion of large particles. Therefore, when the particles of the present invention are made into battery pole pieces, the surface capacity and expansion of the pole pieces The distribution is relatively more uniform, and the expansion rate of the pole piece will be smaller.
- the outer surface of the particles is further coated with a continuous carbon protective layer, which increases the conductivity of the material and further reduces the specific surface area of the composite material, reduces the formation of SEI, and is beneficial to improving the coulombic efficiency and battery cycle retention rate. Since the structure of the material of the present invention is more stable and the expansion is smaller, more silicon oxide particles can be added to the negative electrode material to achieve the purpose of increasing the energy density of the battery.
- Figure 1 is a high-power scanning electron micrograph of the secondary particles prepared in Example 1.
- FIG. 2 is a schematic diagram of the structure of the secondary particles prepared in Example 1.
- FIG. 2 is a schematic diagram of the structure of the secondary particles prepared in Example 1.
- FIG. 3 is a schematic diagram of the structure of the secondary particles prepared in Example 2.
- FIG. 3 is a schematic diagram of the structure of the secondary particles prepared in Example 2.
- FIG. 4 is a schematic diagram of the structure of the secondary particles prepared in Example 4.
- FIG. 4 is a schematic diagram of the structure of the secondary particles prepared in Example 4.
- FIG. 5 is a graph showing the particle size distribution of the silicon oxide raw materials used in Comparative Examples 2 and 6, and the secondary particles prepared in Comparative Examples 1, 2, and 6.
- Fig. 6 is a low-power scanning electron micrograph of the secondary particles prepared in Example 6.
- FIG. 7 is a high-power scanning electron micrograph of the secondary particles prepared in Example 6.
- Example 8 is an electron micrograph of a cross section of a negative electrode of a battery containing secondary particles prepared in Example 6 after formation.
- FIG. 9 is a high-power scanning electron micrograph of the secondary particles prepared in Example 14.
- FIG. 9 is a high-power scanning electron micrograph of the secondary particles prepared in Example 14.
- Figure 10 is a scanning electron microscope photograph of particles prepared in Comparative Example 1.
- Figure 11 is a scanning electron micrograph of particles prepared in Comparative Example 2.
- Figure 1 is a high-magnification scanning electron micrograph of the secondary particles prepared in Example 1
- Figure 2 is a schematic diagram of the structure.
- the particles prepared in Example 1 are dense secondary particles.
- the coated carbon layer B is composited.
- the silicon oxide material undergoes a heat treatment above 800°C, a disproportionation reaction will occur: 2SiO ⁇ Si+SiO 2 , forming silicon nanocrystalline grains/clusters uniformly dispersed in SiOx. According to the results of the X-ray diffraction pattern, substituting the Sherrer equation, it can be calculated that the Si(111) crystal plane in the material obtained in Example 1 corresponds to a crystal grain size of 2.9 nm.
- Hitachi SU8010 field emission scanning electron microscope to observe the surface morphology of the sample.
- Quantachrome Nova4200e specific surface area tester was used to test the specific surface area of the material.
- the elementar vario EL cube elemental analyzer is used to determine the carbon content in the material.
- the Rigaku MiniFlex600 X-ray diffractometer was used to test the crystal structure of the material.
- Half-cell evaluation the above-prepared silicon-oxygen-containing secondary particle negative electrode sheet, diaphragm, lithium sheet, and stainless steel gasket were sequentially stacked, and 200 ⁇ L of electrolyte was added dropwise, and then sealed to produce a 2016-type lithium-ion half-cell.
- Example 2 The process of Example 2 is similar to that of Example 1. The difference is that in the process of material synthesis, in addition to taking 100kg of silica powder and 12kg of coal pitch powder into the VC mixer, an additional 0.3kg of Ketjen Black and 0.2 kg of multi-walled carbon nanotube conductive additive powder. Therefore, the final product is silicon oxide/amorphous carbon composite secondary particles containing conductive additives.
- the structure is shown in Figure 3. This material is composed of silicon oxide primary particles A, conductive additives C and the two connected and coated in The carbon layer B is compounded together, and the conductive additive C is uniformly dispersed on the inner and outer surfaces of the secondary particles.
- the crystal grain size corresponding to the crystal plane is 2.9 nm.
- Example 2 Take 100kg of the secondary particles prepared in Example 1, and take 1kg of petroleum pitch powder, add them to the VC mixer, and mix them mechanically at a line speed of 3m/s for 10 minutes, and then reduce the speed to 2m/s in a nitrogen atmosphere. While stirring, the equipment was heated to 300°C and kept for 1 h, and then slowly cooled to room temperature. The above-mentioned pitch-coated material was kept at 400°C for 2h in an argon inert atmosphere, then heated to 900°C and carbonized for 4h, naturally cooled to room temperature, crushed, sieved and demagnetized to obtain a second layer of amorphous Carbon-coated silicon oxide/amorphous carbon composite particles.
- the crystal grain size corresponding to the crystal plane is 2.9 nm.
- FIG. 4 is a schematic diagram of the structure of the secondary particles prepared in this embodiment. As shown in Figure 4, the material is composed of primary silicon oxide particles A, conductive additives C, and a carbon layer B that connects and coats the two. , The conductive additive C is uniformly dispersed inside the secondary particles, and there is a second continuous carbon coating layer D on the outer surface of the secondary particles.
- the crystal grain size corresponding to the crystal plane is 2.9 nm.
- Example 3 The half-cell and full-cell evaluation methods are the same as in Example 1, and the results are summarized in Table 1. It can be seen that, as in Example 3, the performance of the product can be significantly improved after multiple coatings.
- sucrose solution Dissolve 0.2 kg of sucrose in 8 kg of deionized water to obtain a sucrose solution, then add 0.6 g of single-walled carbon nanotubes to the sucrose solution and stir and disperse the carbon nanotube slurry, and then add 2 kg of silicon oxide powder while stirring (same implementation Example 1), followed by ultrasonic dispersion for 1 hour while stirring, to obtain a composite slurry of sucrose/single-walled carbon nanotubes/silica particles.
- the composite slurry is spray-dried, the air inlet temperature is 150°C, and the spray nozzle atomization pressure is 0.2Mpa, to obtain dry powder of sucrose/single-walled carbon nanotube/silica composite secondary particles.
- the crystal grain size corresponding to the (111) crystal plane is 2.9 nm.
- FIG. 5 shows the particle size distribution diagram of the silica powder raw material and the silica composite material (ie, secondary particles) in this embodiment.
- FIG. 6 and FIG. 7 show scanning electron micrographs of the secondary particles prepared in this example
- FIG. 8 is a cross-sectional electron micrograph of the negative pole piece of a lithium ion battery containing the secondary particles prepared in this example.
- the particles obtained in this embodiment are secondary particles of uniform size, without monodisperse primary particles.
- Fig. 7 and Fig. 8 at the same time, it can be seen that the particles prepared in this embodiment are dense secondary particles.
- the carbon content is 3.0wt%, and the crystal grain size corresponding to the Si(111) crystal plane is 4.1nm.
- the half-cell and full-cell evaluation methods are the same as in Example 1.
- the results are summarized in Table 1.
- the weight energy density of the full battery reached 311Wh/kg, the cycle retention rate reached 90.7%, and the battery expansion rate was 7.6%.
- the obtained battery has excellent performance.
- Example 9 The process steps of Example 9 are similar to those of Example 8. The only difference is that in the granulation step, the holding temperature in the VC mixer is 400° C., and the holding time is 3 h.
- the crystal grain size corresponding to the crystal plane is 3.9 nm.
- Example 10 The process steps of Example 10 are similar to those of Example 8, with the only difference being that in the granulation step, the holding temperature in the VC mixer is 150° C., and the holding time is 6 hours.
- the crystal grain size corresponding to the crystal plane is 3.9 nm.
- Example 11 The process steps of Example 11 are similar to those of Example 9, with the only difference being that the amount of petroleum pitch added is 9 kg.
- the crystal grain size corresponding to the crystal plane is 3.9 nm.
- Example 12 The process steps of Example 12 are similar to those of Example 9, with the only difference being that the amount of petroleum pitch added is 3 kg.
- the crystal grain size corresponding to the crystal plane is 3.9 nm.
- FIG. 9 is a high-power scanning electron micrograph of the secondary particles prepared in Example 14.
- FIG. 9 is a high-power scanning electron micrograph of the secondary particles prepared in Example 14.
- silicon oxide block (average particle size about 2cm) in a box furnace, pass in an argon protective atmosphere, heat up at 3°C/min to 1000°C for high temperature heat treatment for 2 hours to obtain a disproportionated modified silicon oxide block body.
- Figure 10 is an electron microscope picture of the silicon oxide composite material in Comparative Example 1. It can be seen that there are many fine powder particles in the composite material, mostly monodisperse primary particles, and the particles have sharp edges and corners. It can be seen from the particle size distribution diagram of the silica composite material in Comparative Example 1 in FIG. 5 that the particle size distribution of the product of Comparative Example 1 is wider than that of Example 6, and the proportion of small particles is higher.
- the particle size distribution curve in Figure 5 is a weight/volume distribution curve. The height of the small particle segment curve is relatively high, indicating that the weight/volume ratio of small particles is relatively high. The ratio of the number of small particles and the ratio of specific surface area are orders of magnitude. increase. Therefore, it can be seen from the figure that compared with Example 6, the number of small particles in Comparative Example 1 is much higher, and the specific surface area also increases greatly.
- Example 1 Refer to the half-cell and full-cell evaluation methods of Example 1 to evaluate the performance of the battery prepared by the particles of this comparative example, and the results are summarized in Table 1.
- a precursor 1 put 100 kg of silica powder (same as Example 6) and 10 kg of petroleum pitch powder in a VC mixer, adjust the linear speed to 10 m/s, and mix for 0.5 h to obtain a precursor 1.
- Add the precursor 1 to the vacuum kneader control the temperature of the material to be above 250°C by heating and circulating the heat transfer oil, kneading for 6 hours until the material becomes viscous, and then quickly transfer to the flaking mill for flaking treatment before the material is cooled.
- the thickness of the rolled sheet is 2.0 ⁇ 5.0mm. After the rolled sheet is cooled, it is mechanically crushed.
- the median particle size is controlled to be 2.0 ⁇ 15.0 ⁇ m.
- the crushed material is subjected to isostatic pressure treatment with a controlled pressure of 20MPa and a temperature of 250°C. , The pressure treatment for 0.1h was carried out, and the precursor 2 was obtained.
- the precursor 2 is placed in a roller kiln, and a nitrogen protective gas is introduced to raise the temperature to 1000°C at 3°C/min, keep the temperature for 7 hours, and cool to room temperature naturally.
- the coulter is crushed for 1 hour, the maximum linear speed of the coulter is 3m/s, and then sieved, demagnetized, and dried to obtain silica particles.
- the crystal grain size corresponding to the crystal plane is 4.0 nm.
- Figure 11 is an electron microscope picture of the silica particles in Comparative Example 2. It can be seen that there are many fine powder particles in the composite material, and more monodisperse primary particles. There are some loose particles with larger and smaller primary particles that have a larger specific surface area. Secondary particles. It can be seen from the particle size distribution diagram of the silica particles in Comparative Example 2 in FIG. 5 that the particle size distribution of the product of Comparative Example 2 is wider than that of Example 1, and the proportions of small particles and large particles are both higher.
- Example 1 Refer to the half-cell and full-cell evaluation methods of Example 1 to evaluate the performance of the battery prepared by the particles of this comparative example, and the results are summarized in Table 1.
- Comparative Example 3 The process steps of Comparative Example 3 are similar to those of Examples 8-10. The only difference is that after mixing with a VC mixer at room temperature, the granulation process of heating and stirring is not carried out, and the material is discharged directly, and the material is subsequently carbonized and crushed. , Screening, demagnetization treatment.
- the crystal grain size corresponding to the crystal plane is 3.9 nm.
- the prior art As far as the prior art is concerned, its preparation process is complicated, such as kneading, sheet rolling, and compression molding processes that are difficult to achieve large-scale production.
- the carbon precursor is bound to adhere and agglomerate adjacent silicon oxide particles after being carbonized, and subsequent crushing, pulverization and other processes will damage the carbon coating layer.
- the material prepared in the prior art has a wide particle size distribution, and the proportions of large and small particles are relatively high.
- the coulombic efficiency, expansion rate, and cycle retention rate of the prepared battery are all unsatisfactory, and the area capacity and micro-area expansion distribution are uneven.
- the secondary particles used in the negative electrode material prepared by the present invention are compact, narrow in particle size distribution, and small in specific surface area.
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Abstract
Description
Claims (26)
- 一种用于电极材料的硅氧颗粒,其特征在于,所述硅氧颗粒包括:氧化亚硅颗粒,其通式为SiOx;碳层,多个所述氧化亚硅颗粒由所述碳层粘结,且碳层粘结的多个所述氧化亚硅颗粒由所述碳层包覆。
- 根据权利要求1所述的硅氧颗粒,其特征在于,所述碳层由葡萄糖、蔗糖、壳聚糖、淀粉、柠檬酸、明胶、海藻酸、羧甲基纤维素、煤沥青、石油沥青、酚醛树脂、焦油、萘油、蒽油、聚丙烯酸、聚丙烯酸酯、聚苯乙烯、聚乙烯吡咯烷酮、聚氧化乙烯、聚乙烯醇、环氧树脂、聚丙烯腈、聚甲基丙烯酸甲酯中的一种或多种前驱体材料的组合经碳化处理得到。
- 根据权利要求1所述的硅氧颗粒,其特征在于,所述氧化亚硅颗粒中,0.5≤x≤1.5。
- 根据权利要求1所述的硅氧颗粒,其特征在于,所述氧化亚硅颗粒的中值粒径D50为0.05-20μm,优选为0.3-10μm。
- 根据权利要求1所述的硅氧颗粒,其特征在于,氧化亚硅颗粒占所述硅氧颗粒质量比为80-99.9wt%,优选为90-99.5wt%。
- 根据权利要求1所述的硅氧颗粒,其特征在于,还包括均匀分散于所述硅氧颗粒内部和外表面的导电添加剂。
- 根据权利要求6所述的硅氧颗粒,其特征在于,所述导电添加剂选自Super P、科琴黑、气相生长碳纤维、乙炔黑、导电石墨、碳纳米管、石墨烯中的一种或多种的组合。
- 根据权利要求6所述的硅氧颗粒,其特征在于,所述的导电添加剂占所述硅氧颗粒质量比为0.01-10wt%,优选为0.03-5wt%。
- 根据权利要求1或6所述的硅氧颗粒,其特征在于,还包括在 所述硅氧颗粒外表面包覆的一层或多层附加碳层,优选为一层。
- 根据权利要求9所述的硅氧颗粒,其特征在于,所述附加碳层由煤沥青、石油沥青、聚乙烯醇、环氧树脂、聚丙烯腈、聚甲基丙烯酸甲酯中的一种或多种前驱体材料的组合经碳化处理得到,或由甲烷、乙烷、乙烯、乙炔、丙烷、丙烯、丁烷、丁烯、丁二烯、苯、甲苯、二甲苯、苯乙烯或苯酚中的任意一种或者多种的组合经化学气相沉积得到。
- 根据权利要求9所述的硅氧颗粒,其特征在于,所述附加碳层占所述硅氧颗粒质量比为0.1-10wt%,优选为0.3-6wt%。
- 根据权利要求1-11任一所述的硅氧颗粒,其特征在于,所述硅氧颗粒的D50为1-40μm,优选为3-20μm,更优选为3.5-10μm。
- 根据权利要求12所述的硅氧颗粒,其特征在于,所述硅氧颗粒的粒径满足:(D90-D10)/D50≤1.4,优选为≤1.35。
- 根据权利要求12所述的硅氧颗粒,其特征在于,所述硅氧颗粒的比表面积为0.1-10m 2/g,优选为0.3-6m 2/g,更优选为0.8-2.7m 2/g。
- 根据权利要求14所述的硅氧颗粒,其特征在于,所述硅氧颗粒的振实密度≥0.6g/cm 3,优选为≥0.8g/cm 3。
- 如权利要求1-15任一所述的硅氧颗粒在电极材料中的应用。
- 一种负极材料,其特征在于,包括权利要求1-15任一所述的硅氧颗粒。
- 包括权利要求17所述负极材料的极片或电池。
- 如权利要求1所述的硅氧颗粒的制备方法,其特征在于,包括:将氧化亚硅颗粒同碳层的前驱体材料混合造粒后在非氧化性气氛中进行碳化,碳化产物经打散、过筛、除磁处理。
- 如权利要求19所述的硅氧颗粒的制备方法,其特征在于,所述氧化亚硅颗粒同碳层的前驱体材料混合造粒步骤还包括加入导电添加剂的步骤。
- 如权利要求19或20所述的硅氧颗粒的制备方法,其特征在于,该方法进一步包括包覆一层或多层附加碳层的步骤,优选为一层。
- 如权利要求19-21任一所述的硅氧颗粒的制备方法,其特征在于,所述造粒的设备包括VC混合机、机械融合机、包覆釜或反应釜;所述造粒过程中,设备中搅拌部件最大直径处的线速度为1-30m/s;温度为100-1050℃,时间为0.5-10小时,并由惰性气氛保护。
- 如权利要求19-21任一所述的硅氧颗粒的制备方法,其特征在于,所述造粒的设备还可以选自喷雾干燥设备;所述碳化的设备包括管式炉、气氛箱式炉、推板窑、辊道窑、回转炉;所述碳化反应的温度为600-1200℃,时间为0.5-24小时;所述非氧化性气氛由下述至少一种气体提供:氮气、氩气、氢气、氦气。
- 如权利要求19-21任一所述的硅氧颗粒的制备方法,其特征在于,所述打散工艺采用的设备包括采用气流粉碎机、球磨机、涡轮式粉碎机、雷蒙磨、犁刀粉碎机、齿盘磨中的任意一种。
- 如权利要求21所述的硅氧颗粒的制备方法,其特征在于,包覆所述附加碳层的设备包括机械融合机、VC混合机、高速分散机、包覆釜或反应釜中的任意一种。
- 如权利要求21所述的硅氧颗粒的制备方法,其特征在于,包覆所述附加碳层选自化学气相沉积方法,该方法包括步骤:在700℃至1050℃的温度下于有机气体和/或蒸汽中实施化学气相沉积。
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CN112687853B (zh) * | 2020-12-10 | 2022-08-16 | 安普瑞斯(南京)有限公司 | 硅氧颗粒团聚体及其制备方法、负极材料、电池 |
CN113594430B (zh) * | 2021-06-24 | 2022-09-13 | 安普瑞斯(南京)有限公司 | 硅基负极材料及其制备方法和应用 |
CN115763797A (zh) * | 2021-09-03 | 2023-03-07 | 贝特瑞新材料集团股份有限公司 | 负极材料及其制备方法、锂离子电池 |
CN114784233A (zh) * | 2022-03-02 | 2022-07-22 | 安普瑞斯(南京)有限公司 | 一种负极活性材料及其制备方法和应用 |
CN114864890A (zh) * | 2022-04-19 | 2022-08-05 | 赣州市瑞富特科技有限公司 | 一种表面多孔微小中空球体硅碳负极材料及其制备方法 |
KR20230161157A (ko) * | 2022-05-18 | 2023-11-27 | 에스케이온 주식회사 | 이차 전지용 음극 활물질 및 이를 포함하는 리튬 이차 전지 |
CN115241459B (zh) * | 2022-08-17 | 2023-04-21 | 厦门凯纳石墨烯技术股份有限公司 | 一种用于离子电池的正极极片及离子电池 |
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