CN110395728A - Preparation method of porous carbon sphere negative electrode material for lithium battery - Google Patents
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- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 title claims abstract description 96
- 229910052799 carbon Inorganic materials 0.000 title claims abstract description 90
- 239000007773 negative electrode material Substances 0.000 title claims abstract description 38
- WHXSMMKQMYFTQS-UHFFFAOYSA-N Lithium Chemical compound [Li] WHXSMMKQMYFTQS-UHFFFAOYSA-N 0.000 title claims abstract description 20
- 229910052744 lithium Inorganic materials 0.000 title claims abstract description 20
- 238000002360 preparation method Methods 0.000 title claims abstract description 20
- HBBGRARXTFLTSG-UHFFFAOYSA-N Lithium ion Chemical compound [Li+] HBBGRARXTFLTSG-UHFFFAOYSA-N 0.000 claims abstract description 28
- 229910001416 lithium ion Inorganic materials 0.000 claims abstract description 28
- 229910021392 nanocarbon Inorganic materials 0.000 claims abstract description 17
- 239000002253 acid Substances 0.000 claims abstract description 8
- 238000000034 method Methods 0.000 claims abstract description 7
- 239000003054 catalyst Substances 0.000 claims abstract description 4
- 239000007789 gas Substances 0.000 claims description 22
- 238000006243 chemical reaction Methods 0.000 claims description 13
- XKRFYHLGVUSROY-UHFFFAOYSA-N Argon Chemical compound [Ar] XKRFYHLGVUSROY-UHFFFAOYSA-N 0.000 claims description 12
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 claims description 12
- KWYUFKZDYYNOTN-UHFFFAOYSA-M Potassium hydroxide Chemical group [OH-].[K+] KWYUFKZDYYNOTN-UHFFFAOYSA-M 0.000 claims description 9
- 238000010438 heat treatment Methods 0.000 claims description 8
- WMFOQBRAJBCJND-UHFFFAOYSA-M Lithium hydroxide Chemical compound [Li+].[OH-] WMFOQBRAJBCJND-UHFFFAOYSA-M 0.000 claims description 6
- CDBYLPFSWZWCQE-UHFFFAOYSA-L Sodium Carbonate Chemical compound [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 claims description 6
- 229910052786 argon Inorganic materials 0.000 claims description 6
- GRYLNZFGIOXLOG-UHFFFAOYSA-N Nitric acid Chemical compound O[N+]([O-])=O GRYLNZFGIOXLOG-UHFFFAOYSA-N 0.000 claims description 5
- HSFWRNGVRCDJHI-UHFFFAOYSA-N alpha-acetylene Natural products C#C HSFWRNGVRCDJHI-UHFFFAOYSA-N 0.000 claims description 5
- 125000002534 ethynyl group Chemical group [H]C#C* 0.000 claims description 5
- 239000004005 microsphere Substances 0.000 claims description 5
- 229910017604 nitric acid Inorganic materials 0.000 claims description 5
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 claims description 4
- 230000008021 deposition Effects 0.000 claims description 4
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 claims description 4
- BWHMMNNQKKPAPP-UHFFFAOYSA-L potassium carbonate Chemical compound [K+].[K+].[O-]C([O-])=O BWHMMNNQKKPAPP-UHFFFAOYSA-L 0.000 claims description 4
- 238000005245 sintering Methods 0.000 claims description 4
- ATRRKUHOCOJYRX-UHFFFAOYSA-N Ammonium bicarbonate Chemical compound [NH4+].OC([O-])=O ATRRKUHOCOJYRX-UHFFFAOYSA-N 0.000 claims description 3
- 230000009471 action Effects 0.000 claims description 3
- 239000001099 ammonium carbonate Substances 0.000 claims description 3
- 235000012501 ammonium carbonate Nutrition 0.000 claims description 3
- 229910000029 sodium carbonate Inorganic materials 0.000 claims description 3
- 239000003345 natural gas Substances 0.000 claims description 2
- IJGRMHOSHXDMSA-UHFFFAOYSA-N nitrogen Substances N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims description 2
- 229910052757 nitrogen Inorganic materials 0.000 claims description 2
- QJGQUHMNIGDVPM-UHFFFAOYSA-N nitrogen group Chemical group [N] QJGQUHMNIGDVPM-UHFFFAOYSA-N 0.000 claims description 2
- 229910000027 potassium carbonate Inorganic materials 0.000 claims description 2
- 230000035484 reaction time Effects 0.000 claims description 2
- 238000010792 warming Methods 0.000 claims 1
- 238000005406 washing Methods 0.000 claims 1
- 239000000463 material Substances 0.000 abstract description 17
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- 239000002245 particle Substances 0.000 abstract description 7
- 238000007599 discharging Methods 0.000 abstract description 5
- 125000000524 functional group Chemical group 0.000 abstract description 5
- 238000000151 deposition Methods 0.000 abstract description 4
- 230000007246 mechanism Effects 0.000 abstract description 4
- 238000013508 migration Methods 0.000 abstract description 3
- 230000005012 migration Effects 0.000 abstract description 3
- 239000003513 alkali Substances 0.000 abstract description 2
- 238000009792 diffusion process Methods 0.000 abstract description 2
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- 239000010405 anode material Substances 0.000 description 8
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- 239000002077 nanosphere Substances 0.000 description 6
- 229910002804 graphite Inorganic materials 0.000 description 5
- 239000010439 graphite Substances 0.000 description 5
- 238000003860 storage Methods 0.000 description 5
- 239000002131 composite material Substances 0.000 description 4
- 239000011148 porous material Substances 0.000 description 4
- 150000001875 compounds Chemical class 0.000 description 3
- 238000005336 cracking Methods 0.000 description 3
- 238000000227 grinding Methods 0.000 description 3
- 239000011261 inert gas Substances 0.000 description 3
- 150000002500 ions Chemical class 0.000 description 3
- 229920005610 lignin Polymers 0.000 description 3
- 239000002243 precursor Substances 0.000 description 3
- 238000003756 stirring Methods 0.000 description 3
- 238000000967 suction filtration Methods 0.000 description 3
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 2
- 238000002441 X-ray diffraction Methods 0.000 description 2
- 239000011149 active material Substances 0.000 description 2
- 239000002194 amorphous carbon material Substances 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 2
- 238000005229 chemical vapour deposition Methods 0.000 description 2
- 238000009831 deintercalation Methods 0.000 description 2
- 238000011161 development Methods 0.000 description 2
- 239000001257 hydrogen Substances 0.000 description 2
- 229910052739 hydrogen Inorganic materials 0.000 description 2
- 230000006872 improvement Effects 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 230000002829 reductive effect Effects 0.000 description 2
- 238000011160 research Methods 0.000 description 2
- 230000002441 reversible effect Effects 0.000 description 2
- 238000007873 sieving Methods 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 1
- 239000006230 acetylene black Substances 0.000 description 1
- HMYNUKPKYAKNHH-UHFFFAOYSA-N acetylene;hydrate Chemical compound O.C#C HMYNUKPKYAKNHH-UHFFFAOYSA-N 0.000 description 1
- 230000002378 acidificating effect Effects 0.000 description 1
- 238000005054 agglomeration Methods 0.000 description 1
- 230000002776 aggregation Effects 0.000 description 1
- 229910003481 amorphous carbon Inorganic materials 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 239000011230 binding agent Substances 0.000 description 1
- 230000005540 biological transmission Effects 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 238000003763 carbonization Methods 0.000 description 1
- 239000003153 chemical reaction reagent Substances 0.000 description 1
- 239000011889 copper foil Substances 0.000 description 1
- 239000013078 crystal Substances 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000003795 desorption Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000004090 dissolution Methods 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000007720 emulsion polymerization reaction Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 230000003628 erosive effect Effects 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 238000000605 extraction Methods 0.000 description 1
- 238000005087 graphitization Methods 0.000 description 1
- 125000004435 hydrogen atom Chemical group [H]* 0.000 description 1
- 238000003780 insertion Methods 0.000 description 1
- 230000037431 insertion Effects 0.000 description 1
- 238000009830 intercalation Methods 0.000 description 1
- 230000002687 intercalation Effects 0.000 description 1
- 230000002427 irreversible effect Effects 0.000 description 1
- 238000011031 large-scale manufacturing process Methods 0.000 description 1
- XGZVUEUWXADBQD-UHFFFAOYSA-L lithium carbonate Chemical compound [Li+].[Li+].[O-]C([O-])=O XGZVUEUWXADBQD-UHFFFAOYSA-L 0.000 description 1
- 229910052808 lithium carbonate Inorganic materials 0.000 description 1
- 230000003446 memory effect Effects 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 239000004570 mortar (masonry) Substances 0.000 description 1
- 239000005486 organic electrolyte Substances 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 230000036961 partial effect Effects 0.000 description 1
- 238000011056 performance test Methods 0.000 description 1
- 230000008569 process Effects 0.000 description 1
- 230000001681 protective effect Effects 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 238000006479 redox reaction Methods 0.000 description 1
- 238000012827 research and development Methods 0.000 description 1
- 229910052710 silicon Inorganic materials 0.000 description 1
- 239000010703 silicon Substances 0.000 description 1
- 239000002002 slurry Substances 0.000 description 1
- 238000001179 sorption measurement Methods 0.000 description 1
- 238000012360 testing method Methods 0.000 description 1
- 238000009834 vaporization Methods 0.000 description 1
- 230000008016 vaporization Effects 0.000 description 1
- 238000012795 verification Methods 0.000 description 1
Classifications
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B82—NANOTECHNOLOGY
- B82Y—SPECIFIC USES OR APPLICATIONS OF NANOSTRUCTURES; MEASUREMENT OR ANALYSIS OF NANOSTRUCTURES; MANUFACTURE OR TREATMENT OF NANOSTRUCTURES
- B82Y30/00—Nanotechnology for materials or surface science, e.g. nanocomposites
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B82—NANOTECHNOLOGY
- B82Y—SPECIFIC USES OR APPLICATIONS OF NANOSTRUCTURES; MEASUREMENT OR ANALYSIS OF NANOSTRUCTURES; MANUFACTURE OR TREATMENT OF NANOSTRUCTURES
- B82Y40/00—Manufacture or treatment of nanostructures
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- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B32/00—Carbon; Compounds thereof
- C01B32/30—Active carbon
- C01B32/312—Preparation
- C01B32/318—Preparation characterised by the starting materials
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- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B32/00—Carbon; Compounds thereof
- C01B32/30—Active carbon
- C01B32/312—Preparation
- C01B32/342—Preparation characterised by non-gaseous activating agents
- C01B32/348—Metallic compounds
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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
- H01M10/0525—Rocking-chair batteries, i.e. batteries with lithium insertion or intercalation in both electrodes; Lithium-ion batteries
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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
- H01M4/36—Selection of substances as active materials, active masses, active liquids
- H01M4/58—Selection of substances as active materials, active masses, active liquids of inorganic compounds other than oxides or hydroxides, e.g. sulfides, selenides, tellurides, halogenides or LiCoFy; of polyanionic structures, e.g. phosphates, silicates or borates
- H01M4/583—Carbonaceous material, e.g. graphite-intercalation compounds or CFx
- H01M4/587—Carbonaceous material, e.g. graphite-intercalation compounds or CFx for inserting or intercalating light metals
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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
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Abstract
本发明公开了一种锂电池用多孔碳球负极材料的制备方法,该方法通过在无催化剂和低温的条件下对碳源气体进行沉积反应得到纳米碳球,再经碱活化和强酸酸化处理,得到多孔碳球负极材料。本发明不仅增加碳球表面缺陷,有效缩短锂离子扩散迁移路径,还增加多孔碳球材料的表面官能团和比表面积,有效的缓解纳米多孔碳球在材料中成膜稳定性,有利于大电流充放电,保证负极材料适当的体积能量密度和库伦效率。本发明制备的锂离子电池用纳米多孔碳球负极材料粒径小且均匀,比表面积大,在大电流充放电机制下,首次放电比容量近1400 mAh/g,循环100次后比容量能稳定在400mAh/g以上,具有高比容量,良好的倍率性能和循环性能,具有良好的应用前景。The invention discloses a preparation method of a porous carbon sphere negative electrode material for a lithium battery. The method obtains nano-carbon spheres by depositing a carbon source gas under conditions of no catalyst and low temperature, and then undergoes alkali activation and strong acid acidification treatment. The porous carbon sphere negative electrode material is obtained. The invention not only increases the surface defects of carbon spheres, effectively shortens the diffusion and migration path of lithium ions, but also increases the surface functional groups and specific surface area of the porous carbon sphere material, effectively alleviates the film-forming stability of nanoporous carbon spheres in the material, and is conducive to high-current charging. Discharge, to ensure the appropriate volumetric energy density and Coulombic efficiency of the negative electrode material. The nanoporous carbon sphere negative electrode material for lithium ion batteries prepared by the present invention has a small and uniform particle size and a large specific surface area. Under the high-current charging and discharging mechanism, the specific capacity of the first discharge is nearly 1400 mAh/g, and the specific capacity can be stable after 100 cycles. Above 400mAh/g, it has high specific capacity, good rate performance and cycle performance, and has a good application prospect.
Description
技术领域technical field
本发明属于锂离子电池技术领域,具体涉及一种锂电池用多孔碳球负极材料的制备方法。The invention belongs to the technical field of lithium ion batteries, and in particular relates to a preparation method of a porous carbon ball negative electrode material for lithium batteries.
背景技术Background technique
锂离子电池由于具有能量密度高,开路电压高,循环性能好,无记忆效应,绿色环保、自放电小等优点,已广泛用于手机、游戏机、笔记本电脑、电动汽车以及航天航空、新能源电网等领域。锂离子电池也一直是全球学者们研究和开发的热点,负极材料是影响锂离子电池综合电化学性能的关键因素之一。Lithium-ion batteries have been widely used in mobile phones, game consoles, notebook computers, electric vehicles, aerospace and new energy due to their high energy density, high open circuit voltage, good cycle performance, no memory effect, green environmental protection, and small self-discharge. power grid and other fields. Lithium-ion batteries have always been a hot spot of research and development by scholars around the world. Anode materials are one of the key factors affecting the comprehensive electrochemical performance of lithium-ion batteries.
碳材料是最早实现商业化的锂电池负极材料。这是由于碳基材料具有良好的导电性与机械稳定性,电池充放电过程中材料具有良好的循环稳定性及倍率性能,其次其原材料的廉价性且随处可见,制备工艺简便且成熟,对于锂离子在碳材料中的脱嵌机理和反应机理已被研究者所熟知。碳基负极材料可分为两类:石墨和无定形碳。石墨的理论比容量为372mAh/g,而商业化石墨负极的实际容量已接近理论值,提高空间十分有限,已经较难满足高能量密度电池需求。石墨本身还存在一定问题,如对电解液的要求相对较高等问题。虽然无定形碳材料对电解液的要求没有石墨高,但首次充放电是电池的可逆容量较低,且无定形碳材料中含有较多的氢原子使得电池在循环中产生了明显的电压滞后现象。因此开发具有高容量的新型负极材料是目前锂离子电池领域研究的重要方向之一。Carbon materials are the earliest commercialized lithium battery anode materials. This is because the carbon-based material has good electrical conductivity and mechanical stability, and the material has good cycle stability and rate performance during battery charging and discharging. Secondly, its raw materials are cheap and can be seen everywhere, and the preparation process is simple and mature. For lithium The deintercalation mechanism and reaction mechanism of ions in carbon materials have been well known by researchers. Carbon-based anode materials can be divided into two categories: graphite and amorphous carbon. The theoretical specific capacity of graphite is 372mAh/g, while the actual capacity of commercial graphite anodes is close to the theoretical value, and the room for improvement is very limited, making it difficult to meet the needs of high energy density batteries. Graphite itself still has certain problems, such as relatively high requirements for electrolytes. Although amorphous carbon materials do not require as much electrolyte as graphite, the reversible capacity of the battery is low for the first charge and discharge, and the amorphous carbon materials contain more hydrogen atoms, which makes the battery have obvious voltage hysteresis during the cycle. . Therefore, the development of new anode materials with high capacity is one of the important research directions in the field of lithium-ion batteries.
针对上述问题研究者们进行了大量实验研究。主要是针对碳负极材料容量低,能量密度低,续航能力不足,对电解液要求高,电压滞后现象等现象导致材料无法发挥电化学性能等问题,主要从两个方面入手:一、对传统的碳负极材料改性;二、开发新型的碳基材料。如发明专利CN201410103033.9公开一种作为锂离子电池的负极材料的Si/C复合物,该方法包括提供含有硅的活性材料,提供木质素,将所述活性材料与含有木质素的C前体接触,在至少400℃的温度下在惰性气体气氛中将木质素转化成无机碳。但该方法得到的碳石墨化程度低,获得的Si/C复合物用在锂离子电池上时,循环性能及容量并不理想,容量仅为800mAh/g左右。发明专利CN201310522221.0公开了一种多孔炭微球、制备方法及锂离子电池负极材料,使用乳液聚合法制备的多孔炭微球同时具有微孔、中孔和大孔结构,该多孔炭微球用于锂离子电池负极材料时,大孔结构为电解液提供了快速迁移的通道,中孔结构与有机电解液中离子大小相当,利于离子的快速吸附和脱附,微孔结构有利于锂离子的插入,从而使得锂离子二次电池具有较高的比容量和较好的大倍率充放电性能,但其可供锂离子存储的活性位点较少,容量上升空间较小,因此它所存在问题为能量密度低,续航能力不足。Researchers have conducted a lot of experimental research on the above problems. It is mainly aimed at problems such as low capacity, low energy density, insufficient battery life, high requirements for electrolyte, and voltage hysteresis, which lead to the inability of the material to perform electrochemical performance of the carbon negative electrode material. It mainly starts from two aspects: 1. For the traditional Modification of carbon anode materials; 2. Development of new carbon-based materials. For example, the invention patent CN201410103033.9 discloses a Si/C composite as a negative electrode material for a lithium-ion battery. The method includes providing an active material containing silicon, providing lignin, and combining the active material with a C precursor containing lignin Contacting converts lignin into inorganic carbon at a temperature of at least 400°C in an inert gas atmosphere. However, the degree of carbon graphitization obtained by this method is low, and when the obtained Si/C composite is used in a lithium-ion battery, the cycle performance and capacity are not ideal, and the capacity is only about 800mAh/g. Invention patent CN201310522221.0 discloses a porous carbon microsphere, a preparation method and a lithium-ion battery negative electrode material. The porous carbon microsphere prepared by emulsion polymerization has micropore, mesopore and macropore structure at the same time. The porous carbon microsphere When used as a negative electrode material for lithium-ion batteries, the macroporous structure provides a channel for rapid migration of the electrolyte, the mesopore structure is equivalent to the size of ions in the organic electrolyte, and is conducive to the rapid adsorption and desorption of ions, and the microporous structure is conducive to lithium ions. Insertion, so that the lithium-ion secondary battery has a higher specific capacity and better high-rate charge-discharge performance, but it has fewer active sites for lithium-ion storage, and the space for capacity increase is small, so it exists The problem is low energy density and insufficient battery life.
发明内容Contents of the invention
针对现有技术存在的上述不足,本发明的目的在于提供一种锂电池用多孔碳球负极材料的制备方法,解决现有负极材料粒径大,不可逆容量大,可逆容量低,能量密度低,续航能力不足,且对电解液要求高,与电极浸润性差,导致电化学性能不佳等问题。In view of the above-mentioned deficiencies in the prior art, the purpose of the present invention is to provide a preparation method of porous carbon sphere negative electrode material for lithium batteries, which solves the problems of large particle size, large irreversible capacity, low reversible capacity and low energy density of existing negative electrode materials. Insufficient battery life, high requirements on the electrolyte, and poor wettability with the electrode, resulting in poor electrochemical performance and other problems.
为实现上述目的,本发明采用如下技术方案:一种锂电池用多孔碳球负极材料的制备方法,包括以下步骤:In order to achieve the above object, the present invention adopts the following technical scheme: a preparation method of porous carbon sphere negative electrode material for lithium batteries, comprising the following steps:
1)将管式炉在惰性气氛下,按照5~10℃/min升温速率升温至450~580℃,然后通入碳源气体,在无催化剂的作用下进行化学气相沉积反应,得到纳米碳球;1) Under an inert atmosphere, the tube furnace is heated up to 450-580°C at a heating rate of 5-10°C/min, and then the carbon source gas is introduced, and the chemical vapor deposition reaction is carried out under the action of no catalyst to obtain nano-carbon spheres ;
这样,碳源气体在较低的温度(450~580℃)下进行化学裂解,由于气体未达到完全碳化(裂解)的温度而沉积,并且导致其生成的碳球其内部以及表面存在较多的含氢化合物,此类化合物在酸性环境下较为容易被脱除而在碳材料中产生缺陷,并且在无催化剂作用与适当气流下,沉积速度慢,生产的碳材料为粒径较小与缺陷较多的碳球。In this way, the carbon source gas is chemically cracked at a lower temperature (450~580°C), and the gas is deposited because the gas does not reach the temperature of complete carbonization (cracking), and there are more carbon spheres inside and on the surface. Hydrogen-containing compounds, such compounds are easier to be removed in an acidic environment and cause defects in carbon materials, and without catalyst action and proper air flow, the deposition rate is slow, and the produced carbon materials have smaller particle sizes and fewer defects. Lots of carbon spheres.
2)将步骤1)得到的纳米碳球加入碱性物质中,充分混合,然后在惰性气氛保护下烧结,进行活化处理,冷却至室温,洗涤至中性、干燥,然后将其研磨后用多孔筛300~400目过筛后得到多孔碳球;2) Add the carbon nanospheres obtained in step 1) into the alkaline substance, mix them thoroughly, then sinter under the protection of an inert atmosphere, perform activation treatment, cool to room temperature, wash until neutral, dry, and then grind them with a porous Sieve 300~400 mesh to get porous carbon spheres;
在保护气环境下,当环境温度上升至碱的溶解温度时,纳米碳球上的碱性物质会分解为氧化物和水,在纳米碳球表面形成孔洞,对其进行第一次活化。当温度继续上升到上述氧化物的分解温度与汽化温度后,氧化物会与碳材料发生部分氧化还原反应,适当增大碳材料的比表面积,从而增加材料的缺陷,加快锂离子的嵌脱与增加存储情况。In the protective gas environment, when the ambient temperature rises to the dissolution temperature of the alkali, the alkaline substance on the carbon nanosphere will be decomposed into oxide and water, and holes will be formed on the surface of the carbon nanosphere, which will be activated for the first time. When the temperature continues to rise to the decomposition temperature and vaporization temperature of the above-mentioned oxides, the oxides will undergo a partial redox reaction with the carbon material, appropriately increasing the specific surface area of the carbon material, thereby increasing the defects of the material, and accelerating the intercalation and extraction of lithium ions. Increase the storage situation.
3)将步骤2)制备的多孔碳球置于强酸溶液中反应,反应结束后,进行抽滤、洗涤至中性、干燥,即得到锂离子电池用多孔碳球负极材料。3) Put the porous carbon spheres prepared in step 2) into a strong acid solution for reaction. After the reaction, perform suction filtration, wash until neutral, and dry to obtain the porous carbon sphere negative electrode material for lithium-ion batteries.
通过强酸酸化,一方面为了除去碳球内部以及表面存在的含氢化合物,在材料表面及内部形成孔洞缺陷,其有利于锂离子的快速脱嵌以及储存;另一方面增加碳材料表面的官能团,有效的缓解纳米多孔碳球在材料中成膜稳定性,有利于大电流充放电,保证负极材料适当的体积能量密度和库伦效率。Through strong acid acidification, on the one hand, in order to remove the hydrogen-containing compounds existing inside and on the surface of carbon spheres, hole defects are formed on the surface and inside of the material, which is conducive to the rapid deintercalation and storage of lithium ions; on the other hand, increasing the functional groups on the surface of carbon materials, It can effectively alleviate the stability of the film formation of nanoporous carbon spheres in the material, which is conducive to high-current charging and discharging, and ensures the appropriate volumetric energy density and Coulombic efficiency of the negative electrode material.
作为优选的,所述碳源为天然气或乙炔。Preferably, the carbon source is natural gas or acetylene.
作为优选的,所述碱性物质为氢氧化钾、氢氧化钠、氢氧化锂、碳酸钠、碳酸钾、碳酸锂或碳酸铵。Preferably, the alkaline substance is potassium hydroxide, sodium hydroxide, lithium hydroxide, sodium carbonate, potassium carbonate, lithium carbonate or ammonium carbonate.
作为优选的,所述碳源气体的流量为100~500mL/min。Preferably, the flow rate of the carbon source gas is 100-500 mL/min.
碳源气体在较低的温度下进行裂解,若碳源气体的流速过快,则使得气体处于未裂解状态或裂解初始状态则被排出,导致无沉积材料生成;若碳源气体的流速过慢,则使得沉积量过大,颗粒粒径偏大,其表面的缺陷就会相应减少不利于锂离子的快速传递以及存储量会减小。The carbon source gas is cracked at a lower temperature. If the flow rate of the carbon source gas is too fast, the gas will be discharged in an uncracked state or the initial state of cracking, resulting in no deposition material; if the flow rate of the carbon source gas is too slow , so that the deposition amount is too large, the particle size is too large, and the defects on the surface will be reduced accordingly, which is not conducive to the rapid transmission of lithium ions and the storage capacity will be reduced.
作为优选的,所述纳米碳球与碱性物质的质量比为1:1~8。Preferably, the mass ratio of the carbon nanospheres to the alkaline substance is 1:1-8.
作为优选的,所述烧结温度为600~900℃,烧结时间为1~4h。Preferably, the sintering temperature is 600-900° C., and the sintering time is 1-4 hours.
作为优选的,所述强酸溶液的浓度为1~6mol,所述强酸为硝酸和硫酸中的一种或多种按任意比例混合。Preferably, the concentration of the strong acid solution is 1-6 mol, and the strong acid is one or more of nitric acid and sulfuric acid mixed in any proportion.
作为优选的,步骤3)所述反应温度为60~90℃,反应时间为1~3h。Preferably, the reaction temperature in step 3) is 60-90° C., and the reaction time is 1-3 h.
作为优选的,所述惰性气氛为氮气或氩气,所述惰性气氛的流量为100~300mL/min。Preferably, the inert atmosphere is nitrogen or argon, and the flow rate of the inert atmosphere is 100-300 mL/min.
本发明还提供了采用上述方法制备的锂电池用多孔碳球负极材料。The invention also provides the porous carbon sphere negative electrode material for lithium batteries prepared by the method.
一种锂离子电池,包含上述多孔碳球负极材料。A lithium ion battery, comprising the above-mentioned porous carbon sphere negative electrode material.
相比现有技术,本发明具有如下有益效果:Compared with the prior art, the present invention has the following beneficial effects:
1、本发明在制备锂离子电池用纳米多孔碳球负极材料中,采用化学气相沉积法技术通过控制碳源气体流量与低温设置制备出均匀、稳定、分散性好的纳米碳球,纳米碳球的平均直径为80~100 nm之间;再通过碱性物质对纳米碳球的二次活化,增加了纳米碳球的缺陷和比表面积,使其孔径更均匀;最后采用强酸酸化处理,不仅进一步在多孔碳球表面及内部形成孔洞缺陷,还在纳米碳球表面形成更多含氧官能团。因此,本发明不仅增加碳球表面缺陷,有效缩短锂离子扩散迁移路径,还增加多孔碳球材料的表面官能团和比表面积,有效的缓解纳米多孔碳球在材料中成膜稳定性,有利于大电流充放电,保证负极材料适当的体积能量密度和库伦效率,有效解决现有碳材料存在容量低,能量密度低,续航能力不足,对电解液要求高,电压滞后现象等现象导致材料无法发挥电化学性能等问题。1. In the preparation of nanoporous carbon sphere negative electrode materials for lithium-ion batteries, the present invention adopts chemical vapor deposition technology to prepare uniform, stable, and well-dispersed nanocarbon spheres by controlling the carbon source gas flow rate and low temperature settings. Nanocarbon spheres The average diameter of the nano-carbon spheres is between 80 and 100 nm; the secondary activation of the nano-carbon spheres by alkaline substances increases the defects and specific surface area of the nano-carbon spheres, making the pore diameter more uniform; Pore defects are formed on the surface and inside of the porous carbon spheres, and more oxygen-containing functional groups are formed on the surface of the nano-carbon spheres. Therefore, the present invention not only increases the surface defects of carbon spheres, effectively shortens the diffusion and migration path of lithium ions, but also increases the surface functional groups and specific surface area of the porous carbon sphere material, effectively alleviating the film-forming stability of nanoporous carbon spheres in the material, which is beneficial to large Current charging and discharging ensures proper volumetric energy density and coulombic efficiency of negative electrode materials, and effectively solves the problems of low capacity, low energy density, insufficient battery life, high requirements for electrolyte, and voltage hysteresis in existing carbon materials. chemical properties etc.
2、本发明制备的锂离子电池用纳米多孔碳球负极材料粒径小且均匀,比表面积大,在大电流充放电机制下,首次放电比容量近1400 mAh/g,循环100次后比容量能稳定在400mAh/g 以上,具有高比容量,良好的倍率性能和循环性能。本发明的制备方法工艺流程简单,成本低,易于规模化生产,具有良好的应用前景。2. The nanoporous carbon sphere negative electrode material for lithium-ion batteries prepared by the present invention has a small and uniform particle size and a large specific surface area. Under the high-current charging and discharging mechanism, the specific capacity of the first discharge is nearly 1400 mAh/g, and the specific capacity after 100 cycles Can be stable above 400mAh/g, with high specific capacity, good rate performance and cycle performance. The preparation method of the invention has simple technological process, low cost, easy large-scale production and good application prospect.
附图说明Description of drawings
图1是实施例1制得的多孔碳球负极材料的XRD图;Fig. 1 is the XRD pattern of the porous carbon sphere negative electrode material that embodiment 1 makes;
图2是实施例1制得的多孔碳球负极材料的SEM图;Fig. 2 is the SEM figure of the porous carbon sphere negative electrode material that embodiment 1 makes;
图3是实施例1制得的多孔碳球负极材料的为负极的扣式电池在200mA/g下的比容量与循环次数循环图。Fig. 3 is the cycle diagram of specific capacity and cycle number under 200mA/g of the negative electrode material of porous carbon spheres prepared in Example 1 as a negative electrode button battery.
具体实施方式Detailed ways
下面结合具体实施例和附图对本发明作进一步详细说明。以下实施例中未对实验方法进行特别说明的,均为常规操作,所用试剂为普通市售。The present invention will be described in further detail below in conjunction with specific embodiments and accompanying drawings. In the following examples, the experimental methods that are not specifically described are all routine operations, and the reagents used are generally commercially available.
一、一种锂电池用多孔碳球负极材料的制备方法One, a kind of preparation method of porous carbon sphere negative electrode material for lithium battery
实施例1Example 1
1)将管式炉在200mL/min流量的氩气气氛保护下,按照5℃/min升温速率升温至450℃,保温30min后,然后通入200mL/min流量的乙炔气体裂解反应1h,得到纳米碳球;1) Under the protection of an argon gas atmosphere with a flow rate of 200mL/min, the tube furnace was heated to 450°C at a heating rate of 5°C/min, and kept for 30 minutes, and then acetylene gas was introduced at a flow rate of 200mL/min for 1 hour to obtain nano carbon spheres;
2)向步骤1)得到的纳米碳球中加入碱性物质(氢氧化钠和碳酸钠摩尔比为1:3),使纳米碳球与碱性物质的质量比为1:4,然后在200 mL/min氩气气体流量保护下,按照5℃/min升温速率升温至900 ℃下保温30 min后烧结4 h进行活化处理,冷却至室温,洗涤至中性,研磨后用多孔筛300目过筛后得到多孔碳球;2) Add alkaline substances (the molar ratio of sodium hydroxide and sodium carbonate is 1:3) to the nanocarbon spheres obtained in step 1) so that the mass ratio of nanocarbon spheres to alkaline substances is 1:4, and then at 200 Under the protection of mL/min argon gas flow rate, heat up to 900 °C at a heating rate of 5 °C/min for 30 min, then sinter for 4 h for activation treatment, cool to room temperature, wash until neutral, and pass through a 300-mesh porous sieve after grinding Porous carbon spheres are obtained after sieving;
3)将步骤2)制备的多孔碳球置于2 mol/L硝酸溶液中,于60℃下恒温搅拌3h,反应结束后,进行抽滤、洗涤至中性、干燥,即得到锂离子电池用多孔碳球负极材料。3) Put the porous carbon spheres prepared in step 2) in 2 mol/L nitric acid solution, and stir at 60°C for 3 hours at a constant temperature. After the reaction, perform suction filtration, wash until neutral, and dry to obtain lithium-ion battery. Porous carbon sphere anode material.
实施例2Example 2
1)将管式炉在100mL/min流量的氩气气体保护下,按照5℃/min升温速率升温至550℃,保温40min后,然后通入100mL/min流量的乙炔气体裂解反应2h,得到纳米碳球;1) Under the protection of argon gas at a flow rate of 100mL/min, the tube furnace was heated to 550°C at a heating rate of 5°C/min, kept for 40min, and then acetylene gas at a flow rate of 100mL/min was introduced for 2h for cracking reaction to obtain nano carbon spheres;
2)向步骤1)得到的纳米碳球中加入碱性物质(氢氧化钾和碳酸铵摩尔比为1:1),使纳米碳球与碱性物质的质量比为1:5,然后在在100 mL/min惰性气体流量保护下,按照5℃/min升温速率升温至800 ℃下保温40 min后烧结3 h进行活化处理,冷却至室温,洗涤至中性,研磨后用多孔筛400目过筛后得到多孔碳球;2) Add alkaline substances (the molar ratio of potassium hydroxide and ammonium carbonate is 1:1) to the carbon nanospheres obtained in step 1), so that the mass ratio of carbon nanospheres to alkaline substances is 1:5, and then Under the protection of 100 mL/min inert gas flow rate, the temperature was raised to 800 °C at a heating rate of 5 °C/min for 40 min, and then sintered for 3 h for activation treatment, cooled to room temperature, washed to neutral, and passed through a 400-mesh porous sieve after grinding Porous carbon spheres are obtained after sieving;
3)将步骤2)制备的多孔碳球置于6mol/L硝酸溶液中,于80℃下恒温搅拌2h,反应结束后,进行抽滤、洗涤至中性、干燥,即得到锂离子电池用多孔碳球负极材料。3) Put the porous carbon spheres prepared in step 2) in a 6mol/L nitric acid solution, and stir at a constant temperature of 80°C for 2 hours. After the reaction, perform suction filtration, wash until neutral, and dry to obtain the porous carbon spheres for lithium-ion batteries. Carbon sphere anode material.
实施例3Example 3
1)将管式炉在400mL/min流量的氩气气体保护下,按照10℃/min升温速率升温至580℃,保温30min后,然后通入400mL/min流量的乙炔气体裂解反应2h,得到纳米碳球;1) Under the protection of argon gas at a flow rate of 400mL/min, the tube furnace was heated to 580°C at a heating rate of 10°C/min, kept for 30 minutes, and then acetylene gas at a flow rate of 400mL/min was introduced for 2 hours to obtain nano carbon spheres;
2)向步骤1)得到的纳米碳球中加入氢氧化钠,使纳米碳球与碱性物质的质量比为1:8,然后在在400 mL/min惰性气体流量保护下,按照10℃/min升温速率升温至900 ℃下保温30min后烧结1h进行活化处理,冷却至室温,洗涤至中性,研磨后用多孔筛300目过筛后得到多孔碳球;2) Add sodium hydroxide to the nanocarbon spheres obtained in step 1), so that the mass ratio of nanocarbon spheres to alkaline substances is 1:8, and then under the protection of 400 mL/min inert gas flow rate, according to 10 ℃ / The heating rate is raised to 900°C for 30 minutes, then sintered for 1 hour for activation treatment, cooled to room temperature, washed to neutrality, and sieved with a 300-mesh porous sieve to obtain porous carbon spheres after grinding;
3)将步骤2)制备的多孔碳球置于5 mol/L硝酸溶液中,于90℃下恒温搅拌2h,反应结束后,进行抽滤、洗涤至中性、干燥,即得到锂离子电池用多孔碳球负极材料。3) Put the porous carbon spheres prepared in step 2) in a 5 mol/L nitric acid solution, and stir at 90°C for 2 hours at a constant temperature. After the reaction, filter with suction, wash until neutral, and dry to obtain lithium-ion batteries. Porous carbon sphere anode material.
二、性能验证2. Performance verification
1、采用X射线衍射分析仪分析实施例1所得纳米多孔碳球负极材料的结构,如图1所示。1. Use an X-ray diffraction analyzer to analyze the structure of the nanoporous carbon sphere negative electrode material obtained in Example 1, as shown in FIG. 1 .
由图1可以看出,本发明提供的实施例1所制备的纳米多孔碳球负极材料在2θ =26°处存在一个尖锐的衍射峰,对应碳的(002)晶面,在2θ=43°处存在次强峰,对应碳的(100),说明本发明提供的制备方法制备得到了纯相的纳米多孔碳球负极材料。It can be seen from Figure 1 that the nanoporous carbon sphere negative electrode material prepared in Example 1 provided by the present invention has a sharp diffraction peak at 2θ = 26°, corresponding to the (002) crystal plane of carbon, at 2θ = 43° There is a sub-strong peak at , which corresponds to (100) of carbon, indicating that the preparation method provided by the present invention has prepared a pure-phase nanoporous carbon sphere negative electrode material.
2、使用扫描电镜观察实施例1所得活化后前驱体多孔碳球材料的形貌,如图2所示。2. Use a scanning electron microscope to observe the morphology of the activated precursor porous carbon sphere material obtained in Example 1, as shown in FIG. 2 .
从图2可以看出前驱体纳米多孔碳球粒径均一,颗粒团聚现象较弱,平均直径分布约为80-100nm,其表面出现少许裂痕,表明活化程度的提升对材料表面刻蚀情况也越严重,则材料的孔道及缺陷越多,理论上这些缺陷及孔道提升材料的比表面积将有利于储存锂离子,增加材料的储锂能力。It can be seen from Figure 2 that the particle size of the precursor nanoporous carbon spheres is uniform, the particle agglomeration phenomenon is weak, the average diameter distribution is about 80-100nm, and there are a few cracks on the surface, which indicates that the improvement of the activation degree will also lead to the erosion of the surface of the material. Seriously, the more pores and defects the material has, theoretically these defects and pores will increase the specific surface area of the material, which will help store lithium ions and increase the lithium storage capacity of the material.
3、将实施例1制备的纳米多孔碳球负极复合材料、乙炔黑和水性粘结剂,按质量比8:1:1进行配料,并置于研钵中研磨制备粘度适中的浆料,均匀的涂敷于铜箔上制得电极片,再将电极片在手套箱中组装成CR2032扣式电池,测试其电化学性能。3. The nanoporous carbon sphere negative electrode composite material prepared in Example 1, acetylene black and water-based binder are batched according to a mass ratio of 8:1:1, and placed in a mortar to grind to prepare a moderately viscous slurry, uniform coated on copper foil to make electrode sheets, and then assembled into CR2032 button cells in a glove box to test its electrochemical performance.
将组装成的CR2032扣式电池,在200mA/g的电流密度下进行100次循环性能测试,结果如图3所示。The assembled CR2032 button battery was subjected to a 100-cycle performance test at a current density of 200mA/g, and the results are shown in Figure 3.
从图3可以看出,经100次循环后纳米多孔碳球负极复合材料,除第一次循环衰减比较严重外,其余循环比容量容量较稳定,初始容量保持在1357mAh/g左右,100次循环之后保持在480mAh/g左右;较好的循环性能归因于较高的比表面积以及充足的官能团缓解纳米多孔碳球在材料中成膜稳定性,也大大提高了材料的电化学活性。It can be seen from Figure 3 that after 100 cycles, the nanoporous carbon sphere negative electrode composite material, except for the serious attenuation of the first cycle, the other cycle specific capacity capacity is relatively stable, the initial capacity remains at about 1357mAh/g, and after 100 cycles After that, it remained at about 480mAh/g; the better cycle performance was attributed to the higher specific surface area and sufficient functional groups to ease the film-forming stability of nanoporous carbon spheres in the material, and also greatly improved the electrochemical activity of the material.
最后说明的是,以上实施例仅用以说明本发明的技术方案而非限制,尽管参照较佳实施例对本发明进行了详细说明,本领域的普通技术人员应当理解,可以对本发明的技术方案进行修改或者等同替换,而不脱离本发明技术方案的宗旨和范围,其均应涵盖在本发明的权利要求范围当中。Finally, it is noted that the above embodiments are only used to illustrate the technical solutions of the present invention without limitation. Although the present invention has been described in detail with reference to the preferred embodiments, those of ordinary skill in the art should understand that the technical solutions of the present invention can be carried out Modifications or equivalent replacements without departing from the spirit and scope of the technical solution of the present invention shall be covered by the claims of the present invention.
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