CN103390750A - Method for preparing lithium iron phosphate positive material - Google Patents
Method for preparing lithium iron phosphate positive material Download PDFInfo
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- CN103390750A CN103390750A CN2013103210045A CN201310321004A CN103390750A CN 103390750 A CN103390750 A CN 103390750A CN 2013103210045 A CN2013103210045 A CN 2013103210045A CN 201310321004 A CN201310321004 A CN 201310321004A CN 103390750 A CN103390750 A CN 103390750A
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- 239000000463 material Substances 0.000 claims abstract description 53
- GELKBWJHTRAYNV-UHFFFAOYSA-K lithium iron phosphate Chemical compound [Li+].[Fe+2].[O-]P([O-])([O-])=O GELKBWJHTRAYNV-UHFFFAOYSA-K 0.000 claims abstract description 47
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims abstract description 26
- 229910052799 carbon Inorganic materials 0.000 claims abstract description 26
- 238000000034 method Methods 0.000 claims abstract description 21
- 238000005245 sintering Methods 0.000 claims abstract description 20
- 238000002360 preparation method Methods 0.000 claims abstract description 14
- XUIMIQQOPSSXEZ-UHFFFAOYSA-N Silicon Chemical compound [Si] XUIMIQQOPSSXEZ-UHFFFAOYSA-N 0.000 claims abstract description 11
- 239000011247 coating layer Substances 0.000 claims abstract description 11
- 239000010703 silicon Substances 0.000 claims abstract description 11
- 229910052710 silicon Inorganic materials 0.000 claims abstract description 11
- 238000005019 vapor deposition process Methods 0.000 claims abstract description 7
- 239000007789 gas Substances 0.000 claims description 48
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims description 42
- XKRFYHLGVUSROY-UHFFFAOYSA-N Argon Chemical compound [Ar] XKRFYHLGVUSROY-UHFFFAOYSA-N 0.000 claims description 26
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 claims description 24
- 238000010438 heat treatment Methods 0.000 claims description 16
- 229910052757 nitrogen Inorganic materials 0.000 claims description 16
- 229910052786 argon Inorganic materials 0.000 claims description 13
- 239000011248 coating agent Substances 0.000 claims description 12
- 238000000576 coating method Methods 0.000 claims description 12
- BLRPTPMANUNPDV-UHFFFAOYSA-N Silane Chemical compound [SiH4] BLRPTPMANUNPDV-UHFFFAOYSA-N 0.000 claims description 11
- XGZVUEUWXADBQD-UHFFFAOYSA-L lithium carbonate Chemical compound [Li+].[Li+].[O-]C([O-])=O XGZVUEUWXADBQD-UHFFFAOYSA-L 0.000 claims description 11
- 229910052808 lithium carbonate Inorganic materials 0.000 claims description 11
- 239000011261 inert gas Substances 0.000 claims description 10
- UHOVQNZJYSORNB-UHFFFAOYSA-N Benzene Chemical compound C1=CC=CC=C1 UHOVQNZJYSORNB-UHFFFAOYSA-N 0.000 claims description 9
- WMFOQBRAJBCJND-UHFFFAOYSA-M Lithium hydroxide Chemical compound [Li+].[OH-] WMFOQBRAJBCJND-UHFFFAOYSA-M 0.000 claims description 9
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 claims description 9
- LFVGISIMTYGQHF-UHFFFAOYSA-N ammonium dihydrogen phosphate Chemical compound [NH4+].OP(O)([O-])=O LFVGISIMTYGQHF-UHFFFAOYSA-N 0.000 claims description 9
- 229910000387 ammonium dihydrogen phosphate Inorganic materials 0.000 claims description 9
- 238000000498 ball milling Methods 0.000 claims description 9
- 239000002270 dispersing agent Substances 0.000 claims description 9
- 229940062993 ferrous oxalate Drugs 0.000 claims description 9
- XEEYBQQBJWHFJM-UHFFFAOYSA-N iron Substances [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 claims description 9
- OWZIYWAUNZMLRT-UHFFFAOYSA-L iron(2+);oxalate Chemical compound [Fe+2].[O-]C(=O)C([O-])=O OWZIYWAUNZMLRT-UHFFFAOYSA-L 0.000 claims description 9
- 235000019837 monoammonium phosphate Nutrition 0.000 claims description 9
- CSCPPACGZOOCGX-UHFFFAOYSA-N Acetone Chemical compound CC(C)=O CSCPPACGZOOCGX-UHFFFAOYSA-N 0.000 claims description 8
- WHXSMMKQMYFTQS-UHFFFAOYSA-N Lithium Chemical compound [Li] WHXSMMKQMYFTQS-UHFFFAOYSA-N 0.000 claims description 8
- 229910052744 lithium Inorganic materials 0.000 claims description 8
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims description 7
- 238000001291 vacuum drying Methods 0.000 claims description 7
- OTMSDBZUPAUEDD-UHFFFAOYSA-N Ethane Chemical compound CC OTMSDBZUPAUEDD-UHFFFAOYSA-N 0.000 claims description 6
- PZPGRFITIJYNEJ-UHFFFAOYSA-N disilane Chemical compound [SiH3][SiH3] PZPGRFITIJYNEJ-UHFFFAOYSA-N 0.000 claims description 6
- 239000006185 dispersion Substances 0.000 claims description 6
- PQXKHYXIUOZZFA-UHFFFAOYSA-M lithium fluoride Chemical compound [Li+].[F-] PQXKHYXIUOZZFA-UHFFFAOYSA-M 0.000 claims description 6
- CZMRCDWAGMRECN-UGDNZRGBSA-N Sucrose Chemical compound O[C@H]1[C@H](O)[C@@H](CO)O[C@@]1(CO)O[C@@H]1[C@H](O)[C@@H](O)[C@H](O)[C@@H](CO)O1 CZMRCDWAGMRECN-UGDNZRGBSA-N 0.000 claims description 5
- 229930006000 Sucrose Natural products 0.000 claims description 5
- HSFWRNGVRCDJHI-UHFFFAOYSA-N alpha-acetylene Natural products C#C HSFWRNGVRCDJHI-UHFFFAOYSA-N 0.000 claims description 5
- 238000001816 cooling Methods 0.000 claims description 5
- 125000002534 ethynyl group Chemical group [H]C#C* 0.000 claims description 5
- ABTOQLMXBSRXSM-UHFFFAOYSA-N silicon tetrafluoride Chemical compound F[Si](F)(F)F ABTOQLMXBSRXSM-UHFFFAOYSA-N 0.000 claims description 5
- 239000005720 sucrose Substances 0.000 claims description 5
- WQZGKKKJIJFFOK-GASJEMHNSA-N Glucose Natural products OC[C@H]1OC(O)[C@H](O)[C@@H](O)[C@@H]1O WQZGKKKJIJFFOK-GASJEMHNSA-N 0.000 claims description 4
- 239000003822 epoxy resin Substances 0.000 claims description 4
- 239000008103 glucose Substances 0.000 claims description 4
- 229920001568 phenolic resin Polymers 0.000 claims description 4
- 239000005011 phenolic resin Substances 0.000 claims description 4
- 229920000647 polyepoxide Polymers 0.000 claims description 4
- VGGSQFUCUMXWEO-UHFFFAOYSA-N Ethene Chemical compound C=C VGGSQFUCUMXWEO-UHFFFAOYSA-N 0.000 claims description 3
- 239000004698 Polyethylene Substances 0.000 claims description 3
- WQZGKKKJIJFFOK-VFUOTHLCSA-N beta-D-glucose Chemical compound OC[C@H]1O[C@@H](O)[C@H](O)[C@@H](O)[C@@H]1O WQZGKKKJIJFFOK-VFUOTHLCSA-N 0.000 claims description 3
- 239000001307 helium Substances 0.000 claims description 3
- 229910052734 helium Inorganic materials 0.000 claims description 3
- SWQJXJOGLNCZEY-UHFFFAOYSA-N helium atom Chemical compound [He] SWQJXJOGLNCZEY-UHFFFAOYSA-N 0.000 claims description 3
- XIXADJRWDQXREU-UHFFFAOYSA-M lithium acetate Chemical compound [Li+].CC([O-])=O XIXADJRWDQXREU-UHFFFAOYSA-M 0.000 claims description 3
- -1 polyethylene Polymers 0.000 claims description 3
- 229920000573 polyethylene Polymers 0.000 claims description 3
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- 239000002243 precursor Substances 0.000 abstract description 21
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- 239000010406 cathode material Substances 0.000 abstract description 12
- 239000011204 carbon fibre-reinforced silicon carbide Substances 0.000 abstract description 9
- HBBGRARXTFLTSG-UHFFFAOYSA-N Lithium ion Chemical compound [Li+] HBBGRARXTFLTSG-UHFFFAOYSA-N 0.000 abstract description 8
- 229910001416 lithium ion Inorganic materials 0.000 abstract description 6
- 238000012986 modification Methods 0.000 abstract description 4
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- 239000002245 particle Substances 0.000 description 5
- 239000007774 positive electrode material Substances 0.000 description 5
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- KXGFMDJXCMQABM-UHFFFAOYSA-N 2-methoxy-6-methylphenol Chemical compound [CH]OC1=CC=CC([CH])=C1O KXGFMDJXCMQABM-UHFFFAOYSA-N 0.000 description 3
- 239000013078 crystal Substances 0.000 description 3
- 150000002500 ions Chemical class 0.000 description 3
- 239000012299 nitrogen atmosphere Substances 0.000 description 3
- 238000011160 research Methods 0.000 description 3
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 2
- 239000005977 Ethylene Substances 0.000 description 2
- 239000012300 argon atmosphere Substances 0.000 description 2
- 238000004146 energy storage Methods 0.000 description 2
- 238000003746 solid phase reaction Methods 0.000 description 2
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- 229910052493 LiFePO4 Inorganic materials 0.000 description 1
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- 125000002791 glucosyl group Chemical group C1([C@H](O)[C@@H](O)[C@H](O)[C@H](O1)CO)* 0.000 description 1
- 125000005842 heteroatom Chemical group 0.000 description 1
- 238000009830 intercalation Methods 0.000 description 1
- 230000002687 intercalation Effects 0.000 description 1
- 229910000398 iron phosphate Inorganic materials 0.000 description 1
- WBJZTOZJJYAKHQ-UHFFFAOYSA-K iron(3+) phosphate Chemical compound [Fe+3].[O-]P([O-])([O-])=O WBJZTOZJJYAKHQ-UHFFFAOYSA-K 0.000 description 1
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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
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Abstract
本发明公开了一种磷酸铁锂正极材料的制备方法。该方法针对磷酸铁锂材料现有改性不足之处,在合成前驱体中加入一定量的碳源结合烧结过程中引入碳源气体和硅源气体,利用化学气相沉积的方法在磷酸铁锂材料表面均匀沉积一层SiC包覆层,实现表面具有均匀SiC/C包覆层的磷酸铁锂材料的制备。合成过程中通过调节前驱体中碳源加入量和气相沉积过程中碳源、硅源气体的进气压力、流量及气相沉积时间,获得表面具有均匀的C/SiC包覆层的磷酸铁锂正极材料。这种材料具有较小的一次粒径,表面具有一层均匀紧密的C/SiC包覆层,具有较高的振实密度,其具有较好的倍率充放电性能,加工性能优异。在动力锂离子电池领域具有广泛的应用前景。
The invention discloses a preparation method of lithium iron phosphate cathode material. This method aims at the shortcomings of the existing modification of lithium iron phosphate materials. A certain amount of carbon source is added to the synthetic precursor and carbon source gas and silicon source gas are introduced during the sintering process. A layer of SiC coating layer is evenly deposited on the surface to realize the preparation of lithium iron phosphate material with a uniform SiC/C coating layer on the surface. During the synthesis process, the lithium iron phosphate positive electrode with a uniform C/SiC coating layer on the surface was obtained by adjusting the amount of carbon source added in the precursor and the inlet pressure, flow rate and vapor deposition time of the carbon source and silicon source gas during the vapor deposition process. Material. This material has a small primary particle size, a uniform and compact C/SiC coating layer on the surface, a high tap density, good rate charge and discharge performance, and excellent processing performance. It has broad application prospects in the field of power lithium-ion batteries.
Description
技术领域technical field
本发明涉及电化学材料制备和新能源领域,尤其涉及一种磷酸铁锂正极材料的制备方法。The invention relates to the fields of electrochemical material preparation and new energy, in particular to a preparation method of lithium iron phosphate cathode material.
背景技术Background technique
随着能源危机的日益加剧,全球都在寻找新的可再生资源,可再生资源如太阳能、风能、潮汐能、地热能等具有地域性喝时间性的特点。要充分利用这些资源,需要智能电网或者大规模的储能系统。锂离子电池作为储能电势有着良好的应用前景。另一方面,石化能源的日益枯竭迫使人们开发混合电动或纯电动交通工具,其核心部件电池成为研究重点。锂离子与其他电池相比其较高的能量密度,良好的安全性和较长的使用寿命而备受亲睐。With the increasing energy crisis, the whole world is looking for new renewable resources. Renewable resources such as solar energy, wind energy, tidal energy, geothermal energy, etc. have regional and temporal characteristics. To make full use of these resources, smart grids or large-scale energy storage systems are required. Lithium-ion batteries have promising application prospects as energy storage potentials. On the other hand, the depletion of petrochemical energy forces people to develop hybrid electric or pure electric vehicles, and its core component battery has become a research focus. Compared with other batteries, lithium-ion is favored for its high energy density, good safety and long service life.
磷酸铁锂材料作为锂离子电池正极材料,以其原料丰富、价格低廉、绿色环保、工作电压适中、热稳定性好等优点,引起了人们的广泛关注。Lithium iron phosphate material, as the cathode material of lithium-ion batteries, has attracted widespread attention due to its abundant raw materials, low price, environmental protection, moderate working voltage, and good thermal stability.
经过多年的研究发展,其性能得到了明显的改善,但是,磷酸铁锂仍存在离子传导率和电子传导率均较低的问题,高倍率充放电时性能较差。目前对磷酸铁锂材料的改性研究主要通过以下几种方式:(1)纳米化处理,减小合成磷酸铁锂的晶粒尺寸可以提高磷酸铁锂的离子传导率。晶体颗粒半径越小,锂离子在离子中的固相扩散过程越短,锂离子嵌入脱出就越容易;(2)元素掺杂,在材料晶格中引入杂原子以提高材料的电导率,但是其可行性和工作机理目前尚部清晰,效果不明显,也会随着随着元素掺杂量的增加容量降低;(3)掺杂导电剂,可以提高材料的电子导电率,大部分采用碳包覆技术,因碳材料形式复杂,大部分碳包覆后的磷酸铁锂材料振实密度会大大降低,加工性能会受到一定的影响。After years of research and development, its performance has been significantly improved. However, lithium iron phosphate still has the problem of low ion conductivity and electronic conductivity, and its performance is poor when charging and discharging at high rates. At present, the research on the modification of lithium iron phosphate materials is mainly through the following methods: (1) Nano treatment, reducing the grain size of synthesized lithium iron phosphate can improve the ion conductivity of lithium iron phosphate. The smaller the crystal particle radius, the shorter the solid phase diffusion process of lithium ions in the ions, and the easier the intercalation and extraction of lithium ions; (2) element doping, introducing heteroatoms into the material lattice to improve the electrical conductivity of the material, but Its feasibility and working mechanism are still unclear at present, and the effect is not obvious, and the capacity will decrease with the increase of element doping amount; (3) Doping with conductive agent can improve the electronic conductivity of the material, and most of them use carbon Coating technology, due to the complex form of carbon materials, the tap density of most carbon-coated lithium iron phosphate materials will be greatly reduced, and the processing performance will be affected to a certain extent.
关于磷酸铁锂材料的改性研究比较多,但是目前还未发现在前驱体中加入碳源结合烧结过程中气相沉积SiC来合成小粒径且具有紧密的SiC/C碳包覆层的磷酸铁锂材料的研究。There are many studies on the modification of lithium iron phosphate materials, but it has not been found that adding carbon source to the precursor combined with vapor deposition of SiC during the sintering process to synthesize iron phosphate with small particle size and tight SiC/C carbon coating Research on lithium materials.
发明内容Contents of the invention
本发明要解决的技术问题是提供一种磷酸铁锂正极材料的制备方法。The technical problem to be solved by the present invention is to provide a preparation method of lithium iron phosphate cathode material.
为了解决上述技术问题,本发明采用的技术方案是:一种磷酸铁锂正极材料的制备方法,其特征在于包括以下步骤:In order to solve the above-mentioned technical problems, the technical solution adopted in the present invention is: a preparation method of lithium iron phosphate cathode material, which is characterized in that it comprises the following steps:
1)按照摩尔比Li∶Fe∶P∶C=1.02∶1∶1∶0.2~0.5称取锂源、草酸亚铁、磷酸二氢铵、有机碳源,以酒精或丙酮为分散剂进行球磨分散处理,再进行真空干燥处理获得前驱体;1) Weigh the lithium source, ferrous oxalate, ammonium dihydrogen phosphate, and organic carbon source according to the molar ratio Li:Fe:P:C=1.02:1:1:0.2~0.5, and use alcohol or acetone as the dispersant for ball milling to disperse treatment, and then vacuum drying treatment to obtain the precursor;
2)将所述前驱体置于管式炉中550℃条件下,氮气保护下进行预烧,升温速率5℃/分钟,保温时间5小时,自然冷却降至室温,对预烧料进行粗粉碎;2) Place the precursor in a tube furnace at 550°C and pre-burn it under the protection of nitrogen. The heating rate is 5°C/min, the holding time is 5 hours, and it is naturally cooled down to room temperature, and the pre-burned material is coarsely pulverized ;
3)将经过粗粉碎的预烧料置于管式炉中进行二次烧结,在惰性气体保护下以5℃/分钟的升温速率升至700-750℃,保温8-15小时;升温过程中惰性气体进气压力为0.15MPa,流量为0.1L/min;当温度达到设定温度后,引入碳源气体和硅源气体进行气相沉积包覆,气相沉积过程中碳源气体进气压力0.1~0.2MPa,流量为0.04~0.12L/min;硅源气体进气压力0.1~0.2MPa,流量为0.04~0.12L/min;同时调节惰性气体进气压力0.1~0.2MPa,流量为0.04~0.12L/min;气相沉积时间30min-240min后,关闭碳源气体和硅源气体进气,保持惰性气体进气压力0.15MPa,流量为0.1L/min;在此惰性气氛下完成余下的烧结过程,并自然冷却至室温,即得到具有表面C/SiC包覆层的磷酸铁锂正极材料。3) Place the coarsely crushed calcined material in a tube furnace for secondary sintering, raise the temperature to 700-750°C at a rate of 5°C/min under the protection of an inert gas, and keep it warm for 8-15 hours; The inlet pressure of the inert gas is 0.15MPa, and the flow rate is 0.1L/min; when the temperature reaches the set temperature, carbon source gas and silicon source gas are introduced for vapor deposition and coating. During the vapor deposition process, the inlet pressure of carbon source gas is 0.1~ 0.2MPa, the flow rate is 0.04-0.12L/min; the silicon source gas inlet pressure is 0.1-0.2MPa, the flow rate is 0.04-0.12L/min; at the same time, the inert gas inlet pressure is adjusted to 0.1-0.2MPa, and the flow rate is 0.04-0.12L /min; after the vapor deposition time is 30min-240min, close the intake of carbon source gas and silicon source gas, keep the inlet pressure of inert gas at 0.15MPa, and the flow rate at 0.1L/min; complete the rest of the sintering process under this inert atmosphere, and Cool naturally to room temperature to obtain a lithium iron phosphate positive electrode material with a surface C/SiC coating layer.
作为优选,步骤1)中所述的锂源为碳酸锂、氢氧化锂、醋酸锂、氟化锂中的一种或至少两种的组合;所述有机碳源为葡萄糖、蔗糖、酚醛树脂、环氧树脂或聚乙烯中的一种或至少两种的组合。As preferably, the lithium source described in step 1) is one or a combination of at least two of lithium carbonate, lithium hydroxide, lithium acetate, lithium fluoride; the organic carbon source is glucose, sucrose, phenolic resin, One or a combination of at least two of epoxy resin or polyethylene.
作为另一个优选,步骤3)中所述的碳源气体为甲烷、乙烷、乙烯、乙炔、苯、甲苯中的一种或至少两种的组合;所述硅源气体为甲硅烷、乙硅烷、四氟化硅中一种或至少两种的组合。As another preference, the carbon source gas described in step 3) is one or a combination of at least two of methane, ethane, ethylene, acetylene, benzene, toluene; the silicon source gas is monosilane, disilane 1. One or a combination of at least two of silicon tetrafluoride.
还有一个优选,步骤3)中所述的惰性气体为氦气、氮气和氩气中的一种或至少两种的混合气体。Still another preference, the inert gas described in step 3) is one or a mixture of at least two of helium, nitrogen and argon.
本发明的有益效果是:The beneficial effects of the present invention are:
结合在前驱体中加入碳源并在后续的热处理过程中通过化学气相沉积过程引入SiC,有效抑制了传统固相反应过程中晶体颗粒的长大,实现了在磷酸铁锂材料表面均匀包覆C/SiC层,这种材料具有优异的倍率充放电性能和加工性能。Combining the addition of carbon source to the precursor and the introduction of SiC through the chemical vapor deposition process in the subsequent heat treatment process, the growth of crystal particles in the traditional solid-state reaction process is effectively inhibited, and the uniform coating of C on the surface of lithium iron phosphate material is realized. /SiC layer, this material has excellent rate charge and discharge performance and processing performance.
附图说明Description of drawings
下面结合附图和具体实施方式对本发明作进一步详细的说明。The present invention will be further described in detail below in conjunction with the accompanying drawings and specific embodiments.
图1是本发明磷酸铁锂正极材料的制备方法实施例3所获得磷酸铁锂材料的TEM图。Fig. 1 is a TEM image of the lithium iron phosphate material obtained in Example 3 of the preparation method of the lithium iron phosphate cathode material of the present invention.
图2是本发明磷酸铁锂正极材料的制备方法实施例3中所获得磷酸铁锂材料的SEM图。Fig. 2 is an SEM image of the lithium iron phosphate material obtained in Example 3 of the preparation method of the lithium iron phosphate cathode material of the present invention.
图3是本发明磷酸铁锂正极材料的制备方法实施例3中所获得磷酸铁锂材料与对比实施例中所获得磷酸铁锂材料0.2C倍率下放电曲线对比图。3 is a comparison chart of the discharge curves of the lithium iron phosphate material obtained in Example 3 of the preparation method of the lithium iron phosphate cathode material of the present invention and the lithium iron phosphate material obtained in the comparative example at a rate of 0.2C.
图中,a为C/SiC气相沉积包覆磷酸铁锂,b为碳包覆磷酸铁锂,c为SiC气相沉积包覆磷酸铁锂,d为纯相磷酸铁锂。In the figure, a is C/SiC vapor deposition coated lithium iron phosphate, b is carbon coated lithium iron phosphate, c is SiC vapor deposition coated lithium iron phosphate, and d is pure phase lithium iron phosphate.
图4是本发明磷酸铁锂正极材料的制备方法实施例3中所获得磷酸铁锂材料的倍率放电曲线图。4 is a rate discharge curve of the lithium iron phosphate material obtained in Example 3 of the preparation method of the lithium iron phosphate cathode material of the present invention.
具体实施方式Detailed ways
实施例1Example 1
1)按照摩尔比Li∶Fe∶P∶C=1.02∶1∶1∶0.2称取碳酸锂、草酸亚铁、磷酸二氢铵、蔗糖,以酒精为分散剂进行球磨分散处理5小时,再进行真空干燥处理获得前驱体;将上述所获得的干燥前驱体置于管式炉中550℃条件下,氮气保护下进行预烧,升温速率5℃/分钟,保温时间5小时,自然冷却降至室温,对预烧料进行粗粉碎;1) Weigh lithium carbonate, ferrous oxalate, ammonium dihydrogen phosphate, and sucrose according to the molar ratio Li:Fe:P:C=1.02:1:1:0.2, and carry out ball milling dispersion treatment with alcohol as a dispersant for 5 hours, and then carry out The precursor was obtained by vacuum drying; the dry precursor obtained above was placed in a tube furnace at 550°C and pre-fired under the protection of nitrogen. The heating rate was 5°C/min, and the holding time was 5 hours. Natural cooling down to room temperature , coarsely pulverize the calcined material;
2)将上述所获得的经过粗粉碎的预烧料置于管式炉中进行二次烧结,在氮气保护下以5℃/分钟的升温速率升至700℃,保温10小时。升温过程中氮气进气压力为0.15MPa,流量为0.1L/min。当温度达到设定温度后,引入甲烷气体和甲硅烷气体进行气相沉积包覆,气相沉积过程中甲烷气体进气压力0.1MPa,流量为0.12L/min,甲硅烷气体进气压力0.1MPa,流量为0.12L/min,同时调节氮气进气压力0.1MPa,流量为0.04L/min。气相沉积时间30min后,关闭甲烷气体和甲硅烷气体进气,保持氮气进气压力0.15MPa,流量为0.1L/min,在此氮气气氛下完成余下的烧结过程,并自然冷却至室温,即得到具有表面C/SiC包覆层的磷酸铁锂正极材料。该材料的振实密度为1.05g/cm3。2) Place the coarsely pulverized calcined material obtained above in a tube furnace for secondary sintering, and raise the temperature to 700° C. at a rate of 5° C./min under the protection of nitrogen, and keep it warm for 10 hours. During the heating process, the nitrogen inlet pressure is 0.15MPa, and the flow rate is 0.1L/min. When the temperature reaches the set temperature, introduce methane gas and monosilane gas for vapor deposition coating. During vapor deposition, the inlet pressure of methane gas is 0.1MPa, the flow rate is 0.12L/min, the inlet pressure of monosilane gas is 0.1MPa, and the flow rate is 0.1MPa. 0.12L/min, while adjusting the nitrogen inlet pressure to 0.1MPa, and the flow rate to 0.04L/min. After 30 minutes of vapor deposition, turn off the intake of methane gas and monosilane gas, keep the nitrogen intake pressure at 0.15MPa, and the flow rate at 0.1L/min, complete the rest of the sintering process in this nitrogen atmosphere, and naturally cool to room temperature, that is, A lithium iron phosphate cathode material with a surface C/SiC coating layer. The material had a tap density of 1.05 g/cm 3 .
实施例2Example 2
1)按照摩尔比Li∶Fe∶P∶C=1.02∶1∶1∶0.3称取碳酸锂、草酸亚铁、磷酸二氢铵、葡萄糖,以丙酮为分散剂进行球磨分散处理5小时,再进行真空干燥处理获得前驱体;将上述所获得的干燥前驱体置于管式炉中550℃条件下,氩气保护下进行预烧,升温速率5℃/分钟,保温时间5小时,自然冷却降至室温,对预烧料进行粗粉碎;1) Weigh lithium carbonate, ferrous oxalate, ammonium dihydrogen phosphate, and glucose according to the molar ratio Li:Fe:P:C=1.02:1:1:0.3, and use acetone as a dispersant to carry out ball milling dispersion treatment for 5 hours, and then carry out The precursor was obtained by vacuum drying; the dry precursor obtained above was placed in a tube furnace at 550°C and pre-fired under the protection of argon. The heating rate was 5°C/min, the holding time was 5 hours, and the natural cooling decreased to At room temperature, coarsely pulverize the calcined material;
2)将上述所获得的经过粗粉碎的预烧料置于管式炉中进行二次烧结,在氩气保护下以5℃/分钟的升温速率升至720℃,保温10小时。升温过程中氩气进气压力为0.15MPa,流量为0.1L/min。当温度达到设定温度后,引入乙烷气体和乙硅烷气体进行气相沉积包覆,气相沉积过程中乙烷气体进气压力0.12MPa,流量为0.1L/min,乙硅烷气体进气压力0.12MPa,流量为0.1L/min,同时调节氩气进气压力0.1MPa,流量为0.08L/min。气相沉积时间60min后,关闭乙烷气体和乙硅烷气体进气,保持氩气进气压力0.15MPa,流量为0.1L/min,在此氩气气氛下完成余下的烧结过程,并自然冷却至室温,即得到具有表面C/SiC包覆层的磷酸铁锂正极材料。该材料的振实密度为1.1g/cm3。2) Place the coarsely pulverized calcined material obtained above in a tube furnace for secondary sintering, and raise the temperature to 720° C. at a rate of 5° C./min under the protection of argon, and keep it warm for 10 hours. During the heating process, the argon inlet pressure is 0.15MPa, and the flow rate is 0.1L/min. When the temperature reaches the set temperature, introduce ethane gas and disilane gas for vapor deposition coating. During the vapor deposition process, the inlet pressure of ethane gas is 0.12MPa, the flow rate is 0.1L/min, and the inlet pressure of disilane gas is 0.12MPa , the flow rate is 0.1L/min, and at the same time adjust the argon inlet pressure to 0.1MPa, and the flow rate is 0.08L/min. After 60 minutes of vapor deposition, turn off the ethane gas and disilane gas inlets, keep the argon inlet pressure at 0.15MPa, and the flow rate at 0.1L/min, complete the rest of the sintering process in this argon atmosphere, and naturally cool to room temperature , that is, a lithium iron phosphate positive electrode material with a surface C/SiC coating layer is obtained. The tap density of this material was 1.1 g/cm 3 .
实施例3Example 3
1)按照摩尔比Li∶Fe∶P∶C=1.02∶1∶1∶0.35称取碳酸锂、草酸亚铁、磷酸二氢铵、酚醛树脂,以酒精为分散剂进行球磨分散处理5小时,再进行真空干燥处理获得前驱体;将上述所获得的干燥前驱体置于管式炉中550℃条件下,氮气保护下进行预烧,升温速率5℃/分钟,保温时间5小时,自然冷却降至室温,对预烧料进行粗粉碎;1) Weigh lithium carbonate, ferrous oxalate, ammonium dihydrogen phosphate, and phenolic resin according to the molar ratio Li:Fe:P:C=1.02:1:1:0.35, and carry out ball milling dispersion treatment with alcohol as a dispersant for 5 hours, and then Carry out vacuum drying to obtain the precursor; place the dry precursor obtained above in a tube furnace at 550°C and pre-burn under the protection of nitrogen. The heating rate is 5°C/min, the holding time is 5 hours, and the natural cooling is reduced to At room temperature, coarsely pulverize the calcined material;
2)将上述所获得的经过粗粉碎的预烧料置于管式炉中进行二次烧结,在氮气保护下以5℃/分钟的升温速率升至740℃,保温10小时。升温过程中氮气气体进气压力为0.15MPa,流量为0.1L/min。当温度达到设定温度后,引入甲烷气体和甲硅烷气体进行气相沉积包覆,气相沉积过程中甲烷气体进气压力0.12MPa,流量为0.08L/min,甲硅烷气体进气压力0.12MPa,流量为0.08L/min,同时调节氮气气体进气压力0.1MPa,流量为0.1L/min。气相沉积时间120min后,关闭甲烷气体和甲硅烷气体进气,保持氮气气体进气压力0.15MPa,流量为0.1L/min,在此氮气气氛下完成余下的烧结过程,并自然冷却至室温,即得到具有表面C/SiC包覆层的磷酸铁锂正极材料。该材料的振实密度为1.3g/cm3,所获得的磷酸铁锂材料的TEM和SEM分别如图1、图2所示,半电池充放电曲线如图3所示。2) Place the coarsely pulverized calcined material obtained above in a tube furnace for secondary sintering, and raise the temperature to 740° C. at a rate of 5° C./min under the protection of nitrogen, and keep it warm for 10 hours. During the heating process, the inlet pressure of nitrogen gas is 0.15MPa, and the flow rate is 0.1L/min. When the temperature reaches the set temperature, introduce methane gas and monosilane gas for vapor deposition coating. During the vapor deposition process, the inlet pressure of methane gas is 0.12MPa, the flow rate is 0.08L/min, the inlet pressure of monosilane gas is 0.12MPa, and the flow rate 0.08L/min, while adjusting the nitrogen gas inlet pressure to 0.1MPa, and the flow rate to 0.1L/min. After 120 minutes of vapor deposition, close the intake of methane gas and monosilane gas, keep the intake pressure of nitrogen gas at 0.15MPa, and the flow rate at 0.1L/min, complete the rest of the sintering process in this nitrogen atmosphere, and naturally cool to room temperature, that is A lithium iron phosphate cathode material with a surface C/SiC coating layer is obtained. The tap density of the material is 1.3g/cm 3 . The TEM and SEM of the obtained lithium iron phosphate material are shown in Figure 1 and Figure 2 respectively, and the half-cell charge and discharge curve is shown in Figure 3 .
实施例4Example 4
1)按照摩尔比Li∶Fe∶P∶C=1.02∶1∶1∶0.5称取碳酸锂、草酸亚铁、磷酸二氢铵、环氧树脂,以丙酮为分散剂进行球磨分散处理5小时,再进行真空干燥处理获得前驱体;将上述所获得的干燥前驱体置于管式炉中550℃条件下,氩气保护下进行预烧,升温速率5℃/分钟,保温时间5小时,自然冷却降至室温,对预烧料进行粗粉碎;1) Weigh lithium carbonate, ferrous oxalate, ammonium dihydrogen phosphate, and epoxy resin according to the molar ratio Li:Fe:P:C=1.02:1:1:0.5, and use acetone as a dispersant to carry out ball milling dispersion treatment for 5 hours, Then carry out vacuum drying treatment to obtain the precursor; place the dry precursor obtained above in a tube furnace at 550°C, and pre-burn it under the protection of argon, with a heating rate of 5°C/min, a holding time of 5 hours, and natural cooling Cool down to room temperature, coarsely pulverize the calcined material;
2)将上述所获得的经过粗粉碎的预烧料置于管式炉中进行二次烧结,在氩气保护下以5℃/分钟的升温速率升至740℃,保温10小时。升温过程中氩气进气压力为0.15MPa,流量为0.1L/min。当温度达到设定温度后,引入乙炔气体和四氟化硅气体进行气相沉积包覆,气相沉积过程中乙炔气体进气压力0.2MPa,流量为0.04L/min,四氟化硅气体进气压力0.2MPa,流量为0.04L/min,同时调节氩气进气压力0.1MPa,流量为0.1L/min。气相沉积时间220min后,关闭乙炔气体和四氟化硅气体进气,保持氩气进气压力0.15MPa,流量为0.1L/min,在此氩气气氛下完成余下的烧结过程,并自然冷却至室温,即得到具有表面C/SiC包覆层的磷酸铁锂正极材料。该材料的振实密度为1.1g/cm3。2) Place the coarsely pulverized calcined material obtained above in a tube furnace for secondary sintering, and raise the temperature to 740° C. at a rate of 5° C./min under the protection of argon, and keep it warm for 10 hours. During the heating process, the argon inlet pressure is 0.15MPa, and the flow rate is 0.1L/min. When the temperature reaches the set temperature, acetylene gas and silicon tetrafluoride gas are introduced for vapor deposition coating. 0.2MPa, the flow rate is 0.04L/min, and at the same time, adjust the argon inlet pressure to 0.1MPa, and the flow rate is 0.1L/min. After 220 minutes of vapor deposition, close the acetylene gas and silicon tetrafluoride gas inlet, keep the argon inlet pressure at 0.15MPa, and the flow rate at 0.1L/min, complete the rest of the sintering process in this argon atmosphere, and cool naturally to At room temperature, a lithium iron phosphate positive electrode material with a surface C/SiC coating layer is obtained. The tap density of this material was 1.1 g/cm 3 .
对比实施例1Comparative Example 1
1)按照摩尔比Li∶Fe∶P∶C=i.02∶1∶1∶0.35称取碳酸锂、草酸亚铁、磷酸二氢铵、蔗糖,以酒精为分散剂进行球磨分散处理5小时,再进行真空干燥处理获得前驱体;将上述所获得的干燥前驱体置于管式炉中550℃条件下,氮气保护下进行预烧,升温速率5℃/分钟,保温时间5小时,自然冷却降至室温,对预烧料进行粗粉碎;1) Weigh lithium carbonate, ferrous oxalate, ammonium dihydrogen phosphate, and sucrose according to the molar ratio Li:Fe:P:C=i.02:1:1:0.35, and carry out ball milling dispersion treatment with alcohol as a dispersant for 5 hours, Then carry out vacuum drying treatment to obtain the precursor; place the dry precursor obtained above in a tube furnace at 550 ° C, and pre-burn it under the protection of nitrogen. The heating rate is 5 ° C / min, and the holding time is 5 hours. To room temperature, coarsely pulverize the calcined material;
2)将上述所获得的经过粗粉碎的预烧料置于管式炉中进行二次烧结,在氮气气体保护下以5℃/分钟的升温速率升至740℃,保温10小时。过程中氮气气体进气压力为0.15MPa,流量为0.1L/min。并自然冷却至室温,即得到未经过气相沉积过程的碳包覆磷酸铁锂正极材料。该材料的振实密度为0.85g/cm3。2) Put the coarsely pulverized calcined material obtained above into a tube furnace for secondary sintering, and raise the temperature to 740° C. at a rate of 5° C./min under the protection of nitrogen gas, and keep it warm for 10 hours. During the process, the inlet pressure of nitrogen gas is 0.15MPa, and the flow rate is 0.1L/min. And naturally cooled to room temperature, that is, a carbon-coated lithium iron phosphate positive electrode material that has not undergone a vapor phase deposition process is obtained. The material has a tap density of 0.85 g/cm 3 .
对比实施例2Comparative Example 2
1)按照摩尔比Li∶Fe∶P=1.02∶1∶1称取碳酸锂、草酸亚铁、磷酸二氢铵,以酒精为分散剂进行球磨分散处理5小时,再进行真空干燥处理获得前驱体;将上述所获得的干燥前驱体置于管式炉中550℃条件下,氮气保护下进行预烧,升温速率5℃/分钟,保温时间5小时,自然冷却降至室温,对预烧料进行粗粉碎;1) Weigh lithium carbonate, ferrous oxalate, and ammonium dihydrogen phosphate according to the molar ratio Li:Fe:P=1.02:1:1, use alcohol as a dispersant for ball milling and dispersing for 5 hours, and then vacuum dry to obtain the precursor ; Place the dry precursor obtained above in a tube furnace at 550°C, under the protection of nitrogen for pre-burning, the heating rate is 5°C/min, the holding time is 5 hours, naturally cool down to room temperature, and the pre-fired material is Coarse crushing;
2)将上述所获得的经过粗粉碎的预烧料置于管式炉中进行二次烧结,在氮气保护下以5℃/分钟的升温速率升至740℃,保温10小时。升温过程中氮气气体进气压力为0.15MPa,流量为0.1L/min。当温度达到设定温度后,引入甲烷气体和甲硅烷气体进行气相沉积包覆,气相沉积过程中甲烷气体进气压力0.12MPa,流量为0.08L/min,甲硅烷气体进气压力0.12MPa,流量为0.08L/min,同时调节氮气气体进气压力0.1MPa,流量为0.1L/min。气相沉积时间120min后,关闭甲烷气体和甲硅烷气体进气,保持氮气气体进气压力0.15MPa,流量为0.1L/min,在此氮气气氛下完成余下的烧结过程,并自然冷却至室温,即得到具有表面SiC包覆层的磷酸铁锂正极材料。该材料的振实密度为1.15g/cm3。2) Place the coarsely pulverized calcined material obtained above in a tube furnace for secondary sintering, and raise the temperature to 740° C. at a rate of 5° C./min under the protection of nitrogen, and keep it warm for 10 hours. During the heating process, the inlet pressure of nitrogen gas is 0.15MPa, and the flow rate is 0.1L/min. When the temperature reaches the set temperature, introduce methane gas and monosilane gas for vapor deposition coating. During the vapor deposition process, the inlet pressure of methane gas is 0.12MPa, the flow rate is 0.08L/min, the inlet pressure of monosilane gas is 0.12MPa, and the flow rate 0.08L/min, while adjusting the nitrogen gas inlet pressure to 0.1MPa, and the flow rate to 0.1L/min. After 120 minutes of vapor deposition, close the intake of methane gas and monosilane gas, keep the intake pressure of nitrogen gas at 0.15MPa, and the flow rate at 0.1L/min, complete the rest of the sintering process in this nitrogen atmosphere, and naturally cool to room temperature, that is A lithium iron phosphate cathode material with a surface SiC coating layer is obtained. The material had a tap density of 1.15 g/cm 3 .
对比实施例3Comparative Example 3
1)按照摩尔比Li∶Fe∶P=i.02∶1∶1称取碳酸锂、草酸亚铁、磷酸二氢铵,以酒精为分散剂进行球磨分散处理5小时,再进行真空干燥处理获得前驱体;将上述所获得的干燥前驱体置于管式炉中550℃条件下,氮气保护下进行预烧,升温速率5℃/分钟,保温时间5小时,自然冷却降至室温,对预烧料进行粗粉碎;1) Weigh lithium carbonate, ferrous oxalate, and ammonium dihydrogen phosphate according to the molar ratio Li:Fe:P=i.02:1:1, use alcohol as a dispersant for ball milling and dispersing for 5 hours, and then vacuum dry to obtain Precursor: Place the dry precursor obtained above in a tube furnace at 550°C under the protection of nitrogen for pre-calcination, the heating rate is 5°C/min, the holding time is 5 hours, and naturally cool down to room temperature. The material is coarsely crushed;
2)将上述所获得的经过粗粉碎的预烧料置于管式炉中进行二次烧结,在氮气气体保护下以5℃/分钟的升温速率升至740℃,保温10小时。过程中氮气气体进气压力为0.15MPa,流量为0.1L/min。并自然冷却至室温,即得到经固相反应获得的纯相磷酸铁锂正极材料。该材料的振实密度为1.0g/cm3。2) Put the coarsely pulverized calcined material obtained above into a tube furnace for secondary sintering, and raise the temperature to 740° C. at a rate of 5° C./min under the protection of nitrogen gas, and keep it warm for 10 hours. During the process, the inlet pressure of nitrogen gas is 0.15MPa, and the flow rate is 0.1L/min. And naturally cooled to room temperature, the pure-phase lithium iron phosphate positive electrode material obtained through solid-state reaction is obtained. The material had a tap density of 1.0 g/cm 3 .
将上述实施例和对比实施例中所获得的磷酸铁锂材料组装成扣式电池,极片中活性物质配比为LiFeP04∶SP∶PVDF=80∶10∶10,采用采用Clgard2300型隔膜,对电极为金属锂片,分别以0.2C、1C、4C、5C倍率进行放电,充电倍率固定为0.2C,充放电电压范围为2.0-4.0V。实施例3和对比实施例1、例2、例3所获得的C/SiC包覆、C包覆、SiC包覆以及纯相的磷酸铁锂材料的充放电曲线如图3所示。The lithium iron phosphate material obtained in the above-mentioned examples and comparative examples was assembled into a button battery, the ratio of the active material in the pole piece was LiFeP04:SP:PVDF=80:10:10, the Clgard2300 type diaphragm was adopted, and the counter electrode It is a metal lithium sheet, which is discharged at 0.2C, 1C, 4C, and 5C rates, the charge rate is fixed at 0.2C, and the charge and discharge voltage range is 2.0-4.0V. The charge-discharge curves of the C/SiC-coated, C-coated, SiC-coated and pure-phase lithium iron phosphate materials obtained in Example 3 and Comparative Example 1, Example 2, and Example 3 are shown in FIG. 3 .
实施例与对比实施例结果表明:磷酸铁锂材料的合成,通过在前驱体中加入有机碳源,以及后续烧结过程中进行CVD气相沉积过程,一方面有效抑制了烧结过程中晶体颗粒的长大,合成了小粒径的磷酸铁锂,另一方面实现了对磷酸铁锂材料表面的C/CSi紧密包覆,有效解决了单纯碳包覆磷酸铁锂材料振实密度低的问题。与碳包覆磷酸铁锂、气相沉积SiC包覆以及纯相磷酸铁锂材料相比,具有更高的放电比容量和优异的倍率放电性能。The results of Examples and Comparative Examples show that: the synthesis of lithium iron phosphate materials, by adding an organic carbon source to the precursor, and performing CVD vapor deposition process in the subsequent sintering process, on the one hand, effectively inhibits the growth of crystal particles during the sintering process , synthesized lithium iron phosphate with small particle size, on the other hand, realized the tight coating of C/CSi on the surface of lithium iron phosphate material, effectively solved the problem of low tap density of pure carbon-coated lithium iron phosphate material. Compared with carbon-coated lithium iron phosphate, vapor deposition SiC coating and pure phase lithium iron phosphate materials, it has higher discharge specific capacity and excellent rate discharge performance.
上述实施例中,有机碳源至列举了蔗糖的情况,选用其他有机碳源如葡萄糖、酚醛树脂、环氧树脂和聚乙烯与这种有机碳源所产生的实验结果是相似的;实施例中,锂源至列举了碳酸锂的情况,选用其他锂源如氢氧化锂、醋酸锂、氟化锂与碳酸锂产生了相似的实验结果;选用其他碳源气体如甲烷、乙烷、乙烯、乙炔、苯、甲苯产生了相似的实验结果,选择其他的硅源气体如乙硅烷、四氟化硅产生了相似的实验结果,选择其他保护气体如氦气、氩气、二氧化碳与氮气产生了相似的实验结果。In the foregoing examples, the organic carbon source has listed the situation of sucrose, and other organic carbon sources such as glucose, phenolic resin, epoxy resin and polyethylene are similar to the experimental results produced by this organic carbon source; in the embodiment , the lithium source has listed the situation of lithium carbonate, the selection of other lithium sources such as lithium hydroxide, lithium acetate, lithium fluoride and lithium carbonate have produced similar experimental results; the selection of other carbon source gases such as methane, ethane, ethylene, acetylene , benzene, and toluene produced similar experimental results, and choosing other silicon source gases such as disilane and silicon tetrafluoride produced similar experimental results, and selecting other protective gases such as helium, argon, carbon dioxide, and nitrogen produced similar experimental results. Experimental results.
以上所述的本发明实施方式,并不构成对本发明保护范围的限定。任何在本发明的精神和原则之内所作的修改、等同替换和改进等,均应包含在本发明的权利要求保护范围之内。The embodiments of the present invention described above are not intended to limit the protection scope of the present invention. Any modifications, equivalent replacements and improvements made within the spirit and principle of the present invention shall be included in the protection scope of the claims of the present invention.
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Cited By (11)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN103794788A (en) * | 2014-02-21 | 2014-05-14 | 合肥国轩高科动力能源股份公司 | Surface carbon coating method of lithium iron phosphate positive electrode material |
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Citations (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN1741301A (en) * | 2005-09-09 | 2006-03-01 | 贵州新材料矿业发展有限公司 | Process for producing lithium ion battery anode material ferrtilithium phosphate |
CN101217195A (en) * | 2007-12-28 | 2008-07-09 | 龚思源 | A lithium ion battery anode material of lithium iron phosphate and the corresponding vapor deposition and cladding method of conductive network |
CN101533912A (en) * | 2008-03-11 | 2009-09-16 | 比亚迪股份有限公司 | Method for preparing lithium iron phosphate used as positive active material of lithium ion secondary battery |
WO2011069348A1 (en) * | 2009-12-11 | 2011-06-16 | 中国科学院宁波材料技术与工程研究所 | Lithium iron phosphate positive electrode active material modified by graphene, preparation method and lithium ion secondary battery thereof |
CN102347475A (en) * | 2010-07-27 | 2012-02-08 | 曾永斌 | High-performance lithium ion battery and preparation process thereof |
CN102522547A (en) * | 2011-12-28 | 2012-06-27 | 彩虹集团公司 | Preparation method for lithium ion fast conductor modified lithium iron phosphate material |
CN102664247A (en) * | 2012-04-01 | 2012-09-12 | 上海锦众信息科技有限公司 | Method for preparing LiFePO4/SiC lithium battery positive plate by microwave heating |
CN103151521A (en) * | 2013-02-22 | 2013-06-12 | 中国科学院过程工程研究所 | Positive electrode material of lithium ion battery and preparing method thereof |
CN103187569A (en) * | 2013-03-31 | 2013-07-03 | 复旦大学 | Preparation method for LiFePO4/C contained anode material for lithium ion battery |
-
2013
- 2013-07-26 CN CN201310321004.5A patent/CN103390750B/en active Active
Patent Citations (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN1741301A (en) * | 2005-09-09 | 2006-03-01 | 贵州新材料矿业发展有限公司 | Process for producing lithium ion battery anode material ferrtilithium phosphate |
CN101217195A (en) * | 2007-12-28 | 2008-07-09 | 龚思源 | A lithium ion battery anode material of lithium iron phosphate and the corresponding vapor deposition and cladding method of conductive network |
CN101533912A (en) * | 2008-03-11 | 2009-09-16 | 比亚迪股份有限公司 | Method for preparing lithium iron phosphate used as positive active material of lithium ion secondary battery |
WO2011069348A1 (en) * | 2009-12-11 | 2011-06-16 | 中国科学院宁波材料技术与工程研究所 | Lithium iron phosphate positive electrode active material modified by graphene, preparation method and lithium ion secondary battery thereof |
CN102347475A (en) * | 2010-07-27 | 2012-02-08 | 曾永斌 | High-performance lithium ion battery and preparation process thereof |
CN102522547A (en) * | 2011-12-28 | 2012-06-27 | 彩虹集团公司 | Preparation method for lithium ion fast conductor modified lithium iron phosphate material |
CN102664247A (en) * | 2012-04-01 | 2012-09-12 | 上海锦众信息科技有限公司 | Method for preparing LiFePO4/SiC lithium battery positive plate by microwave heating |
CN103151521A (en) * | 2013-02-22 | 2013-06-12 | 中国科学院过程工程研究所 | Positive electrode material of lithium ion battery and preparing method thereof |
CN103187569A (en) * | 2013-03-31 | 2013-07-03 | 复旦大学 | Preparation method for LiFePO4/C contained anode material for lithium ion battery |
Cited By (18)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN103794788A (en) * | 2014-02-21 | 2014-05-14 | 合肥国轩高科动力能源股份公司 | Surface carbon coating method of lithium iron phosphate positive electrode material |
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CN105514380A (en) * | 2015-12-21 | 2016-04-20 | 宁波高新区锦众信息科技有限公司 | Preparation method of LiFeSiO composite material for Li-ion batteries |
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JP2022508339A (en) * | 2018-08-14 | 2022-01-19 | エスジェー・アドバンスド・マテリアルズ・カンパニー・リミテッド | A lithium secondary battery equipped with a negative electrode active material, a method for producing the same, and a negative electrode containing the negative electrode. |
JP7559142B2 (en) | 2018-08-14 | 2024-10-01 | エスジェー・アドバンスド・マテリアルズ・カンパニー・リミテッド | Negative electrode active material, its manufacturing method, and lithium secondary battery having a negative electrode including the same |
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US11658292B2 (en) | 2019-12-30 | 2023-05-23 | Shanghai Shanshan Tech Co., Ltd. | Silicon-based anode material and preparation method thereof, lithium ion battery |
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