CN106159269A - A kind of preparation method of high-voltage lithium ion batteries cathode pole piece - Google Patents
A kind of preparation method of high-voltage lithium ion batteries cathode pole piece Download PDFInfo
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- 229910001416 lithium ion Inorganic materials 0.000 title claims abstract description 55
- HBBGRARXTFLTSG-UHFFFAOYSA-N Lithium ion Chemical compound [Li+] HBBGRARXTFLTSG-UHFFFAOYSA-N 0.000 title claims abstract description 53
- 238000002360 preparation method Methods 0.000 title claims abstract description 18
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims abstract description 19
- 229910002804 graphite Inorganic materials 0.000 claims abstract description 18
- 239000010439 graphite Substances 0.000 claims abstract description 18
- -1 organic acid ester Chemical class 0.000 claims abstract description 13
- 238000006243 chemical reaction Methods 0.000 claims abstract description 4
- 239000002002 slurry Substances 0.000 claims description 19
- 229910002099 LiNi0.5Mn1.5O4 Inorganic materials 0.000 claims description 15
- 239000011230 binding agent Substances 0.000 claims description 9
- 239000011248 coating agent Substances 0.000 claims description 9
- 238000000576 coating method Methods 0.000 claims description 9
- 239000006258 conductive agent Substances 0.000 claims description 8
- 239000000463 material Substances 0.000 claims description 8
- 239000007787 solid Substances 0.000 claims description 7
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 7
- RTAQQCXQSZGOHL-UHFFFAOYSA-N Titanium Chemical compound [Ti] RTAQQCXQSZGOHL-UHFFFAOYSA-N 0.000 claims description 6
- 238000001035 drying Methods 0.000 claims description 6
- 239000008367 deionised water Substances 0.000 claims description 5
- 229910021641 deionized water Inorganic materials 0.000 claims description 5
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 claims description 4
- 238000010009 beating Methods 0.000 claims description 4
- 229910052802 copper Inorganic materials 0.000 claims description 4
- 239000010949 copper Substances 0.000 claims description 4
- 239000012528 membrane Substances 0.000 claims description 4
- 229910052759 nickel Inorganic materials 0.000 claims description 4
- 238000005507 spraying Methods 0.000 claims description 4
- 229920000049 Carbon (fiber) Polymers 0.000 claims description 3
- 239000004917 carbon fiber Substances 0.000 claims description 3
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 claims description 3
- 239000002253 acid Substances 0.000 claims description 2
- 239000002131 composite material Substances 0.000 claims description 2
- 229910021385 hard carbon Inorganic materials 0.000 claims description 2
- 229920003063 hydroxymethyl cellulose Polymers 0.000 claims description 2
- 229940031574 hydroxymethyl cellulose Drugs 0.000 claims description 2
- 229910052748 manganese Inorganic materials 0.000 claims description 2
- 238000002156 mixing Methods 0.000 claims description 2
- 239000010450 olivine Substances 0.000 claims description 2
- 229910052609 olivine Inorganic materials 0.000 claims description 2
- 229910021384 soft carbon Inorganic materials 0.000 claims description 2
- 229910052596 spinel Inorganic materials 0.000 claims description 2
- 239000011029 spinel Substances 0.000 claims description 2
- 239000000126 substance Substances 0.000 claims description 2
- 239000003795 chemical substances by application Substances 0.000 claims 2
- 150000002148 esters Chemical class 0.000 claims 2
- 239000010413 mother solution Substances 0.000 claims 2
- ODIGIKRIUKFKHP-UHFFFAOYSA-N (n-propan-2-yloxycarbonylanilino) acetate Chemical compound CC(C)OC(=O)N(OC(C)=O)C1=CC=CC=C1 ODIGIKRIUKFKHP-UHFFFAOYSA-N 0.000 claims 1
- 229910001357 Li2MPO4F Inorganic materials 0.000 claims 1
- 229910032387 LiCoO2 Inorganic materials 0.000 claims 1
- 229910001305 LiMPO4 Inorganic materials 0.000 claims 1
- 229910015645 LiMn Inorganic materials 0.000 claims 1
- 229910013124 LiNiVO4 Inorganic materials 0.000 claims 1
- MTAZNLWOLGHBHU-UHFFFAOYSA-N butadiene-styrene rubber Chemical compound C=CC=C.C=CC1=CC=CC=C1 MTAZNLWOLGHBHU-UHFFFAOYSA-N 0.000 claims 1
- 239000002134 carbon nanofiber Substances 0.000 claims 1
- 210000005056 cell body Anatomy 0.000 claims 1
- 230000005611 electricity Effects 0.000 claims 1
- 239000003792 electrolyte Substances 0.000 abstract description 11
- 239000007773 negative electrode material Substances 0.000 abstract description 11
- 238000007086 side reaction Methods 0.000 abstract description 11
- 238000000354 decomposition reaction Methods 0.000 abstract description 8
- 239000011267 electrode slurry Substances 0.000 abstract description 5
- 239000007774 positive electrode material Substances 0.000 abstract description 3
- 238000002407 reforming Methods 0.000 abstract 1
- 230000000052 comparative effect Effects 0.000 description 21
- 238000000034 method Methods 0.000 description 13
- 239000000654 additive Substances 0.000 description 7
- 229910021382 natural graphite Inorganic materials 0.000 description 6
- 230000015572 biosynthetic process Effects 0.000 description 5
- 239000010406 cathode material Substances 0.000 description 5
- 229910012851 LiCoO 2 Inorganic materials 0.000 description 4
- 239000003575 carbonaceous material Substances 0.000 description 4
- 229910052744 lithium Inorganic materials 0.000 description 4
- 239000012452 mother liquor Substances 0.000 description 4
- 238000007873 sieving Methods 0.000 description 4
- WHXSMMKQMYFTQS-UHFFFAOYSA-N Lithium Chemical compound [Li] WHXSMMKQMYFTQS-UHFFFAOYSA-N 0.000 description 3
- 229910019142 PO4 Inorganic materials 0.000 description 3
- 230000000996 additive effect Effects 0.000 description 3
- 239000010405 anode material Substances 0.000 description 3
- 230000007423 decrease Effects 0.000 description 3
- 239000007770 graphite material Substances 0.000 description 3
- 239000010452 phosphate Substances 0.000 description 3
- NBIIXXVUZAFLBC-UHFFFAOYSA-K phosphate Chemical compound [O-]P([O-])([O-])=O NBIIXXVUZAFLBC-UHFFFAOYSA-K 0.000 description 3
- 238000007761 roller coating Methods 0.000 description 3
- 229910011281 LiCoPO 4 Inorganic materials 0.000 description 2
- 229910015643 LiMn 2 O 4 Inorganic materials 0.000 description 2
- 239000011889 copper foil Substances 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 238000011056 performance test Methods 0.000 description 2
- 229920008712 Copo Polymers 0.000 description 1
- 239000002000 Electrolyte additive Substances 0.000 description 1
- 229910010707 LiFePO 4 Inorganic materials 0.000 description 1
- 229910013275 LiMPO Inorganic materials 0.000 description 1
- BPQQTUXANYXVAA-UHFFFAOYSA-N Orthosilicate Chemical compound [O-][Si]([O-])([O-])[O-] BPQQTUXANYXVAA-UHFFFAOYSA-N 0.000 description 1
- 239000007864 aqueous solution Substances 0.000 description 1
- 229910021383 artificial graphite Inorganic materials 0.000 description 1
- 238000013473 artificial intelligence Methods 0.000 description 1
- 230000005540 biological transmission Effects 0.000 description 1
- OJIJEKBXJYRIBZ-UHFFFAOYSA-N cadmium nickel Chemical compound [Ni].[Cd] OJIJEKBXJYRIBZ-UHFFFAOYSA-N 0.000 description 1
- 239000002041 carbon nanotube Substances 0.000 description 1
- 229910021393 carbon nanotube Inorganic materials 0.000 description 1
- 230000003197 catalytic effect Effects 0.000 description 1
- 239000003245 coal Substances 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 239000006185 dispersion Substances 0.000 description 1
- 238000000840 electrochemical analysis Methods 0.000 description 1
- 239000008151 electrolyte solution Substances 0.000 description 1
- 238000004146 energy storage Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 238000005562 fading Methods 0.000 description 1
- 239000004519 grease Substances 0.000 description 1
- 238000011065 in-situ storage Methods 0.000 description 1
- 238000009776 industrial production Methods 0.000 description 1
- 239000004615 ingredient Substances 0.000 description 1
- 230000037427 ion transport Effects 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 230000014759 maintenance of location Effects 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 229910052987 metal hydride Inorganic materials 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 150000007524 organic acids Chemical class 0.000 description 1
- 239000005486 organic electrolyte Substances 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 230000010287 polarization Effects 0.000 description 1
- 239000007784 solid electrolyte Substances 0.000 description 1
- 229920003048 styrene butadiene rubber Polymers 0.000 description 1
Classifications
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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
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M10/00—Secondary cells; Manufacture thereof
- H01M10/05—Accumulators with non-aqueous electrolyte
- H01M10/052—Li-accumulators
- H01M10/0525—Rocking-chair batteries, i.e. batteries with lithium insertion or intercalation in both electrodes; Lithium-ion batteries
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M4/00—Electrodes
- H01M4/02—Electrodes composed of, or comprising, active material
- H01M4/13—Electrodes for accumulators with non-aqueous electrolyte, e.g. for lithium-accumulators; Processes of manufacture thereof
- H01M4/139—Processes of manufacture
- H01M4/1393—Processes of manufacture of electrodes based on carbonaceous material, e.g. graphite-intercalation compounds or CFx
-
- 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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- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Manufacturing & Machinery (AREA)
- Materials Engineering (AREA)
- Inorganic Chemistry (AREA)
- Battery Electrode And Active Subsutance (AREA)
- Secondary Cells (AREA)
Abstract
本发明公开了一种高电压锂离子电池负极极片的制备方法,是在传统的锂离子电池的负极浆料中加入有机酸脂,人为地在负极表面形成初态的SEI膜,当电池活化时直接参与到形成SEI膜的反应中,修饰电解液和负极材料的界面构造,重整SEI膜组分以提高其SEI膜稳定性和锂离子传输性,达到阻止高电压下电解液在负极表面持续不断的分解等副反应产生。该电池负极极片可以很好的应用到高电压锂离子电池中,提高高电压下全电池的循环性能,解决新型高电压正极材料缺乏兼容性良好的石墨负极材料问题,更重要的是突破高电压下高能量密度锂离子电池难以产业化发展的瓶颈,使得从提高电压角度来提升目前锂离子电池的能量密度成为现实。The invention discloses a preparation method of a negative electrode sheet of a high-voltage lithium-ion battery, which is to add an organic acid ester to the negative electrode slurry of a traditional lithium-ion battery to artificially form an initial SEI film on the surface of the negative electrode. When the battery is activated When directly participating in the reaction of forming the SEI film, modifying the interface structure of the electrolyte and the negative electrode material, reforming the components of the SEI film to improve the stability of the SEI film and the transport of lithium ions, to prevent the electrolyte from forming on the surface of the negative electrode under high voltage. Side reactions such as continuous decomposition occur. The negative electrode sheet of the battery can be well applied to high-voltage lithium-ion batteries, improve the cycle performance of the full battery under high voltage, solve the problem of lack of compatible graphite negative electrode materials for new high-voltage positive electrode materials, and more importantly, break through high-voltage lithium-ion batteries. The bottleneck of high energy density lithium-ion batteries under voltage is difficult to industrialize and develop, making it a reality to increase the energy density of current lithium-ion batteries from the perspective of increasing voltage.
Description
技术领域technical field
本发明涉及锂离子电池,具体是一种高电压锂离子电池负极极片的制备方法。The invention relates to a lithium-ion battery, in particular to a method for preparing a negative pole piece of a high-voltage lithium-ion battery.
背景技术Background technique
自从1990年Sony公司制造出第一代商业锂离子电池,其就在现有市场上占据很大份额,且发展势头迅猛增长,特别是近些年由于人们对石油、煤等不可再生能源的过度开发利用加速了化石资源枯竭的速度,以及由此带来严峻的全球环境问题,人们不得不大力发展像电能一样的可再生能源,其中电能研究最多的是如何进行有效的储存和合理的利用。比起传统的二次电池(铅酸,镍镉,镍氢电池等),锂离子电池具有更高的能量密度和工作电压,具有低污染和更长的使用寿命,已经占据越来越多的市场,是高效的储能元件以及电能释放系统。然而,相对于现代化的发展和行业需求,比如人工智能,移动电话、摄像机、笔记本、手机等便携式电子设备,其较低的能量密度大大阻碍了其发展空间和应用范围,特别是电动汽车的发展更加迫切需要高能量密度的锂离子电池。锂离子的能量密度由工作电压和材料的容量决定,提高其工作电压是提高电池能量密度的一个简单可行方法。比如,现有商用 LiCoO2的充电截止电压为4.2V,对应的比容量为140 mAh g-1。提高其充电截止电压至4.5V 时可以获得约 190 mAh g-1的比容量,显著提高了其能量密度。然而,高电压下对应的电池副反应加剧,电解液分解,其高电压下全电池很难做到实际商品,服务社会。同样,以LiNi0.5Mn1.5O4(LNMO)为代表的尖晶石结构高电压正极材料,存在着4.7V(Vs Li+/Li)高电压充放电平台,比容量146.7 mAh g-1,实际能量密度可以达到甚至超过220wh/kg,而现阶段单体电池能量密度仅为110~150wh·kg-1,而且LNMO正极材料制备成本低廉方法简单,具有优异的大电流充放电性能且安全性高等优点。然而遗憾的是,LNMO/石墨全电池基于现有技术,其电化学性能还未达到实际应用水平,特别是全电池的比容量随着循环进行出现大幅度的衰减,大大制约了其高电压高能量密度锂离子电池的发展。除外,目前还有很多种高电压正极材料,比如磷酸盐系的LiCoPO4、LiMnPO4等也存在着同样的问题,因此实现高电压下高能量密度的商业锂离子电池体系其关键就在于发展与之相匹配的负极材料和电解液。Since Sony manufactured the first generation of commercial lithium-ion batteries in 1990, it has occupied a large share in the existing market, and its development momentum has grown rapidly, especially in recent years due to people's excessive use of non-renewable energy sources such as oil and coal. Exploitation and utilization have accelerated the depletion of fossil resources and brought severe global environmental problems. People have to vigorously develop renewable energy like electric energy. Among them, how to effectively store and rationally use electric energy is the most researched. Compared with traditional secondary batteries (lead-acid, nickel-cadmium, nickel-metal hydride batteries, etc.), lithium-ion batteries have higher energy density and operating voltage, low pollution and longer service life, and have occupied more and more The market is high-efficiency energy storage components and electric energy release systems. However, compared with modern development and industry needs, such as artificial intelligence, portable electronic devices such as mobile phones, cameras, notebooks, and mobile phones, their low energy density greatly hinders their development space and application range, especially the development of electric vehicles. Li-ion batteries with high energy density are more urgently needed. The energy density of lithium ions is determined by the working voltage and the capacity of the material, and increasing its working voltage is a simple and feasible way to increase the energy density of batteries. For example, the charging cut-off voltage of the existing commercial LiCoO 2 is 4.2V, and the corresponding specific capacity is 140 mAh g -1 . A specific capacity of about 190 mAh g -1 can be obtained when the charge cut-off voltage is increased to 4.5 V, which significantly improves its energy density. However, the corresponding side reactions of the battery under high voltage are intensified, and the electrolyte solution is decomposed. It is difficult for the full battery under high voltage to be a practical commodity and serve the society. Similarly, the spinel-structured high-voltage cathode material represented by LiNi 0.5 Mn 1.5 O 4 (LNMO) has a 4.7V (Vs Li + /Li) high-voltage charge-discharge platform with a specific capacity of 146.7 mAh g -1 . The energy density can reach or even exceed 220wh/kg, while the energy density of a single battery at this stage is only 110~150wh·kg -1 , and the preparation cost of LNMO cathode material is low and the method is simple, it has excellent high-current charge and discharge performance and high safety, etc. advantage. Unfortunately, based on the existing technology, the electrochemical performance of LNMO/graphite full battery has not yet reached the level of practical application. In particular, the specific capacity of the full battery decreases significantly with the cycle, which greatly restricts its high voltage and high performance. Energy Density Li-ion Battery Development. In addition, there are many kinds of high-voltage cathode materials, such as phosphate-based LiCoPO 4 , LiMnPO 4 , etc., which also have the same problem. Therefore, the key to realizing a commercial lithium-ion battery system with high energy density at high voltage lies in the development and The matching negative electrode material and electrolyte.
为了改善高电压下锂离子全电池的电化学性能,探索高电压电解液添加剂,优化电解液配方也是一重要途径,但是添加剂本身也会对电池的电阻和容量的发挥产生影响。本发明的出发点是从负极方面进行探索,提出直接从电池反应最剧烈的固体电解质膜(SEI)着手,针对高电压条件下设法在SEI膜上进行修饰和改性;另外,经统计基于石墨材料的资源丰富,制备简单和成本廉价等,现在锂离子电池实际商业应用中,石墨碳材料仍然占锂离子电池的负极材料的主导地位。因此,本发明的高电压锂电池用负极材料也是在石墨材料上进行的,具有直接的商用价值,可直接投入生产。In order to improve the electrochemical performance of lithium-ion full batteries under high voltage, it is also an important way to explore high-voltage electrolyte additives and optimize the electrolyte formula, but the additives themselves will also affect the resistance and capacity of the battery. The starting point of the present invention is to explore from the aspect of the negative electrode, and proposes to start directly from the solid electrolyte membrane (SEI) with the most violent battery reaction, and try to modify and modify the SEI membrane under high voltage conditions; The resource is abundant, the preparation is simple and the cost is cheap, and now in the actual commercial application of lithium-ion batteries, graphitic carbon materials still occupy the dominant position of the negative electrode materials of lithium-ion batteries. Therefore, the negative electrode material for the high-voltage lithium battery of the present invention is also carried out on the graphite material, has direct commercial value, and can be directly put into production.
发明内容Contents of the invention
为解决目前高电压锂离子全电池循环性能差,容量衰减严重问题 ,本发明提供一种高电压锂离子电池负极极片的制备方法,从锂离子电池负极方面来提升高电压锂离子全电池的循环性能,从而实现其商用价值。In order to solve the problems of poor cycle performance and serious capacity fading of current high-voltage lithium-ion full batteries, the present invention provides a method for preparing negative pole pieces of high-voltage lithium-ion batteries, which improves the performance of high-voltage lithium-ion full batteries from the aspect of negative electrodes of lithium-ion batteries. Cycle performance, so as to realize its commercial value.
实现本发明目的的技术方案是:The technical scheme that realizes the object of the present invention is:
一种高电压锂离子电池负极极片的制备方法,包括以下步骤:A method for preparing a high-voltage lithium-ion battery negative pole piece, comprising the following steps:
(1)先将一定量的粘结剂溶于去离子水中,制成均一水性粘性浆料母液;(1) First dissolve a certain amount of binder in deionized water to make a uniform water-based viscous slurry mother liquor;
(2)然后将导电剂和负极材料加入浆料母液中,待均匀分散后,加入有机酸酯混合打浆,制成负极浆料;(2) Then add the conductive agent and the negative electrode material into the slurry mother liquor, and after being uniformly dispersed, add the organic acid ester for mixing and beating to make the negative electrode slurry;
(3)将步骤(2)制得的负极浆料置于真空状态-0.08MPa ~ -0.1MPa,保持真空时间0.5h~20h,真空温度控制在20~50℃,保证有机酸脂分散到负极材料表面;(3) Put the negative electrode slurry prepared in step (2) in a vacuum state of -0.08MPa ~ -0.1MPa, keep the vacuum for 0.5h~20h, and control the vacuum temperature at 20~50°C to ensure that the organic acid grease is dispersed to the negative electrode material surface;
(4)将步骤(3)浆料过筛得到细度为15 ~ 45um,采用辊涂或者喷涂方式涂覆在负极导电铜箔上,烘干后即得到表面具有初态SEI膜结构的负极极片,与正极极片组装成电池体系,最后采用恒流0.02C~0.5C进行化成得到稳定SEI膜;(4) Sieve the slurry in step (3) to obtain a fineness of 15 ~ 45um, and coat it on the negative electrode conductive copper foil by roller coating or spraying, and obtain the negative electrode with the initial SEI film structure on the surface after drying sheet, assembled with the positive electrode sheet to form a battery system, and finally use a constant current of 0.02C~0.5C for chemical formation to obtain a stable SEI film;
所述负极的配料由负极材料、导电剂、粘结剂和有机酸酯制成,其比例分别为∶The batching of described negative pole is made by negative pole material, conductive agent, binding agent and organic acid ester, and its ratio is respectively:
负极材料 75~90%Anode material 75~90%
粘结剂 1~5%Binder 1~5%
导电剂 2~5%Conductive agent 2~5%
有机酸酯 1~20%Organic acid ester 1~20%
配料完成后溶于去离子水中得到负极浆料,浆料固含量为25~55%,粘度为1000~5000mPa.s。After the batching is completed, it is dissolved in deionized water to obtain negative electrode slurry. The solid content of the slurry is 25-55%, and the viscosity is 1000-5000mPa.s.
上述制备方法中,步骤(2)所述打浆温度为20~50℃,湿度为5~20%。In the above preparation method, the beating temperature in step (2) is 20-50° C., and the humidity is 5-20%.
步骤(4)所述辊涂方式的涂布速度为3~10m/min,烘烤温度为70~110℃;喷涂方式的涂布速度为5~13m/min,烘箱温度为70~110℃;制得负极极片的厚度为0.02~0.2mm。In step (4), the coating speed of the roller coating method is 3-10m/min, and the baking temperature is 70-110°C; the coating speed of the spray coating method is 5-13m/min, and the oven temperature is 70-110°C; The thickness of the prepared negative electrode sheet is 0.02-0.2mm.
所述负极材料为天然石墨、人造石墨、复合石墨、软碳、硬碳中的至少一种。The negative electrode material is at least one of natural graphite, artificial graphite, composite graphite, soft carbon, and hard carbon.
所述导电剂为导电石墨(包括 SP、KS-6、碳纳米管);碳纤维(CF)中的至少一种。The conductive agent is at least one of conductive graphite (including SP, KS-6, carbon nanotubes); carbon fiber (CF).
所述粘结剂为水性羟甲基纤维素(CMC)、丁苯橡胶(SBR)、粘结剂LA133中的至少一种。The binder is at least one of water-based hydroxymethylcellulose (CMC), styrene-butadiene rubber (SBR), and binder LA133.
所述有机酸酯为有机钛酸酯、有机硅酸酯、有机磷酸酯中的至少一种The organic acid ester is at least one of organic titanate, organic silicate, and organic phosphate
采用本发明方法制备的高电压锂离子电池负极极片可以与以下高电压型的正极材料相匹配制备商业全电池:尖晶石结构的LiMn2O4,LiNi0.5Mn1.5O4,LizNixMn1-xO2;LizCo1-(x+y)NixMnyO2(其中,x、y、x+y<1、z≥1);橄榄石结构LiMPO4或Li2MPO4F(M=Co,Mn,Ni);LiNiVO4,LiMeSO4F (Me=Co,Ni,Cu),高电压层状LiCoO2(充电截止电压≥4.3V)。The high-voltage lithium-ion battery negative electrode sheet prepared by the method of the present invention can be matched with the following high-voltage positive electrode materials to prepare commercial full batteries: LiMn 2 O 4 with spinel structure, LiNi 0.5 Mn 1.5 O 4 , Li z Ni x Mn 1-x O 2 ; Li z Co 1-(x+y) Ni x Mn y O 2 (where x, y, x+y<1, z≥1); olivine structure LiMPO 4 or Li 2 MPO 4 F (M=Co, Mn, Ni); LiNiVO 4 , LiMeSO 4 F (Me=Co, Ni, Cu), high-voltage layered LiCoO 2 (charge cut-off voltage ≥ 4.3V).
本发明方法是在负极表面采用有机酸酯进行改性,在充放电过程中有机酸酯参与到SEI膜的形成,修饰电解液和负极材料的界面结构,重整SEI膜组分以提高其SEI膜稳定性和锂离子传输性,达到阻止高电压下电解液在负极表面持续不断的分解等副反应产生。The method of the present invention is to modify the surface of the negative electrode with an organic acid ester, and the organic acid ester participates in the formation of the SEI film during the charge and discharge process, modifies the interface structure between the electrolyte and the negative electrode material, and reforms the components of the SEI film to improve its SEI. Membrane stability and lithium ion transport can prevent side reactions such as continuous decomposition of the electrolyte on the surface of the negative electrode under high voltage.
本发明的负极极片主要用作于工作电压高于4.3V的锂离子电池,传统的锂离子电池电压一般在4.0V以下(LiCoO2/碳材料,LiFePO4/碳材料,LiMn2O4/碳材料等等),比如中国专利CN201210221178制备的负极极片也是应用于低电压锂电池中,此电压下对有机电解液氧化分解有限。从能量密度角度来说,提升锂电池的电压必然带来能量密度的提升,电压越高能量密度越高,但是当电压高于4.3V会引起电解液的快速分解,分解产物附着在负极表面形成较厚的SEI膜阻碍锂离子的传输通道导致锂离子电池循环寿命减少和容量的快速衰减,当充电电压到4.8V时电池基本无循环容量。The negative pole piece of the present invention is mainly used as a lithium-ion battery with a working voltage higher than 4.3V, and the voltage of a traditional lithium-ion battery is generally below 4.0V (LiCoO 2 /carbon material, LiFePO 4 /carbon material, LiMn 2 O 4 / Carbon materials, etc.), for example, the negative pole piece prepared by Chinese patent CN201210221178 is also used in low-voltage lithium batteries, and the oxidation decomposition of organic electrolyte is limited under this voltage. From the perspective of energy density, increasing the voltage of lithium batteries will inevitably lead to an increase in energy density. The higher the voltage, the higher the energy density. However, when the voltage is higher than 4.3V, the electrolyte will decompose rapidly, and the decomposition products will adhere to the surface of the negative electrode to form The thicker SEI film hinders the transmission channel of lithium ions, which leads to the reduction of cycle life and rapid decline of capacity of lithium ion batteries. When the charging voltage reaches 4.8V, the battery basically has no cycle capacity.
本发明高电压锂离子电池负极极片的制备方法与现在技术相比:Compared with the present technology, the preparation method of the negative pole piece of the high-voltage lithium-ion battery of the present invention:
(1)本发明是在传统的锂离子电池用负极材料基础上面发展起来,用作高电压锂离子电池负极材料,制备方法简单可行,成本低易于实现,完全可以应用到规模化、大批量、工业化生产。(1) The present invention is developed on the basis of traditional negative electrode materials for lithium-ion batteries. It is used as negative electrode materials for high-voltage lithium-ion batteries. The preparation method is simple and feasible, and the cost is low and easy to implement. Industrial production.
(2)本发明所制得的电池负极极片可以很好的应用到高电压锂离子电池中,应用到现有的LiNi0.5Mn1.5O4,高电压LiCoO2,Li3V2(PO4)3,LiCoPO4,Li2CoPO4F,Li2FeSiO4,Li2FePO4F等新型高电压正极材料,提高高电压下全电池的循环性能,解决新型高电压正极材料缺乏兼容性良好的石墨负极材料问题,更重要的是突破高电压下高能量密度锂离子电池难以产业化发展的瓶颈,使得从提高电压角度来提升目前锂离子电池的能量密度成为现实。(2) The battery negative pole piece prepared by the present invention can be well applied to high-voltage lithium-ion batteries, such as the existing LiNi 0.5 Mn 1.5 O 4 , high-voltage LiCoO 2 , Li 3 V 2 (PO 4 ) 3 , LiCoPO 4 , Li 2 CoPO 4 F, Li 2 FeSiO 4 , Li 2 FePO 4 F and other new high-voltage cathode materials can improve the cycle performance of full batteries under high voltage and solve the lack of compatibility of new high-voltage cathode materials. The issue of graphite anode materials, more importantly, is to break through the bottleneck of high-energy-density lithium-ion batteries under high voltage, which is difficult to industrialize and develop, making it a reality to increase the energy density of current lithium-ion batteries from the perspective of increasing voltage.
(3)本发明制备方法对比了加入无机添加剂(Li2CO3)制备的负极极片,本发明制备的负极极片能能更好地适用于高电压下的电池体系。相对于低电压下的反应,其高电压下对于锂离子电池负极材料提出了更严峻的挑战,不仅要保证首次效率和比容量大等电化学性能优良,而且还要保证其高电压下对电解液的异相催化作用最低,实验表明相对于无机物负极添加剂,有机酸酯更好地在充放电过程中原位参与到SEI膜的形成中,固化和修饰SEI膜构造阻止电解液的进一步分解。(3) The preparation method of the present invention is compared with the negative electrode sheet prepared by adding inorganic additives (Li 2 CO 3 ), and the negative electrode sheet prepared by the present invention can be better applied to the battery system under high voltage. Compared with the reaction at low voltage, its high voltage poses a more severe challenge to the anode material of lithium-ion batteries, not only to ensure excellent electrochemical performance such as first-time efficiency and large specific capacity, but also to ensure its electrolytic performance at high voltage. The heterogeneous catalytic effect of liquid is the lowest. Compared with inorganic negative electrode additives, organic acid esters can better participate in the formation of SEI film in situ during charge and discharge, and solidify and modify the structure of SEI film to prevent further decomposition of electrolyte.
附图说明Description of drawings
图1为对比例1、2和本发明实施例1、2、3制备的电池负极极片匹配4.7V高电压正极LNMO组装成的全电池首次充放电对比曲线;Fig. 1 is the comparison curve of the first charge and discharge of the full battery assembled by the battery negative pole pieces prepared in Comparative Examples 1, 2 and Examples 1, 2, 3 of the present invention and matched with 4.7V high-voltage positive LNMO;
图2为对比例1、2和本发明实施例1、2、3制备的电池负极极片匹配4.7V高电压正极LNMO组装成的全电池循环性能对比曲线Figure 2 is a comparison curve of the cycle performance of the full battery assembled in Comparative Examples 1, 2 and Examples 1, 2, and 3 of the present invention.
图3为对比例1和本发明实施例1、2、3制备的电池负极极片匹配4.7V高电压正极LNMO组装成的全电池不同循环次数的放电曲线图,分别是第1, 5,10,20,50次的放电曲线图。Fig. 3 is the discharge curve diagram of different cycle times of the full battery assembled by the battery negative electrode sheet matched with the 4.7V high-voltage positive electrode LNMO prepared by Comparative Example 1 and Examples 1, 2, and 3 of the present invention, respectively 1st, 5th, and 10th. , 20, 50 discharge curves.
具体实施方式detailed description
下面结合具体实施例和附图对本发明内容作进一步详细说明,但本发明并不局限于以下这些实施例。The content of the present invention will be described in further detail below in conjunction with specific embodiments and drawings, but the present invention is not limited to the following embodiments.
对比例1Comparative example 1
采用普通石墨材料制备的常规负极极片,包括如下步骤:The conventional negative pole sheet prepared by common graphite material comprises the following steps:
(1)将3%的CMC溶于去离子水中,制成粘性浆料母液;(1) Dissolve 3% CMC in deionized water to make viscous slurry mother liquor;
(2)待浆料母液充分混合后加入2%的导电剂混合制备导电浆料;(2) After the slurry mother liquor is fully mixed, add 2% conductive agent and mix to prepare conductive slurry;
(3)待均匀分散后,加入90%的天然石墨材料,控制打浆温度25℃,湿度10%;(3) After uniform dispersion, add 90% natural graphite material, control the beating temperature to 25°C, and the humidity to 10%;
(4)待物料混合均匀后,调整浆料粘度为4000mPa.s,固含量为48%;(4) After the materials are mixed evenly, adjust the viscosity of the slurry to 4000mPa.s and the solid content to 48%;
(5)把浆料置于真空状态-0.08MPa,保持此真空状态5h,真空温度25℃;(5) Put the slurry in a vacuum state of -0.08MPa, keep the vacuum state for 5 hours, and the vacuum temperature is 25°C;
(6)将打制好的浆料过筛后细度为30um后,通过辊涂的方式涂覆在负极导电铜箔或者铜网上,涂布速度为5m/min,烘箱烘烤温度呈阶梯分布其中最高温度95℃,两边最低温度85℃,烘干后得到负极厚度为0.168mm,负极单面的面密度104g/m2。(6) After sieving the prepared slurry to a fineness of 30um, it is coated on the negative electrode conductive copper foil or copper grid by roller coating, the coating speed is 5m/min, and the oven baking temperature is distributed in steps Among them, the highest temperature is 95°C, and the lowest temperature on both sides is 85°C. After drying, the thickness of the negative electrode is 0.168mm, and the surface density of one side of the negative electrode is 104g/m 2 .
对比例2Comparative example 2
采用常规负极添加剂Li2CO3制备的锂离子电池石墨负极极片,包括如下步骤:Adopt conventional negative electrode additive Li 2 CO 3 Lithium-ion battery graphite negative pole sheet prepared, comprises the following steps:
步骤(1)-(2)与对比例1相同,步骤(3)在加入天然石墨后加入含量为1wt%无机Li2CO3的水溶液作为一种负极添加剂;调整浆料粘度4000mPa.s,固含量为48%;如对比例1继续进行真空操作,过筛和涂覆,烘干得到含有无机Li2CO3添加剂的负极极片,负极片厚度和单面面密度与对比例1相同。Steps (1)-(2) are the same as Comparative Example 1, step (3) after adding natural graphite, add an aqueous solution with a content of 1wt% inorganic Li 2 CO 3 as a negative electrode additive; adjust the viscosity of the slurry to 4000mPa.s, solid The content is 48%; as in Comparative Example 1, the vacuum operation is continued, sieved and coated, and dried to obtain a negative electrode sheet containing inorganic Li 2 CO 3 additives. The thickness and density of the negative electrode sheet are the same as in Comparative Example 1.
无机Li2CO3作为一种SEI膜的主要组成成分之一,可以有效的减少电解液在形成SEI膜的分解程度,在电池化成工序阶段提高锂离子电池的首次效率,对提高电池的循环寿命有着重要的作用,也是现在电池体系中经常用作负极浆料配料中常见的添加剂。As one of the main components of the SEI film, inorganic Li 2 CO 3 can effectively reduce the decomposition degree of the electrolyte in the formation of the SEI film, improve the first-time efficiency of the lithium-ion battery during the battery formation process, and improve the cycle life of the battery. It plays an important role, and it is also commonly used as a common additive in negative electrode slurry ingredients in battery systems.
实施例1Example 1
采用本发明方法制备高电压锂离子电池负极极片,包括如下步骤:Adopting the method of the present invention to prepare the negative pole piece of high-voltage lithium-ion battery comprises the following steps:
步骤(1)-(2)与对比例1相同,步骤(3)在加入天然石墨后加入质量分数10%的有机钛酸酯;调整浆料粘度4000mPa.s,固含量为48%;如对比例1继续进行真空操作,过筛和涂覆,烘干过后即得到表面具有初态有机钛酸酯SEI膜结构的负极极片,负极极片的厚度以及单面面密度与对比例1相同。待电池化成后,有机钛酸酯参与并修饰SEI膜,达到稳定SEI膜的作用,更加耐高电压条件。Steps (1)-(2) are the same as Comparative Example 1, step (3) adds organic titanate with a mass fraction of 10% after adding natural graphite; adjust the viscosity of the slurry to 4000mPa.s, and the solid content is 48%; Proportion 1 continued vacuum operation, sieving and coating, and after drying, a negative electrode sheet with an initial state organic titanate SEI film structure on the surface was obtained. The thickness and single-side surface density of the negative electrode sheet were the same as those of Comparative Example 1. After the battery is formed, organic titanate participates in and modifies the SEI film to stabilize the SEI film and make it more resistant to high voltage conditions.
实施例2Example 2
采用本发明制备方法制备高电压锂离子电池负极极片,包括如下步骤:Adopting the preparation method of the present invention to prepare the negative pole piece of high-voltage lithium-ion battery comprises the following steps:
步骤(1)-(2)与对比例1相同,步骤(3)在加入天然石墨后加入质量分数15%的有机钛酸酯;调整浆料粘度4000mPa.s,固含量为48%;如对比例1继续进行真空操作,过筛和涂覆,烘干过后即得到表面具有初态SEI膜结构的负极极片。Steps (1)-(2) are the same as Comparative Example 1, step (3) adds organic titanate with a mass fraction of 15% after adding natural graphite; adjust the slurry viscosity to 4000mPa.s, and the solid content is 48%; Proportion 1 continues vacuum operation, sieving and coating, and after drying, a negative electrode sheet with an initial SEI film structure on the surface is obtained.
实施例3Example 3
采用本发明制备方法制备高电压锂离子电池负极极片,包括如下步骤:Adopting the preparation method of the present invention to prepare the negative pole piece of high-voltage lithium-ion battery comprises the following steps:
步骤(1)-(2)与对比例1相同,步骤(3)在加入天然石墨后加入质量分数10%的有机磷酸酯;调整浆料粘度4000mPa.s,固含量为48%;如对比例1继续进行真空操作,过筛和涂覆,烘干过后即得到表面具有初态SEI膜结构的负极极片。Steps (1)-(2) are the same as Comparative Example 1, and step (3) adds organic phosphate with a mass fraction of 10% after adding natural graphite; adjust the viscosity of the slurry to 4000mPa.s, and the solid content is 48%; as in the comparative example 1 Continue vacuum operation, sieving and coating, and after drying, a negative electrode sheet with an initial SEI film structure on the surface is obtained.
上述各实施例及对比例所制备的锂离子电池负极极片与高电压正极材料LNMO匹配组成的全电池性能测试参数,如表 1所示。The performance test parameters of the full battery composed of the lithium-ion battery negative pole piece prepared in the above examples and comparative examples and the high-voltage positive electrode material LNMO are shown in Table 1.
本表测试数据是基于LAND电化学测试系统,其测试条件:全电池循环性能测试电压范围3.4~4.8V,首次充放电先以0.5C循环两次,再以1C恒流充放电进行60次循环(其中1C=146.7mAh/g)。The test data in this table is based on the LAND electrochemical test system, and its test conditions: the full battery cycle performance test voltage range is 3.4~4.8V, the first charge and discharge cycle is performed twice at 0.5C, and then 60 cycles with 1C constant current charge and discharge (where 1C=146.7mAh/g).
表1Table 1
从表1数据可以看出,常规石墨负极极片组装的高电压全电池首次效率比本发明制备的高电压负极极片组装的全电池都普遍低,意味着以普通石墨作为电池负极其表面形成SEI膜不稳定且不能有效阻止电解液的分解,其副反应大大高出本发明制备的负极极片。同样,全电池60次循环后容量保持率数据也证实了本发明制备的负极极片在高电压下条件下性能优良,随着循环的进行容量衰减趋势缓慢,提升了高电压锂离子电池的实际使用寿命。另外,常规石墨负极极片组装的全电池第2次和第60次的循环放电平均电压明显低于本发明的实施例1,2,3制备的全电池,说明常规石墨负极极片较本发明的负极极片组成的全电池内部极化严重,发生的副反应多。As can be seen from the data in Table 1, the initial efficiency of the high-voltage full battery assembled by the conventional graphite negative pole piece is generally lower than that of the full battery assembled by the high-voltage negative pole piece prepared by the present invention, which means that ordinary graphite is used as the battery negative pole surface to form The SEI film is unstable and cannot effectively prevent the decomposition of the electrolyte, and its side reactions are much higher than that of the negative electrode sheet prepared by the present invention. Similarly, the capacity retention data of the full battery after 60 cycles has also confirmed that the negative electrode sheet prepared by the present invention has excellent performance under high voltage conditions, and the capacity decay trend is slow as the cycle progresses, which improves the actual performance of high-voltage lithium-ion batteries. service life. In addition, the 2nd and 60th cycle discharge average voltages of the full battery assembled by the conventional graphite negative pole piece are significantly lower than the full battery prepared in Examples 1, 2, and 3 of the present invention, indicating that the conventional graphite negative pole piece is more advanced than the present invention. The internal polarization of the full battery composed of negative pole pieces is serious, and many side reactions occur.
参照图1,对比例1、2和本发明实施例1、2、3制备的电池负极极片匹配4.7V高电压正极LNMO组装成的全电池首次充放电对比曲线,从图中可以看出:本发明实施例1、2、3比普通石墨制备出的负极极片组装的LNMO全电池首次放电平台维持在4.6V左右且平台较平坦,普通石墨对比例的放电平台不明显、倾斜且放电电压平台明显低于4.6V。结合首次充电平台可以根据充电和放电平台之间的电位差可以判断出,对比例1的电位差大大大于本发明的实施例1、2、3,说明普通石墨得到的负极极片用作高电压电池中,电池极化严重,副反应较多。另外,副反应体现最明显是在首次形成SEI膜的过程中,其副反应程度直接影响着电池的首次效率,首次效率高,说明副反应小;首次效率低,意味着副反应剧烈。根据首次充放电数据以及表1可以明显看出普通石墨制备的负极极片对比例1组装成的全电池首次效率仅为59.82%明显低于本发明制备的负极极片,表明着本发明得到的负极极片可以在高电压下降低副反应的发生。值得一提的是,传统掺入Li2CO3得到的负极极片也具较高的首次效率,这说明Li2CO3的加入也抑制了首次形成SEI膜时对电解液的分解作用。Referring to Figure 1, the comparison curves of the first charge and discharge of the full battery assembled by the battery negative pole pieces prepared in Comparative Examples 1, 2 and Examples 1, 2, and 3 of the present invention matched with 4.7V high-voltage positive LNMO can be seen from the figure: The first discharge platform of the LNMO full battery assembled with the negative pole piece prepared by ordinary graphite in Examples 1, 2, and 3 of the present invention is maintained at about 4.6V and the platform is relatively flat. The discharge platform of the ordinary graphite comparative example is not obvious, inclined and the discharge voltage The platform is significantly lower than 4.6V. Combined with the first charging platform, it can be judged according to the potential difference between the charging and discharging platforms, the potential difference of Comparative Example 1 is much greater than that of Examples 1, 2, and 3 of the present invention, indicating that the negative pole piece obtained by ordinary graphite is used as a high voltage In the battery, the battery is severely polarized and has many side reactions. In addition, the side reaction is most obvious in the process of forming the SEI film for the first time. The degree of the side reaction directly affects the first efficiency of the battery. A high first efficiency means that the side reaction is small; a low first efficiency means that the side reaction is severe. According to the first charge and discharge data and Table 1, it can be clearly seen that the first efficiency of the full battery assembled into the negative pole piece prepared by ordinary graphite is only 59.82%, which is obviously lower than the negative pole piece prepared by the present invention, indicating that the present invention obtains The negative pole piece can reduce the occurrence of side reactions under high voltage. It is worth mentioning that the negative electrode sheet obtained by traditionally doping Li 2 CO 3 also has a higher initial efficiency, which shows that the addition of Li 2 CO 3 also inhibits the decomposition of the electrolyte when the SEI film is formed for the first time.
参照图2,对比例1、2和本发明实施例1、2、3制备的电池负极极片匹配4.7V高电压正极LNMO组装成的全电池循环性能对比曲线,从图中可以看出:普通石墨制得的负极极片用在高电压LNMO全电池中,随着循环的进行容量衰减严重,第50次循环后容量仅为初始容量的83.10%;而本发明实施例3随着循环的深入容量基本上没有衰减,第50次循环后容量为初始容量的97.51%,体现出高电压下稳定的循环寿命。另外,对比例2是传统掺入Li2CO3得到的负极极片根据全电池循环曲线可以看出虽然在初始的10次循环之内电池具有较高的比容量,但是10循环后比容量随着循环的进行容量快速衰减,说明通过传统加入Li2CO3制备的负极极片并不适合高电压体系的锂离子电池。Referring to Fig. 2, the cycle performance comparison curves of the full battery assembled by the negative pole piece of the battery prepared in Comparative Examples 1, 2 and Examples 1, 2, and 3 of the present invention matched with 4.7V high-voltage positive electrode LNMO can be seen from the figure: The negative electrode sheet made of graphite is used in a high-voltage LNMO full battery. As the cycle progresses, the capacity decays seriously. After the 50th cycle, the capacity is only 83.10% of the initial capacity; The capacity has basically no decay, and the capacity after the 50th cycle is 97.51% of the initial capacity, reflecting a stable cycle life under high voltage. In addition, Comparative Example 2 is a negative electrode sheet obtained by traditionally doping Li 2 CO 3 . According to the cycle curve of the full battery, it can be seen that although the battery has a high specific capacity within the initial 10 cycles, the specific capacity decreases with time after 10 cycles. The capacity decays rapidly as the cycle progresses, indicating that the negative electrode sheet prepared by traditionally adding Li 2 CO 3 is not suitable for high-voltage lithium-ion batteries.
参照图3,对比例1和本发明实施例1、2、3制备的电池负极极片匹配4.7V高电压正极LNMO组装成的全电池第1, 5,10,20,50次的放电曲线图,从图中可以明显看出不同次数下电压平台状态和容量的衰减程度,通过参照图3可以看出相比对比例1本发明的实施例1、2、3全电池放电平台一致性保持良好,同时容量保持一致性也非常好,说明采用本发明方法制备出的负极极片可以完全适用于高电压体系的锂离子电池体系且性能优良。Referring to Fig. 3, the discharge curves of the first, 5th, 10th, 20th and 50th discharge curves of the full battery assembled by the negative pole piece of the battery prepared in Comparative Example 1 and Examples 1, 2, and 3 of the present invention matched with the 4.7V high-voltage positive electrode LNMO , it can be clearly seen from the figure that the state of the voltage platform and the degree of capacity attenuation under different times can be seen by referring to Figure 3. Compared with Comparative Example 1, the consistency of the full battery discharge platform of Embodiments 1, 2, and 3 of the present invention remains good. , and the consistency of the capacity is also very good, indicating that the negative pole piece prepared by the method of the present invention can be completely applied to the lithium-ion battery system of the high-voltage system and has excellent performance.
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| CN113138221A (en) * | 2021-04-20 | 2021-07-20 | 合肥国轩高科动力能源有限公司 | Method for optimizing proportion representation SEI film impedance of conductive agent and binder |
| CN116364929A (en) * | 2023-03-30 | 2023-06-30 | 湖南金阳烯碳新材料股份有限公司 | A kind of negative electrode material and its preparation method and application |
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