CN102376940A - Lithium ion battery, cathode slurry and preparation method thereof - Google Patents
Lithium ion battery, cathode slurry and preparation method thereof Download PDFInfo
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- HBBGRARXTFLTSG-UHFFFAOYSA-N Lithium ion Chemical compound [Li+] HBBGRARXTFLTSG-UHFFFAOYSA-N 0.000 title claims abstract description 33
- 229910001416 lithium ion Inorganic materials 0.000 title claims abstract description 33
- 238000002360 preparation method Methods 0.000 title claims abstract description 30
- 239000006257 cathode slurry Substances 0.000 title 1
- 239000011267 electrode slurry Substances 0.000 claims abstract description 43
- 238000003756 stirring Methods 0.000 claims abstract description 24
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 23
- 239000006258 conductive agent Substances 0.000 claims abstract description 20
- 239000000314 lubricant Substances 0.000 claims abstract description 17
- 239000000203 mixture Substances 0.000 claims abstract description 17
- 239000002904 solvent Substances 0.000 claims abstract description 16
- 239000007773 negative electrode material Substances 0.000 claims abstract description 13
- 239000011883 electrode binding agent Substances 0.000 claims abstract description 12
- 239000000654 additive Substances 0.000 claims abstract description 11
- 230000000996 additive effect Effects 0.000 claims abstract description 11
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims abstract description 10
- 239000000463 material Substances 0.000 claims abstract description 10
- 238000002156 mixing Methods 0.000 claims abstract description 9
- 229920002134 Carboxymethyl cellulose Polymers 0.000 claims abstract description 8
- DPXJVFZANSGRMM-UHFFFAOYSA-N acetic acid;2,3,4,5,6-pentahydroxyhexanal;sodium Chemical compound [Na].CC(O)=O.OCC(O)C(O)C(O)C(O)C=O DPXJVFZANSGRMM-UHFFFAOYSA-N 0.000 claims abstract description 8
- 235000010948 carboxy methyl cellulose Nutrition 0.000 claims abstract description 8
- 239000001768 carboxy methyl cellulose Substances 0.000 claims abstract description 8
- 235000019812 sodium carboxymethyl cellulose Nutrition 0.000 claims abstract description 8
- 229920001027 sodium carboxymethylcellulose Polymers 0.000 claims abstract description 8
- 150000002576 ketones Chemical class 0.000 claims abstract description 7
- 125000003158 alcohol group Chemical group 0.000 claims abstract description 3
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 claims description 12
- 150000001875 compounds Chemical class 0.000 claims description 10
- 229920003048 styrene butadiene rubber Polymers 0.000 claims description 7
- CSCPPACGZOOCGX-UHFFFAOYSA-N Acetone Chemical compound CC(C)=O CSCPPACGZOOCGX-UHFFFAOYSA-N 0.000 claims description 6
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical group C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 claims description 2
- 239000000843 powder Substances 0.000 claims description 2
- SECXISVLQFMRJM-UHFFFAOYSA-N N-Methylpyrrolidone Chemical compound CN1CCCC1=O SECXISVLQFMRJM-UHFFFAOYSA-N 0.000 claims 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 abstract description 13
- 239000002002 slurry Substances 0.000 abstract description 12
- 229920001971 elastomer Polymers 0.000 abstract description 11
- 229910002804 graphite Inorganic materials 0.000 abstract description 11
- 239000010439 graphite Substances 0.000 abstract description 11
- 238000000034 method Methods 0.000 abstract description 11
- 239000005060 rubber Substances 0.000 abstract description 11
- 239000000126 substance Substances 0.000 abstract description 3
- 238000009736 wetting Methods 0.000 abstract description 3
- 239000000080 wetting agent Substances 0.000 abstract description 2
- 238000004519 manufacturing process Methods 0.000 description 8
- AEDAWHHRIHMZAR-UHFFFAOYSA-N [O-][N+](=O)CN1CCCC1=O Chemical compound [O-][N+](=O)CN1CCCC1=O AEDAWHHRIHMZAR-UHFFFAOYSA-N 0.000 description 7
- 239000002174 Styrene-butadiene Substances 0.000 description 5
- 239000006229 carbon black Substances 0.000 description 5
- 230000000052 comparative effect Effects 0.000 description 5
- 239000003292 glue Substances 0.000 description 5
- 239000004615 ingredient Substances 0.000 description 5
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 4
- 229910021382 natural graphite Inorganic materials 0.000 description 4
- 239000002245 particle Substances 0.000 description 4
- 229910052782 aluminium Inorganic materials 0.000 description 3
- 239000008367 deionised water Substances 0.000 description 3
- 229910021641 deionized water Inorganic materials 0.000 description 3
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 description 2
- 239000013543 active substance Substances 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 239000003792 electrolyte Substances 0.000 description 2
- 229910003002 lithium salt Inorganic materials 0.000 description 2
- 159000000002 lithium salts Chemical class 0.000 description 2
- 239000012046 mixed solvent Substances 0.000 description 2
- OTYYBJNSLLBAGE-UHFFFAOYSA-N CN1C(CCC1)=O.[N] Chemical compound CN1C(CCC1)=O.[N] OTYYBJNSLLBAGE-UHFFFAOYSA-N 0.000 description 1
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 1
- 229910012851 LiCoO 2 Inorganic materials 0.000 description 1
- 229910013870 LiPF 6 Inorganic materials 0.000 description 1
- WHXSMMKQMYFTQS-UHFFFAOYSA-N Lithium Chemical compound [Li] WHXSMMKQMYFTQS-UHFFFAOYSA-N 0.000 description 1
- 239000002033 PVDF binder Substances 0.000 description 1
- 239000006230 acetylene black Substances 0.000 description 1
- 239000011149 active material Substances 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 239000011230 binding agent Substances 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 239000011248 coating agent Substances 0.000 description 1
- 238000000576 coating method Methods 0.000 description 1
- 239000011889 copper foil Substances 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 239000006185 dispersion Substances 0.000 description 1
- 239000012153 distilled water Substances 0.000 description 1
- 238000004146 energy storage Methods 0.000 description 1
- 239000011888 foil Substances 0.000 description 1
- 238000000265 homogenisation Methods 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 229910052744 lithium Inorganic materials 0.000 description 1
- 238000005461 lubrication Methods 0.000 description 1
- 230000014759 maintenance of location Effects 0.000 description 1
- 229910052759 nickel Inorganic materials 0.000 description 1
- 229920002981 polyvinylidene fluoride Polymers 0.000 description 1
- 239000007774 positive electrode material Substances 0.000 description 1
- 238000001556 precipitation Methods 0.000 description 1
- 238000004062 sedimentation Methods 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
Classifications
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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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- Battery Electrode And Active Subsutance (AREA)
Abstract
本发明公开了一种锂离子电池、负极浆料及其制备方法,该方法包括以下步骤:(1)将负极活性物质和负极导电剂在搅拌器中混合后加入润滑剂搅拌均匀;(2)将添加剂羧甲基纤维素钠CMC加入搅拌器中搅拌;(3)将上述搅拌器中物质加入负极溶剂水和负极粘结剂的混合胶料中,混合搅拌均匀,制成负极浆料。所述润滑剂为醇、酮或醇与酮的混合物。本发明由于采用润湿剂与石墨及导电剂混合,可有效缩短润湿时间,缩短浆料制备时间,提高负极浆料的均匀性和稳定性。The invention discloses a lithium ion battery, a negative electrode slurry and a preparation method thereof. The method comprises the following steps: (1) mixing the negative electrode active material and the negative electrode conductive agent in a stirrer, adding a lubricant and stirring evenly; (2) Add the additive sodium carboxymethyl cellulose CMC into the stirrer and stir; (3) add the above-mentioned substance in the stirrer to the mixed rubber material of the negative electrode solvent water and the negative electrode binder, mix and stir evenly, and make the negative electrode slurry. The lubricant is alcohol, ketone or a mixture of alcohol and ketone. Because the present invention mixes the wetting agent with the graphite and the conductive agent, the wetting time can be effectively shortened, the slurry preparation time can be shortened, and the uniformity and stability of the negative electrode slurry can be improved.
Description
技术领域 technical field
本发明涉及锂离子电池制造领域,具体是涉及一种锂离子电池的负极浆料及其制备方法。The invention relates to the field of lithium ion battery manufacturing, in particular to a negative electrode slurry of a lithium ion battery and a preparation method thereof.
背景技术 Background technique
锂离子电池于上世纪90年代由日本索尼公司推向市场,因其单体电池工作电压高、能量密度大、循环寿命长等特点,在手机、笔记本电脑等小型移动电源领域得到广泛应用。随着锂离子电池能量密度及功率密度的进一步提升,它已被视作混合动力汽车及电动汽车的理想电源,是一类具有广阔应用前景的储能装置。Lithium-ion batteries were introduced to the market by Sony Corporation of Japan in the 1990s. Because of their high operating voltage, high energy density, and long cycle life, they are widely used in mobile phones, laptops and other small mobile power fields. With the further improvement of the energy density and power density of lithium-ion batteries, it has been regarded as an ideal power source for hybrid electric vehicles and electric vehicles, and it is a type of energy storage device with broad application prospects.
锂离子电池制备工艺的第一道工序是匀浆,就是将活性物质与溶剂、导电剂、粘结剂等混合均匀以获得具有一定黏度和固含量的浆料。现有的正极浆料多使用NMP(氮甲基吡咯烷酮)为溶剂(即为油性浆料)。负极浆料在降低成本的压力下溶剂由NMP改为水(即为水性浆料)。使用水作溶剂虽可显著降低锂离子电池的制造成本,但水性浆料的稳定性不及油性浆料,容易发生沉降现象,影响了生产的连续稳定运转。为提高水性浆料的稳定性,中国专利文献CN 101609882A提出油水混合的工艺,即在胶液制备过程中使用油水混合溶剂,该工艺可制备比水性浆料稳定性好的负极浆料。然而,该工艺用时很长(14~20h),严重影响了生产效率的提升,而且采用NMP比率过高的话,对降低成本的作用有限。The first process of the lithium-ion battery preparation process is homogenization, which is to mix the active material with solvent, conductive agent, binder, etc. to obtain a slurry with a certain viscosity and solid content. The existing positive electrode slurry mostly uses NMP (nitromethylpyrrolidone) as a solvent (that is, oily slurry). The solvent of negative electrode slurry is changed from NMP to water under the pressure of cost reduction (that is, water-based slurry). Although using water as a solvent can significantly reduce the manufacturing cost of lithium-ion batteries, the stability of water-based slurry is not as good as that of oil-based slurry, and sedimentation is prone to occur, which affects the continuous and stable operation of production. In order to improve the stability of the water-based slurry, the Chinese patent document CN 101609882A proposes a process of mixing oil and water, that is, using a mixed solvent of oil and water in the glue preparation process, and this process can prepare a negative electrode slurry with better stability than the water-based slurry. However, this process takes a long time (14-20 hours), which seriously affects the improvement of production efficiency, and if the ratio of NMP is too high, it will have a limited effect on reducing costs.
由于石墨颗粒在水中的表面张力大,虽然石墨的密度大于水,但将石墨粉末洒向水面后,石墨颗粒表面因无法有效润湿而在水面漂浮,不易在水中均匀分散。现有的水性石墨负极浆料的生产工艺中会加入防沉淀剂羧甲基纤维素钠CMC。CMC黏度高,不利于活性物质与胶液的混合,严重时甚至会因为半干料黏附在搅拌机的搅拌浆上,搅拌浆所受阻力大于搅拌机所能提供的搅拌力,导致设备报警,对正常生产造成很大影响。Due to the high surface tension of graphite particles in water, although the density of graphite is greater than that of water, after the graphite powder is sprinkled on the water surface, the surface of graphite particles cannot be effectively wetted and floats on the water surface, which is not easy to disperse evenly in water. An anti-precipitation agent sodium carboxymethyl cellulose CMC is added in the existing production process of water-based graphite negative electrode slurry. CMC has a high viscosity, which is not conducive to the mixing of active substances and glue. In severe cases, even semi-dry materials will adhere to the stirring paddle of the mixer. The resistance of the stirring paddle is greater than the stirring force that the mixer can provide, causing the equipment to alarm. Production is greatly affected.
发明内容 Contents of the invention
本发明要解决的技术问题是克服以上缺陷,提出一种锂离子电池负极浆料的制备方法,提高水性负极浆料的均匀性、稳定性。The technical problem to be solved by the present invention is to overcome the above defects, propose a preparation method of lithium-ion battery negative electrode slurry, and improve the uniformity and stability of the aqueous negative electrode slurry.
本发明还提出采用该制备方法制备的锂离子电池及其负极浆料。The invention also proposes the lithium ion battery and its negative electrode slurry prepared by the preparation method.
本发明的技术问题是通过以下技术方案予以实现的。The technical problem of the present invention is achieved through the following technical solutions.
这种锂离子电池负极浆料的制备方法包括以下步骤:(1)将负极活性物质和负极导电剂在搅拌器中混合后加入润滑剂搅拌均匀;(2)将添加剂羧甲基纤维素钠CMC加入搅拌器中搅拌;(3)将上述搅拌器中物质加入负极溶剂水和负极粘结剂的混合胶料中,混合搅拌均匀,制成负极浆料。The preparation method of this lithium-ion battery negative electrode slurry comprises the following steps: (1) mixing the negative electrode active material and the negative electrode conductive agent in a stirrer, adding lubricant and stirring evenly; (2) adding the additive sodium carboxymethylcellulose CMC Adding to a stirrer and stirring; (3) adding the above-mentioned substance in the stirrer to the mixed rubber material of the negative electrode solvent water and the negative electrode binder, and mixing and stirring evenly to prepare the negative electrode slurry.
所述润滑剂为醇、酮或醇与酮的混合物。The lubricant is alcohol, ketone or a mixture of alcohol and ketone.
所述润滑剂为氮甲基吡咯烷酮NMP、甲醇、乙醇、丙酮之一种或多种的混合物。The lubricant is one or more of NMP, methanol, ethanol and acetone.
所述润滑剂的重量为负极活性物质和负极导电剂粉体重量和的1/20~1/4。The weight of the lubricant is 1/20-1/4 of the sum of the weight of the negative electrode active material and the negative electrode conductive agent powder.
所述步骤(1)中将负极活性物质和负极导电剂、润滑剂搅拌5~40分钟,并在搅拌时对搅拌器内部抽真空。In the step (1), the negative electrode active material, the negative electrode conductive agent, and the lubricant are stirred for 5 to 40 minutes, and the inside of the stirrer is evacuated during stirring.
所述步骤(2)中将添加剂CMC分次加入搅拌器中搅拌。In the step (2), the additive CMC is added in batches to the stirrer and stirred.
所述负极导电剂为导电碳黑,所述负极粘结剂为丁苯橡胶SBR。The negative electrode conductive agent is conductive carbon black, and the negative electrode binder is styrene-butadiene rubber SBR.
本发明提出的锂离子电池负极浆料采用上述锂离子电池负极浆料的制备方法制备。The lithium ion battery negative electrode slurry proposed by the present invention is prepared by the above-mentioned preparation method of the lithium ion battery negative electrode slurry.
本发明提出的锂离子电池的制备方法,包括负极浆料的制备步骤,所述负极浆料的制备步骤包括以下步骤:(1)将负极活性物质和负极导电剂在搅拌器中混合后加入润滑剂搅拌均匀;(2)将添加剂CMC加入搅拌器中搅拌;(3)将上述搅拌器中物质加入负极溶剂水和负极粘结剂的混合胶料中,混合搅拌均匀,制成负极浆料。The preparation method of the lithium ion battery that the present invention proposes comprises the preparation step of negative electrode slurry, and the preparation step of described negative electrode slurry comprises the following steps: (1) after mixing negative electrode active material and negative electrode conductive agent in agitator, add lubrication (2) Add the additive CMC to the stirrer and stir; (3) Add the above-mentioned substance in the stirrer to the mixed rubber material of the negative electrode solvent water and the negative electrode binder, mix and stir evenly, and make the negative electrode slurry.
本发明提出的锂离子电池采用上述锂离子电池的制备方法制备。The lithium-ion battery proposed by the present invention is prepared by the above-mentioned preparation method of the lithium-ion battery.
本发明与现有技术对比所具有的有益效果是:The beneficial effect that the present invention has compared with prior art is:
1)提高生产效率。由于采用润湿剂与石墨及导电剂混合,当石墨及导电剂表面在良好润湿后,胶液可以更为顺利的达到润湿的颗粒表面,可有效缩短润湿时间,缩短浆料制备时间。1) Improve production efficiency. Due to the use of wetting agent mixed with graphite and conductive agent, when the surface of graphite and conductive agent is well wetted, the glue can reach the wet particle surface more smoothly, which can effectively shorten the wetting time and shorten the slurry preparation time .
2)提高负极浆料的均匀性、稳定性。选用与石墨具有良好润湿作用的有机液体润湿石墨,可使石墨表面充分润湿,有利于石墨颗粒在胶液中的均匀分散,促进胶液与活性物质的均匀混合提高浆料的均匀性及稳定性。2) Improve the uniformity and stability of the negative electrode slurry. Use an organic liquid that has a good wetting effect on graphite to wet the graphite, which can fully wet the graphite surface, facilitate the uniform dispersion of graphite particles in the glue, promote the uniform mixing of the glue and active substances, and improve the uniformity of the slurry and stability.
具体实施方式 Detailed ways
实施例1Example 1
制备一种锂离子电池的负极浆料,其工艺包括下列步骤。A negative electrode slurry for a lithium ion battery is prepared, and the process includes the following steps.
(101)将负极活性物质天然石墨2000g和负极导电剂碳黑50g在搅拌釜中混合,加入润滑剂甲醇15g,搅拌5~40分钟至混合均匀;(101) Mix 2000 g of negative active material natural graphite and 50 g of negative conductive agent carbon black in a stirred tank, add lubricant methanol 15 g, and stir for 5 to 40 minutes until uniformly mixed;
(102)将添加剂羧甲基纤维素钠CMC30g加入搅拌器中搅拌;(102) The additive sodium carboxymethylcellulose CMC30g is added in the stirrer and stirred;
(103)将负极溶剂去离子水2000g和负极粘结剂SBR60g的混合,制成胶料,将上述搅拌器中物质加入胶料中,混合搅拌8小时,制成负极浆料。(103) Mix 2000 g of negative electrode solvent deionized water and 60 g of negative electrode binder SBR to make a rubber compound, add the material in the above-mentioned agitator to the rubber compound, and mix and stir for 8 hours to make a negative electrode slurry.
实施例2Example 2
制备一种锂离子电池的负极浆料,其工艺包括下列步骤。A negative electrode slurry for a lithium ion battery is prepared, and the process includes the following steps.
(201)将负极活性物质天然石墨2000g和负极导电剂碳黑50g在搅拌釜中混合,加入润滑剂氮甲基吡咯烷酮NMP和丙酮共200g,搅拌5~40分钟至混合均匀;(201) 2000 g of natural graphite, a negative electrode active material, and 50 g of negative electrode conductive agent carbon black are mixed in a stirred tank, and a total of 200 g of lubricant nitrogen methyl pyrrolidone NMP and acetone are added, and stirred for 5 to 40 minutes until uniformly mixed;
(202)将添加剂羧甲基纤维素钠CMC30g加入搅拌器中搅拌;(202) The additive sodium carboxymethylcellulose CMC30g is added in the stirrer and stirred;
(203)将负极溶剂去离子水2000g和负极粘结剂SBR60g的混合,制成胶料,将上述搅拌器中物质加入胶料中,混合搅拌7.5小时,制成负极浆料。(203) Mix 2000 g of negative electrode solvent deionized water and 60 g of negative electrode binder SBR to make a rubber compound, add the material in the above-mentioned agitator to the rubber compound, and mix and stir for 7.5 hours to make a negative electrode slurry.
实施例3Example 3
制备一种锂离子电池的负极浆料,其工艺包括下列步骤。A negative electrode slurry for a lithium ion battery is prepared, and the process includes the following steps.
(301)将负极活性物质天然石墨2000g和负极导电剂碳黑50g在搅拌釜中混合,加入润滑剂甲醇和乙醇共600g,搅拌5~40分钟至混合均匀;(301) 2000g of natural graphite, the negative electrode active material, and 50g of the negative electrode conductive agent, carbon black, are mixed in a stirred tank, and a total of 600g of lubricant methanol and ethanol are added, stirred for 5 to 40 minutes until uniformly mixed;
(302)将添加剂羧甲基纤维素钠CMC30g加入搅拌器中搅拌;(302) The additive sodium carboxymethyl cellulose CMC30g is added in the stirrer and stirred;
(303)将负极溶剂蒸馏水2000g和负极粘结剂SBR60g的混合,制成胶料,将上述搅拌器中物质加入胶料中,混合搅拌7小时,制成负极浆料。(303) Mix 2000 g of negative electrode solvent distilled water and 60 g of negative electrode binder SBR to make a rubber compound, add the material in the above-mentioned agitator to the rubber compound, and mix and stir for 7 hours to make a negative electrode slurry.
对比例4Comparative example 4
制备一种锂离子电池的负极浆料,其工艺包括下列步骤。A negative electrode slurry for a lithium ion battery is prepared, and the process includes the following steps.
(401)将负极活性物质天然石墨2000g和负极导电剂碳黑50g在搅拌釜中混合;(401) negative electrode active material natural graphite 2000g and negative electrode conductive agent carbon black 50g are mixed in stirred tank;
(402)将添加剂羧甲基纤维素钠CMC30g加入搅拌器中搅拌;(402) The additive sodium carboxymethylcellulose CMC30g is added in the stirrer and stirred;
(403)将负极溶剂去离子水2000g和负极粘结剂SBR60g的混合,制成胶料,将上述搅拌器中物质加入胶料中,混合搅拌10小时,制成负极浆料。(403) Mix 2000 g of negative electrode solvent deionized water and 60 g of negative electrode binder SBR to make a rubber compound, add the above-mentioned material in the agitator to the rubber compound, and mix and stir for 10 hours to make a negative electrode slurry.
将上述实施例1~3和对比例4制备过程的数据进行比较,测量其制备过程中的浆料粘度、静置8小时后观察浆料的稳定性。如表1所示。The data of the preparation process of the above-mentioned Examples 1-3 and Comparative Example 4 were compared, the viscosity of the slurry during the preparation process was measured, and the stability of the slurry was observed after standing for 8 hours. As shown in Table 1.
表1Table 1
实施例5Example 5
制备型号为423048AH,标称容量为650mAh的锂离子电池,其电芯的制备步骤如下。To prepare a lithium-ion battery with a model number of 423048AH and a nominal capacity of 650mAh, the steps for preparing the battery cell are as follows.
501)正极配料。将正极活性物质钴酸锂LiCoO2、正极导电剂乙炔黑(采用卡博特CABOT超导电碳黑BP2000)、正极粘合剂PVDF(型号RC10214)与溶剂NMP混合搅拌均匀,制成正极浆料。501) Positive electrode ingredients. The positive electrode active material lithium cobaltate LiCoO 2 , the positive electrode conductive agent acetylene black (cabot CABOT superconducting carbon black BP2000), the positive electrode binder PVDF (model RC10214) and the solvent NMP were mixed and stirred evenly to prepare the positive electrode slurry.
502)负极配料。采用实施例1中的步骤制备负极浆料。502) Negative electrode ingredients. The steps in Example 1 were used to prepare negative electrode slurry.
503)涂覆。将正极浆料涂覆在16μm厚度正极集流体铝箔的双面上,干燥并辊压制成正极片,将正极片分切成一定尺寸的正极小片,并在正极小片上焊接上铝带。将负极浆料涂覆在10μm厚度的负极集流体铜箔上,干燥并辊压制成负极片,将负极片分切成一定尺寸的负极小片,并在负极小片上焊接上镍带。503) Coating. The positive electrode slurry was coated on both sides of the positive electrode current collector aluminum foil with a thickness of 16 μm, dried and rolled to form a positive electrode sheet, and the positive electrode sheet was cut into positive electrode pieces of a certain size, and an aluminum strip was welded on the positive electrode sheet. The negative electrode slurry is coated on a negative electrode current collector copper foil with a thickness of 10 μm, dried and rolled to form a negative electrode sheet, the negative electrode sheet is cut into a certain size of negative electrode small pieces, and a nickel strip is welded on the negative electrode small pieces.
504)配制电解液。将锂盐LiPF6溶解在锂盐溶剂中,溶剂采用EC、EMC、DMC混合溶剂,三者的质量比为EC∶EMC∶DMC=1∶1∶1。504) prepare electrolyte. The lithium salt LiPF 6 is dissolved in a lithium salt solvent, and the solvent is a mixed solvent of EC, EMC, and DMC, and the mass ratio of the three is EC:EMC:DMC=1:1:1.
505)装配。将分切好的正极小片、隔膜和负极小片叠置或卷绕后装入铝金属电池外壳中,将电池外壳与盖帽组件进行焊接密封,将配制好的电解液注入铝壳中。505) Assembly. The cut positive electrode pieces, separators and negative electrode pieces are stacked or wound into an aluminum metal battery case, the battery case and the cap assembly are welded and sealed, and the prepared electrolyte is injected into the aluminum case.
506)电池化成、分容。506) Battery formation and capacity division.
实施例6Example 6
其与实施例5不同之处在于,步骤502)负极配料中,采用实施例2中的步骤制备负极浆料。It differs from Example 5 in that, in step 502) in the negative electrode ingredients, the steps in Example 2 are used to prepare the negative electrode slurry.
实施例7Example 7
其与实施例5不同之处在于,步骤502)负极配料中,采用实施例3中的步骤制备负极浆料。It differs from Example 5 in that, in step 502) in the negative electrode ingredients, the steps in Example 3 are used to prepare the negative electrode slurry.
对比例8Comparative example 8
其与实施例5不同之处在于,步骤502)负极配料中,采用对比例4中的步骤制备负极浆料。It differs from Example 5 in that in step 502) in the negative electrode ingredients, the steps in Comparative Example 4 are used to prepare the negative electrode slurry.
取实施例5~7和对比例8所得的电池各50只进行循环性能测试,测试步骤为:先将化成后的电池以0.5C恒流充电至4.2V,再以4.2V恒压充电至截止电流0.02C。然后以1C电流放电至3.7V。重复以上过程,记录每次的放电容量,计算循环300次后的容量保持率。结果如表2所示。Take 50 batteries obtained in Examples 5-7 and Comparative Example 8 to test the cycle performance. The test steps are as follows: first charge the formed batteries to 4.2V at a constant current of 0.5C, and then charge at a constant voltage of 4.2V to the cut-off Current 0.02C. Then discharge to 3.7V with 1C current. Repeat the above process, record the discharge capacity each time, and calculate the capacity retention rate after 300 cycles. The results are shown in Table 2.
表2Table 2
从表1、2中可以看出,在负极浆料中添加醇、酮有机润滑剂后,电池具有良好的循环性能,且由于负极浆料的制备时间缩短,使得电池生产效率得到提高、成本降低。It can be seen from Tables 1 and 2 that after adding alcohol and ketone organic lubricants to the negative electrode slurry, the battery has good cycle performance, and because the preparation time of the negative electrode slurry is shortened, the production efficiency of the battery is improved and the cost is reduced. .
以上内容是结合具体的实施方式对本发明所作的进一步详细说明,不能认定本发明的具体实施只局限于这些说明。对于本发明所属技术领域的普通技术人员来说,在不脱离本发明构思的前提下,还可以做出若干简单推演或替换,都应当视为属于本发明的保护范围。The above content is a further detailed description of the present invention in conjunction with specific embodiments, and it cannot be assumed that the specific implementation of the present invention is limited to these descriptions. For those of ordinary skill in the technical field of the present invention, without departing from the concept of the present invention, some simple deduction or replacement can be made, which should be regarded as belonging to the protection scope of the present invention.
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