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CN114464776B - Preparation method of ultrahigh-power ultrathin negative plate capable of being produced in batch - Google Patents

Preparation method of ultrahigh-power ultrathin negative plate capable of being produced in batch Download PDF

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CN114464776B
CN114464776B CN202210056346.8A CN202210056346A CN114464776B CN 114464776 B CN114464776 B CN 114464776B CN 202210056346 A CN202210056346 A CN 202210056346A CN 114464776 B CN114464776 B CN 114464776B
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negative electrode
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active material
slurry
electrode sheet
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CN114464776A (en
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唐月娇
班宵汉
刘富亮
刘江涛
陈晓涛
袁再芳
胡锦飞
刁思强
苏纪宏
周雄
陈安国
向斌
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Chongqing University
Guizhou Meiling Power Supply Co Ltd
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Guizhou Meiling Power Supply Co Ltd
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    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/02Electrodes composed of, or comprising, active material
    • H01M4/13Electrodes for accumulators with non-aqueous electrolyte, e.g. for lithium-accumulators; Processes of manufacture thereof
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/02Electrodes composed of, or comprising, active material
    • H01M4/13Electrodes for accumulators with non-aqueous electrolyte, e.g. for lithium-accumulators; Processes of manufacture thereof
    • H01M4/131Electrodes based on mixed oxides or hydroxides, or on mixtures of oxides or hydroxides, e.g. LiCoOx
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/02Electrodes composed of, or comprising, active material
    • H01M4/13Electrodes for accumulators with non-aqueous electrolyte, e.g. for lithium-accumulators; Processes of manufacture thereof
    • H01M4/133Electrodes based on carbonaceous material, e.g. graphite-intercalation compounds or CFx
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/02Electrodes composed of, or comprising, active material
    • H01M4/13Electrodes for accumulators with non-aqueous electrolyte, e.g. for lithium-accumulators; Processes of manufacture thereof
    • H01M4/136Electrodes based on inorganic compounds other than oxides or hydroxides, e.g. sulfides, selenides, tellurides, halogenides or LiCoFy
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/02Electrodes composed of, or comprising, active material
    • H01M4/13Electrodes for accumulators with non-aqueous electrolyte, e.g. for lithium-accumulators; Processes of manufacture thereof
    • H01M4/139Processes of manufacture
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/02Electrodes composed of, or comprising, active material
    • H01M4/13Electrodes for accumulators with non-aqueous electrolyte, e.g. for lithium-accumulators; Processes of manufacture thereof
    • H01M4/139Processes of manufacture
    • H01M4/1391Processes of manufacture of electrodes based on mixed oxides or hydroxides, or on mixtures of oxides or hydroxides, e.g. LiCoOx
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/02Electrodes composed of, or comprising, active material
    • H01M4/13Electrodes for accumulators with non-aqueous electrolyte, e.g. for lithium-accumulators; Processes of manufacture thereof
    • H01M4/139Processes of manufacture
    • H01M4/1393Processes of manufacture of electrodes based on carbonaceous material, e.g. graphite-intercalation compounds or CFx
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/02Electrodes composed of, or comprising, active material
    • H01M4/13Electrodes for accumulators with non-aqueous electrolyte, e.g. for lithium-accumulators; Processes of manufacture thereof
    • H01M4/139Processes of manufacture
    • H01M4/1397Processes of manufacture of electrodes based on inorganic compounds other than oxides or hydroxides, e.g. sulfides, selenides, tellurides, halogenides or LiCoFy
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/10Energy storage using batteries

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  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Materials Engineering (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Electrochemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Manufacturing & Machinery (AREA)
  • Inorganic Chemistry (AREA)
  • Battery Electrode And Active Subsutance (AREA)

Abstract

The application discloses a preparation method of an ultra-high power ultra-thin negative plate capable of mass production in the technical field of chemical energy storage batteries, which comprises the following steps of preparing a negative active material, wherein the negative active material is one or more of hard carbon, soft carbon, graphite, mesophase carbon microspheres, lithium titanate, silicon carbon and silicon oxide, D90 of the negative active material is less than or equal to 5 mu m, and the specific surface area of the negative active material is greater than or equal to 5m 2/g. Mixing the raw materials of the negative plate together, kneading to form slurry, when the fineness of the slurry is less than or equal to a negative electrode active substance D90, finishing kneading, adding a binder and water into the kneaded slurry for dilution, regulating and controlling, sieving, putting into a coating machine, carrying out double-sided coating on a current collector, wherein the total thickness of the double-sided coating is less than or equal to 60 mu m, and carrying out high-temperature drying after coating to obtain the high-power ultrathin negative plate. The negative plate realizes 1500C limit discharge, and provides a new solving way for mass production of ultra-high power supply.

Description

一种能批量化生产的超高功率超薄负极片的制备方法A method for preparing ultra-high power ultra-thin negative electrode sheets capable of mass production

技术领域Technical Field

本发明涉及化学储能电池的技术领域,具体涉及一种能批量化生产的超高功率超薄负极片的制备方法。The present invention relates to the technical field of chemical energy storage batteries, and in particular to a method for preparing ultra-high power ultra-thin negative electrode sheets that can be mass-produced.

背景技术Background Art

随着科技的发展,军用及民用储能市场对功率要求越来越高,在极片制备方向上,目前提高电池倍率性能主要有以下途径:即以超级电容器为方向开展高性能超厚极片制备,提高活性物质负载,以提高的超级电容器的比功率和比能量。基于此,目前的高比能锂离子电池,例如航模及无人机等高功率锂离子电池放电在30C,但是负极极片的厚度在100μm左右,电池的比功率在3~5Kw/kg。但是其倍率性能无法满足电子炮、激光武器、微波武器等需求超高功率武器的使用需求。With the development of science and technology, the military and civilian energy storage markets have higher and higher power requirements. In terms of pole piece preparation, there are currently the following main ways to improve battery rate performance: namely, to carry out high-performance ultra-thick pole piece preparation with supercapacitors as the direction, increase the active material load, and improve the specific power and specific energy of supercapacitors. Based on this, the current high-energy lithium-ion batteries, such as high-power lithium-ion batteries such as model aircraft and drones, are discharged at 30C, but the thickness of the negative pole piece is about 100μm, and the specific power of the battery is 3 to 5Kw/kg. However, its rate performance cannot meet the use requirements of ultra-high power weapons such as electronic cannons, laser weapons, and microwave weapons.

发明内容Summary of the invention

本发明针对现有技术的不足,设计一种高功率超薄负极片。In view of the deficiencies of the prior art, the present invention designs a high-power ultra-thin negative electrode sheet.

本发明的目的之一是提供一种能批量化生产的超高功率超薄负极片的制备方法,原料包括负极活性物质,负极活性物质为硬碳、软碳、石墨、中间相碳微球、钛酸锂、硅碳、氧化亚硅中的一种或多种,负极活性物质D90≤5μm,比表面积大于≧5m2/g。One of the purposes of the present invention is to provide a method for preparing ultra-high power ultra-thin negative electrode sheets that can be mass-produced. The raw materials include negative electrode active materials, which are one or more of hard carbon, soft carbon, graphite, mesophase carbon microspheres, lithium titanate, silicon carbon, and silicon oxide. The negative electrode active materials have a D90 of ≤5μm and a specific surface area of greater than ≧ 5m2 /g.

进一步的,原料还包括导电剂、增稠剂和粘结剂,将负极活性物质、导电剂和增稠剂混合在一起,采用捏合工艺捏合形成浆料,当浆料细度≤负极活性物质D90时,捏合结束,加入粘结剂混合均匀,加入去离子水稀释调控,过筛,将浆料装入到涂布机中,对集流体的双面分别进行涂覆,双面涂覆的总厚度≦60μm,涂布后进行高温干燥,得到高功率超薄负极片。Furthermore, the raw materials also include a conductive agent, a thickener and a binder. The negative electrode active material, the conductive agent and the thickener are mixed together and kneaded into a slurry using a kneading process. When the slurry fineness is ≤ D90 of the negative electrode active material, the kneading is completed, the binder is added and mixed evenly, deionized water is added to dilute and regulate, the slurry is sieved, and the slurry is loaded into a coating machine to coat both sides of the current collector respectively. The total thickness of the double-sided coating is ≤60μm. After coating, it is dried at high temperature to obtain a high-power ultra-thin negative electrode sheet.

进一步的,浆料的μ/σ<1s/m。其中μ为浆料粘度,σ为浆料流体的表面张力。Furthermore, μ/σ of the slurry is less than 1 s/m, where μ is the slurry viscosity and σ is the surface tension of the slurry fluid.

进一步的,涂布机为转移式涂布机或挤压式涂布机。Furthermore, the coater is a transfer coater or an extrusion coater.

进一步的,高温干燥在真空干燥箱中进行,干燥温度为100℃~200℃,干燥时间为2~100h,真空度≥85Mpa。Furthermore, high temperature drying is carried out in a vacuum drying oven, the drying temperature is 100°C to 200°C, the drying time is 2 to 100 hours, and the vacuum degree is ≥85Mpa.

进一步的,所述导电剂为超导炭黑SP,增稠剂为CMC,粘结剂为SBR。Furthermore, the conductive agent is superconducting carbon black SP, the thickener is CMC, and the binder is SBR.

进一步的,所述集流体为铜箔。Furthermore, the current collector is copper foil.

本发明的目的之二是提供一种高功率超薄负极片,利用上述方法制备。The second object of the present invention is to provide a high-power ultra-thin negative electrode sheet prepared using the above method.

本发明的目的之三是提供高功率超薄负极片在超高功率电源中的应用。A third object of the present invention is to provide an application of a high-power ultra-thin negative electrode sheet in an ultra-high power power supply.

本发明的工作原理:本发明的原材料选取小粒径的材料,大幅缩短材料的内部的离子和电子传输路径,同时通过高孔超薄极片制备,扩宽Li+在极片的传输通道并缩短Li+传输距离,也缩短电子在极片的传输距离,并结合捏合原理,通过机械搅拌使颗粒-颗粒相互作用,解决高比表面积、小粒径材料负极材料在制浆过程中容易团聚的问题,再通过对浆料进行调控,制备可用于转移式涂布机或挤压式涂布机涂布的进行超薄涂布的负极浆料,制备出厚度偏差低于1μm,无明显涂布缺陷的超高功率负极片,使负极片实现了1500C极限放电,为量产超高功率电源提供一种新的解决途径。Working principle of the present invention: The raw materials of the present invention are selected from materials with small particle size, which greatly shortens the internal ion and electron transmission paths of the materials. At the same time, through the preparation of high-porous ultra-thin electrode sheets, the transmission channel of Li+ in the electrode sheets is widened and the Li+ transmission distance is shortened, and the transmission distance of electrons in the electrode sheets is also shortened. In combination with the kneading principle, mechanical stirring is used to make particles interact with each other, so as to solve the problem that high specific surface area and small particle size negative electrode materials are easy to agglomerate during the pulping process. Then, by regulating the slurry, a negative electrode slurry for ultra-thin coating that can be used for transfer coater or extrusion coater is prepared, and an ultra-high power negative electrode sheet with a thickness deviation of less than 1μm and no obvious coating defects is prepared, so that the negative electrode sheet achieves 1500C limit discharge, providing a new solution for mass production of ultra-high power power supplies.

附图说明BRIEF DESCRIPTION OF THE DRAWINGS

图1为本发明实施案例1捏合成功浆料细度图;FIG1 is a diagram of the fineness of a successfully kneaded slurry in Example 1 of the present invention;

图2为本发明实施案例1高功率超薄极片双面厚度(去集流体厚度)的测试图;FIG2 is a test diagram of the double-sided thickness (excluding the current collector thickness) of the high-power ultra-thin pole piece of Example 1 of the present invention;

图3为本发明实施案例1-2和对比例3-5制备极片1500C秒充放电曲线图。FIG3 is a 1500C second charge-discharge curve diagram of the electrode sheets prepared in Examples 1-2 and Comparative Examples 3-5 of the present invention.

具体实施方式DETAILED DESCRIPTION

面对本发明的具体实施方式作进一步详细的说明,但本发明并不局限于这些实施方式,任何在本实施例基本精神上的改进或代替,仍属于本发明权利要求所要求保护的范围。The specific embodiments of the present invention are further described in detail, but the present invention is not limited to these embodiments. Any improvement or substitution based on the basic spirit of the present embodiment still falls within the scope of protection required by the claims of the present invention.

实施案例1~2的高功率超薄极片和对比案例的1~3负极片按照下述进行制备:The high-power ultra-thin electrode sheets of implementation cases 1 to 2 and the negative electrode sheets of comparison cases 1 to 3 were prepared as follows:

实施例1Example 1

称取D90为5μm,比表面积为6m2/g的石墨材料,和导电剂SP一起,加入到CMC水溶液(CMC与水的质量比为1:40)中进行捏合,其中,负极片的原料中石墨材料、导电剂SP、粘结剂SBR、增稠剂CMC按质量比为95:1:2:2。每搅拌1h取样进行细度测试,如图1所示,直至浆料细度为5μm,确保浆料无团聚,捏合结束,加入一定量SBR继续搅拌,加入水稀释至μ/σ为0.3s/m,过筛,采用转移式涂布机对集流体的双面分别进行涂布,双面涂覆的总厚度为30μm,如图2所示,最终高功率超薄极片双面厚度(去集流体厚度)30μm,涂布后的极片在真空度85Mpa、120℃的环境中干燥12h,得到高功率超薄负极片。Weigh a graphite material with a D90 of 5 μm and a specific surface area of 6 m 2 /g, and add it to a CMC aqueous solution (the mass ratio of CMC to water is 1:40) together with a conductive agent SP for kneading. Among the raw materials of the negative electrode sheet, the mass ratio of the graphite material, the conductive agent SP, the binder SBR, and the thickener CMC is 95:1:2:2. Take a sample for fineness test every 1 hour of stirring, as shown in Figure 1, until the slurry fineness is 5 μm, ensure that the slurry has no agglomeration, kneading is completed, add a certain amount of SBR and continue stirring, add water to dilute to μ/σ of 0.3s/m, sieve, and use a transfer coater to coat both sides of the current collector respectively. The total thickness of the double-sided coating is 30 μm, as shown in Figure 2. The final high-power ultra-thin electrode sheet has a double-sided thickness (excluding the current collector thickness) of 30 μm. The coated electrode sheet is dried for 12 hours in an environment of 85 MPa vacuum and 120°C to obtain a high-power ultra-thin negative electrode sheet.

实施例2Example 2

称取D90为4μm,比表面积为8m2/g的硬碳材料,和导电剂SP一起,加入到CMC水溶液(CMC与水的质量比为1:40)中进行捏合,其中,负极片的原料中硬碳材料、导电剂SP、粘结剂SBR、增稠剂CMC按质量比为95:1:2:2。每搅拌1h取样进行细度测试,直至浆料细度为4μm,确保浆料无团聚,捏合结束,加入一定量SBR继续搅拌,加入水稀释至μ/σ为0.3s/m,过筛,采用转移式涂布机对集流体的双面分别进行涂布,双面涂覆的总厚度为30μm,涂布后的极片在真空度85Mpa、120℃的环境中干燥12h,得到高功率超薄负极片。Weigh a hard carbon material with a D90 of 4 μm and a specific surface area of 8 m 2 /g, and add it to a CMC aqueous solution (the mass ratio of CMC to water is 1:40) together with a conductive agent SP for kneading. The raw materials of the negative electrode sheet have a mass ratio of 95:1:2:2 for the hard carbon material, conductive agent SP, binder SBR, and thickener CMC. Take a sample for fineness test every 1 hour of stirring until the slurry fineness is 4 μm to ensure that the slurry has no agglomeration. After kneading, add a certain amount of SBR and continue stirring. Add water to dilute to μ/σ of 0.3 s/m, sieve, and use a transfer coater to coat both sides of the current collector. The total thickness of the double-sided coating is 30 μm. The coated electrode sheet is dried in a vacuum environment of 85 MPa and 120°C for 12 hours to obtain a high-power ultra-thin negative electrode sheet.

对比例1Comparative Example 1

称取D90为21μm,比表面积为1m2/g的石墨材料,和导电剂SP一起,加入CMC水溶液(CMC与水的质量比为1:40)中进行捏合,负极片的原料中石墨材料、导电剂SP、粘结剂SBR、增稠剂CMC按质量比为95:1:2:2。每搅拌1h取样进行细度测试,直至浆料细度少于21μm,加入一定量SBR搅拌,加入水稀释μ/σ为0.3s/m,过筛,采用转移式涂布机对集流体进行涂布,涂布后的极片在真空度85Mpa、120℃的环境中干燥12h,得到负极片。Weigh a graphite material with a D90 of 21 μm and a specific surface area of 1 m 2 /g, and add it to a CMC aqueous solution (the mass ratio of CMC to water is 1:40) together with a conductive agent SP for kneading. The mass ratio of graphite material, conductive agent SP, binder SBR, and thickener CMC in the raw materials of the negative electrode sheet is 95:1:2:2. Take a sample for fineness test every 1 hour of stirring until the slurry fineness is less than 21 μm, add a certain amount of SBR and stir, add water to dilute μ/σ to 0.3 s/m, sieve, and use a transfer coater to coat the current collector. The coated electrode sheet is dried for 12 hours in an environment with a vacuum degree of 85 MPa and 120°C to obtain a negative electrode sheet.

对比例2Comparative Example 2

称取D90为5μm,比表面积为6m2/g的石墨材料,和导电剂SP一起,加入CMC水溶液(CMC与水的质量比为1:40)中,负极片的原料中石墨材料、导电剂SP、粘结剂SBR、增稠剂CMC按质量比为95:1:2:2。搅拌混合,此时浆料细度为18μm,加入一定量SBR搅拌,加入水稀释至μ/σ为0.3s/m,过筛,采用转移式涂布机对集流体进行涂布,涂布后的极片在真空度85Mpa、120℃的环境中干燥12h,得到负极片。Weigh a graphite material with a D90 of 5 μm and a specific surface area of 6 m 2 /g, and add it to a CMC aqueous solution (the mass ratio of CMC to water is 1:40) together with a conductive agent SP. The mass ratio of the graphite material, conductive agent SP, binder SBR, and thickener CMC in the raw materials of the negative electrode sheet is 95:1:2:2. Stir and mix. At this time, the slurry fineness is 18 μm. Add a certain amount of SBR and stir. Add water to dilute to μ/σ of 0.3 s/m, sieve, and use a transfer coater to coat the current collector. The coated electrode sheet is dried in an environment of 85 MPa vacuum and 120°C for 12 hours to obtain a negative electrode sheet.

对比例3Comparative Example 3

称取D90为10μm,比表面积为1m2/g的石墨材料,和导电剂SP一起,加入CMC水溶液(CMC与水的质量比为1:40)中进行捏合,负极片的原料中石墨材料、导电剂SP、粘结剂SBR、增稠剂CMC按质量比为95:1:2:2。每搅拌1h取样进行细度测试,直至浆料细度少于10μm,加入一定量SBR搅拌,加入水稀释至μ/σ为0.3s/m,过筛,采用转移式涂布机对集流体的双面进行涂布,双面涂覆的总厚度为30μm,涂布后的极片在真空度85Mpa、120℃的环境中干燥12h,得到负极片。Weigh a graphite material with a D90 of 10 μm and a specific surface area of 1 m 2 /g, and add it to a CMC aqueous solution (the mass ratio of CMC to water is 1:40) together with a conductive agent SP for kneading. The mass ratio of graphite material, conductive agent SP, binder SBR, and thickener CMC in the raw materials of the negative electrode sheet is 95:1:2:2. Take a sample for fineness test every 1 hour of stirring until the slurry fineness is less than 10 μm, add a certain amount of SBR and stir, add water to dilute to μ/σ of 0.3 s/m, sieve, and use a transfer coater to coat both sides of the current collector. The total thickness of the double-sided coating is 30 μm. The coated electrode sheet is dried in an environment of 85 MPa vacuum and 120°C for 12 hours to obtain a negative electrode sheet.

对比例4Comparative Example 4

称取选项一定D90为5μm,比表面积为6m2/g的石墨材料,和SP,加入CMC水溶液(CMC与水的质量比为1:40)中进行捏合,负极片的性物质层、导电剂SP、粘结剂SBR、增稠剂CMC,按质量比为95:1:2:2。每搅拌1h取样进行细度测试,直至浆料细度5μm,加入一定量SBR搅拌,加入水稀释至0.3s/m,过筛,采用转移式涂布机对集流体的双面分别进行涂布,双面涂覆的总厚度为30μm,涂布后的极片在真空度85Mpa、85℃的环境中干燥12h,得到负极片。Weigh the graphite material with a certain D90 of 5μm and a specific surface area of 6m2 /g, and SP, add them into CMC aqueous solution (the mass ratio of CMC to water is 1:40) for kneading, and the material layer of the negative electrode sheet, conductive agent SP, binder SBR, thickener CMC, according to the mass ratio of 95:1:2:2. Take samples for fineness test every 1h of stirring until the slurry fineness is 5μm, add a certain amount of SBR and stir, add water to dilute to 0.3s/m, sieve, and use a transfer coater to coat both sides of the current collector respectively. The total thickness of the double-sided coating is 30μm. The coated electrode sheet is dried for 12h in an environment of vacuum degree 85Mpa and 85℃ to obtain a negative electrode sheet.

对比例5Comparative Example 5

称取选项一定D90为5μm,比表面积为6m2/g的石墨材料,和SP,加入CMC水溶液(CMC与水的质量比为1:40)中进行捏合,负极片的性物质层、导电剂SP、粘结剂SBR、增稠剂CMC,按质量比为95:1:2:2。每搅拌1h取样进行细度测试,直至浆料细度5μm,加入一定量SBR搅拌,加入水稀释至0.3s/m,采用转移式涂布机进行涂布,涂布浆料的双面总厚度80μm,120℃干燥12h,真空度85Mpa。Weigh the graphite material with a certain D90 of 5μm and a specific surface area of 6m2 /g, and SP, add them into CMC aqueous solution (the mass ratio of CMC to water is 1:40) for kneading, and the material layer of the negative electrode sheet, conductive agent SP, binder SBR, thickener CMC, according to the mass ratio of 95:1:2:2. Take samples for fineness test every 1h of stirring until the slurry fineness is 5μm, add a certain amount of SBR and stir, add water to dilute to 0.3s/m, and use a transfer coater for coating. The total thickness of the double-sided coating slurry is 80μm, dry at 120℃ for 12h, and the vacuum degree is 85Mpa.

其中,实施例1~2和对比例1~5的集流体选择的是9μm的铜箔,其他厚度或者材质的集流体也适用。The current collectors of Examples 1 to 2 and Comparative Examples 1 to 5 are made of 9 μm copper foil, and current collectors of other thicknesses or materials are also applicable.

表1实施例1-2和对比例的1-5提供的负极片的相关参数。Table 1 Relevant parameters of the negative electrode sheets provided in Examples 1-2 and Comparative Examples 1-5.

从表1可以看出,实施例1、对比例1和2,可以看出,材料颗粒过大,或者浆料团聚,造成浆料细度过大,无法进行均匀超薄极片制备。As can be seen from Table 1, in Example 1 and Comparative Examples 1 and 2, it can be seen that the material particles are too large or the slurry is agglomerated, resulting in excessive slurry fineness, making it impossible to prepare uniform ultra-thin electrode sheets.

应用例Application Examples

实施案例1~2和对比案例的3~4锂离子电容器按照下述进行制备负极片,进行双面涂覆,按公司生产工艺组装1Ah左右叠片电芯。The negative electrode sheets of the lithium ion capacitors of implementation cases 1-2 and comparative cases 3-4 were prepared as follows, double-sided coating was performed, and stacked cells of about 1Ah were assembled according to the company's production process.

图3可以看出,实施1~2能进行1500C放电,说明活性物质重量对脉充放电影响不大,对比例3不能进行1500C放电,说明材料的粒径及比表面积是极限放电的限制因素,对比案例4能进行1500C秒充放电,但是压降大,说明烘干温度对极片极限放电具有影响,可能高温能实现高温造孔,增加扩宽Li+传途通道,对比案例5无法进行1500C秒充放电,说明极片厚度是极高倍率放电的限制因素。As can be seen from Figure 3, implementations 1 to 2 can perform 1500C discharge, indicating that the weight of the active material has little effect on pulse charge and discharge. Comparative Example 3 cannot perform 1500C discharge, indicating that the particle size and specific surface area of the material are the limiting factors of the limit discharge. Comparative Example 4 can perform 1500C second charge and discharge, but the voltage drop is large, indicating that the drying temperature has an impact on the limit discharge of the electrode. It is possible that high temperature can achieve high-temperature pore formation and increase and widen the Li + transmission channel. Comparative Example 5 cannot perform 1500C second charge and discharge, indicating that the electrode thickness is the limiting factor of the extremely high rate discharge.

以上所述的仅是本发明的实施例,方案中公知的具体结构及特性等常识在此未作过多描述。应当指出,对于本领域的技术人员来说,在不脱离本发明结构的前提下,还可以作出若干变形和改进,这些也应该视为本发明的保护范围,这些都不会影响本发明实施的效果和专利的实用性。本申请要求的保护范围应当以其权利要求的内容为准,说明书中的具体实施方式等记载可以用于解释权利要求的内容。The above is only an embodiment of the present invention, and the common knowledge such as the known specific structure and characteristics in the scheme is not described in detail here. It should be pointed out that for those skilled in the art, several deformations and improvements can be made without departing from the structure of the present invention, which should also be regarded as the protection scope of the present invention, and these will not affect the effect of the implementation of the present invention and the practicality of the patent. The scope of protection required by this application shall be based on the content of its claims, and the specific implementation methods and other records in the specification can be used to interpret the content of the claims.

Claims (5)

1.一种能批量化生产的超高功率超薄负极片的制备方法,其特征在于,原料包括负极活性物质,负极活性物质为硬碳、软碳、石墨、中间相碳微球、钛酸锂、硅碳、氧化亚硅中的一种或多种,负极活性物质D90≤5μm,比表面积大于≧5m2/g;原料还包括导电剂、增稠剂和粘结剂,将负极活性物质、导电剂和增稠剂混合在一起,采用捏合工艺捏合形成浆料,当浆料细度≤负极活性物质D90时,捏合结束,加入粘结剂混合均匀,加入去离子水稀释调控,过筛,浆料的μ/σ<1s/m,将浆料装入到涂布机中,对集流体的双面分别进行涂覆,双面涂覆的总厚度≦60μm,涂布后进行高温干燥,干燥温度为120℃,干燥时间为12h,得到高功率超薄负极片。1. A method for preparing an ultra-high power ultra-thin negative electrode sheet capable of mass production, characterized in that the raw materials include a negative electrode active material, the negative electrode active material is one or more of hard carbon, soft carbon, graphite, mesophase carbon microspheres, lithium titanate, silicon carbon, and silicon oxide, the negative electrode active material D90≤5μm, and the specific surface area is greater than≧ 5m2 /g; the raw materials also include a conductive agent, a thickener, and a binder, the negative electrode active material, the conductive agent, and the thickener are mixed together, and a kneading process is adopted to knead the negative electrode active material, when the slurry fineness is ≤D90 of the negative electrode active material, the kneading is terminated, the binder is added and mixed evenly, deionized water is added to dilute and control, the slurry is sieved, the μ/σ of the slurry is <1s/m, the slurry is loaded into a coating machine, and the double sides of the current collector are coated respectively, the total thickness of the double-sided coating is ≤60μm, and high-temperature drying is performed after coating, the drying temperature is 120°C, and the drying time is 12h to obtain a high-power ultra-thin negative electrode sheet. 2.根据权利要求1所述的一种能批量化生产的超高功率超薄负极片的制备方法,其特征在于:涂布机为转移式涂布机或挤压式涂布机。2. The method for preparing an ultra-high power ultra-thin negative electrode sheet capable of mass production according to claim 1, characterized in that the coating machine is a transfer coater or an extrusion coater. 3.根据权利要求2所述的一种能批量化生产的超高功率超薄负极片的制备方法,其特征在于:高温干燥在真空干燥箱中进行,真空度≥85Mpa。3. The method for preparing an ultra-high power ultra-thin negative electrode sheet capable of mass production according to claim 2, characterized in that: high-temperature drying is carried out in a vacuum drying oven with a vacuum degree ≥ 85Mpa. 4.一种利用权利要求1~3任一所述方法制备的超高功率超薄负极片。4. An ultra-high power ultra-thin negative electrode sheet prepared by the method according to any one of claims 1 to 3. 5.一种利用权利要求1~3任一所述方法制备的超高功率超薄负极片在超高功率电源中的应用。5. Application of an ultra-high power ultra-thin negative electrode sheet prepared by the method according to any one of claims 1 to 3 in an ultra-high power power supply.
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CN111758179A (en) * 2018-04-04 2020-10-09 株式会社东芝 Positive electrode, electrode group, and nonaqueous electrolyte battery

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