[go: up one dir, main page]

CN111785925B - Pole piece and application, low-temperature elevated safety lithium-ion battery containing the pole piece - Google Patents

Pole piece and application, low-temperature elevated safety lithium-ion battery containing the pole piece Download PDF

Info

Publication number
CN111785925B
CN111785925B CN202010802351.XA CN202010802351A CN111785925B CN 111785925 B CN111785925 B CN 111785925B CN 202010802351 A CN202010802351 A CN 202010802351A CN 111785925 B CN111785925 B CN 111785925B
Authority
CN
China
Prior art keywords
pole piece
conductive
current collector
coating
active
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Active
Application number
CN202010802351.XA
Other languages
Chinese (zh)
Other versions
CN111785925A (en
Inventor
郑彦俊
暴旭
马华
何伟
从长杰
王驰伟
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Tianjin EV Energies Co Ltd
Original Assignee
Tianjin EV Energies Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Tianjin EV Energies Co Ltd filed Critical Tianjin EV Energies Co Ltd
Priority to CN202010802351.XA priority Critical patent/CN111785925B/en
Publication of CN111785925A publication Critical patent/CN111785925A/en
Application granted granted Critical
Publication of CN111785925B publication Critical patent/CN111785925B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Images

Classifications

    • 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
    • H01M10/00Secondary cells; Manufacture thereof
    • H01M10/05Accumulators with non-aqueous electrolyte
    • H01M10/052Li-accumulators
    • H01M10/0525Rocking-chair batteries, i.e. batteries with lithium insertion or intercalation in both electrodes; Lithium-ion batteries
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M10/00Secondary cells; Manufacture thereof
    • H01M10/05Accumulators with non-aqueous electrolyte
    • H01M10/058Construction or manufacture
    • H01M10/0585Construction or manufacture of accumulators having only flat construction elements, i.e. flat positive electrodes, flat negative electrodes and flat separators
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M10/00Secondary cells; Manufacture thereof
    • H01M10/05Accumulators with non-aqueous electrolyte
    • H01M10/058Construction or manufacture
    • H01M10/0587Construction or manufacture of accumulators having only wound construction elements, i.e. wound positive electrodes, wound negative electrodes and wound separators
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M10/00Secondary cells; Manufacture thereof
    • H01M10/42Methods or arrangements for servicing or maintenance of secondary cells or secondary half-cells
    • H01M10/4235Safety or regulating additives or arrangements in electrodes, separators or electrolyte
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M10/00Secondary cells; Manufacture thereof
    • H01M10/60Heating or cooling; Temperature control
    • H01M10/61Types of temperature control
    • H01M10/613Cooling or keeping cold
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M10/00Secondary cells; Manufacture thereof
    • H01M10/60Heating or cooling; Temperature control
    • H01M10/61Types of temperature control
    • H01M10/617Types of temperature control for achieving uniformity or desired distribution of temperature
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M10/00Secondary cells; Manufacture thereof
    • H01M10/60Heating or cooling; Temperature control
    • H01M10/65Means for temperature control structurally associated with the cells
    • H01M10/653Means for temperature control structurally associated with the cells characterised by electrically insulating or thermally conductive materials
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M10/00Secondary cells; Manufacture thereof
    • H01M10/60Heating or cooling; Temperature control
    • H01M10/65Means for temperature control structurally associated with the cells
    • H01M10/654Means for temperature control structurally associated with the cells located inside the innermost case of the cells, e.g. mandrels, electrodes or electrolytes
    • 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
    • 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
    • H01M4/1397Processes of manufacture of electrodes 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
    • H01M4/36Selection of substances as active materials, active masses, active liquids
    • H01M4/48Selection of substances as active materials, active masses, active liquids of inorganic oxides or hydroxides
    • H01M4/50Selection of substances as active materials, active masses, active liquids of inorganic oxides or hydroxides of manganese
    • H01M4/505Selection of substances as active materials, active masses, active liquids of inorganic oxides or hydroxides of manganese of mixed oxides or hydroxides containing manganese for inserting or intercalating light metals, e.g. LiMn2O4 or LiMn2OxFy
    • 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
    • H01M4/36Selection of substances as active materials, active masses, active liquids
    • H01M4/58Selection 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
    • H01M4/5825Oxygenated metallic salts or polyanionic structures, e.g. borates, phosphates, silicates, olivines
    • 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
    • H01M4/62Selection of inactive substances as ingredients for active masses, e.g. binders, fillers
    • H01M4/624Electric conductive fillers
    • H01M4/625Carbon or graphite
    • 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
    • H01M2004/026Electrodes composed of, or comprising, active material characterised by the polarity
    • H01M2004/028Positive electrodes
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M2220/00Batteries for particular applications
    • H01M2220/20Batteries in motive systems, e.g. vehicle, ship, plane
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M2220/00Batteries for particular applications
    • H01M2220/30Batteries in portable systems, e.g. mobile phone, laptop
    • 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
    • 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
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P70/00Climate change mitigation technologies in the production process for final industrial or consumer products
    • Y02P70/50Manufacturing or production processes characterised by the final manufactured product

Landscapes

  • 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)
  • Crystallography & Structural Chemistry (AREA)
  • Battery Electrode And Active Subsutance (AREA)
  • Secondary Cells (AREA)

Abstract

The invention provides a pole piece and application thereof, and a low-temperature-rise high-safety lithium ion battery containing the pole piece, wherein the pole piece comprises a current collector, and at least two layers of active coatings and at least one layer of high-efficiency conductive PTC film are fixedly arranged on two opposite surfaces of the current collector; the active coating and the high-efficiency conductive PTC film are arranged at intervals from the surface of the current collector from inside to outside, and the outermost side is the active coating; the conductivity of the active coating of the outermost layer is smaller than that of the other active coatings, and/or the active material of the active coating of the outermost layer adopts active material with high thermal stability. The pole piece disclosed by the invention has the advantages that the internal temperature distribution is more uniform, the temperature rise of the battery in normal use or internal short circuit is reduced, and the thermal runaway can be slowed down, so that the safety of the lithium ion battery is improved.

Description

极片及应用、含有该极片的低温升高安全性锂离子电池Pole piece and application, low-temperature elevated safety lithium-ion battery containing the pole piece

技术领域technical field

本发明属于锂离子电池领域,尤其是涉及一种极片及应用、含有该极片的低温升高安全性锂离子电池。The invention belongs to the field of lithium-ion batteries, and in particular relates to a pole piece and its application, and a low-temperature rising safe lithium-ion battery containing the pole piece.

背景技术Background technique

随着科学技术的不断进步,锂离子电池逐渐应用到很多领域,从便携式的电子产品到电动汽车、储能电源、航空领域等。但锂离子电池也存在不容忽视的安全风险。据报道,有多起手机因锂离子电池不良发生燃烧爆炸的事故,涉及三星、苹果等知名公司,有些事件导致了产品的召回;锂离子电池电动汽车发生燃烧爆炸的事例也有很多报道,涉及包括比亚迪、蔚来、特斯拉等知名电动车企。锂离子电池面对的最主要和最严重的安全风险是热失控。热失控的触发和扩散与内短路密切相关,如果内短路电流大则短路点温升高而引起热失控;在其他引发热失控的原因中,内短路也是一个关键助长因素,比如当过充引发热失控,出发的初期温度升高,一旦到达隔膜破坏温度,则会产生内短路,一旦发生内短路,电能则可能在内短路点附近快速释放,产生的热量会促使电池隔膜加速收缩融化,隔膜的融化破坏进一步加大了短路面积降低了短路点的电阻,从而加速电能的释放,加剧热失控。内短路发生的情形可以分为2种,一种情形是锂离子电池遭遇外界强烈的滥用,如严重过充、强烈震动撞击、严重挤压变形、火烧、或被异物刺穿;另一种情形是电池在正常的工作循环中,相对温和的使用条件下,由于锂枝晶、铁的沉积、金属毛刺、循环应力造成的集流体开裂等原因,在温度与压力的扰动作用下,产生接触点面积很小的微短路内短路当然需要尽可能避免。公知的技术通过降低隔膜的热收缩率、严格控制工艺避免金属毛刺的产生、确保负极足量并在低温时降低充电倍率以避免锂枝晶的产生等方式来降低产生内短路的概率。为了避免在高温下电池隔膜的热收缩导致的内短路,公知的技术是在在隔膜和电极之间制作一层耐热的陶瓷粉层来提高电池的高温安全性。常用的方式是将陶瓷粉末通过涂布的方式附着在隔膜的两边,这样处理过的隔膜被称为陶瓷涂布隔膜或CCM(CeramicCoatedMembrane)。With the continuous advancement of science and technology, lithium-ion batteries are gradually applied to many fields, from portable electronic products to electric vehicles, energy storage power supplies, aviation fields, etc. But lithium-ion batteries also have safety risks that cannot be ignored. According to reports, there have been many accidents of mobile phones burning and exploding due to bad lithium-ion batteries, involving well-known companies such as Samsung and Apple, and some incidents have led to product recalls; Well-known electric car companies such as BYD, NIO, and Tesla. The primary and most serious safety risk faced by Li-ion batteries is thermal runaway. The trigger and spread of thermal runaway are closely related to internal short circuit. If the internal short circuit current is large, the temperature of the short circuit point will rise and cause thermal runaway; among other causes of thermal runaway, internal short circuit is also a key contributing factor, such as when overcharging causes Thermal runaway, the initial temperature rises, and once it reaches the diaphragm destruction temperature, an internal short circuit will occur. Once an internal short circuit occurs, the electric energy may be released quickly near the internal short circuit point, and the heat generated will accelerate the shrinkage and melting of the battery diaphragm. The melting damage further increases the short-circuit area and reduces the resistance of the short-circuit point, thus accelerating the release of electric energy and exacerbating thermal runaway. The occurrence of internal short circuit can be divided into two types. One is that the lithium-ion battery is subjected to strong external abuse, such as severe overcharge, strong vibration, severe extrusion deformation, fire, or pierced by foreign objects; the other is In the normal working cycle of the battery, under relatively mild conditions of use, due to lithium dendrites, iron deposition, metal burrs, and current collector cracking caused by cyclic stress, contact points are generated under the disturbance of temperature and pressure. Micro-short-circuit internal short-circuits with a small area must of course be avoided as much as possible. Known technologies reduce the probability of internal short circuits by reducing the thermal shrinkage rate of the separator, strictly controlling the process to avoid the generation of metal burrs, ensuring sufficient negative electrodes, and reducing the charging rate at low temperatures to avoid the generation of lithium dendrites. In order to avoid the internal short circuit caused by the heat shrinkage of the battery separator at high temperature, a known technology is to make a heat-resistant ceramic powder layer between the separator and the electrodes to improve the high temperature safety of the battery. A commonly used method is to attach ceramic powder to both sides of the diaphragm by coating, and the diaphragm treated in this way is called a ceramic coated diaphragm or CCM (Ceramic Coated Membrane).

尽管采用了上述公知的技术,目前的技术水平尚无法将内短路和热失控发生的概率降低到一个可以忽略的水平以下。内短路尤其是微短路发生后,并非必然导致热失控,非热失控型的内短路在宏观上表现为电池的自放电率上升,在电池组中,体现为电池单体之间的不平衡加剧。内短路如果不能避免,我们则希望它体现为温和的自放电率上升,而不是热失控。如果在给定的内短路情形下,能够降低内短路的电流,则可避免或减小热失控的风险。Although the above-mentioned known technologies are adopted, the current technical level is still unable to reduce the probability of internal short circuit and thermal runaway to a negligible level. The internal short circuit, especially the micro short circuit, does not necessarily lead to thermal runaway. The non-thermal runaway internal short circuit is manifested as an increase in the self-discharge rate of the battery macroscopically. In the battery pack, it is reflected in the imbalance between the battery cells. . If the internal short circuit cannot be avoided, we hope that it will be manifested as a mild self-discharge rate increase rather than thermal runaway. If the current of the internal short circuit can be reduced under a given internal short circuit situation, the risk of thermal runaway can be avoided or reduced.

发明内容Contents of the invention

有鉴于此,本发明旨在提出一种极片,以克服现有技术的缺陷,内部温度分布更均匀、电池常规使用或内短路的温升降低,可减缓热失控从而提高锂离子电池的安全性。In view of this, the present invention aims to propose a pole piece to overcome the defects of the prior art. The internal temperature distribution is more uniform, the temperature rise of the battery is reduced in conventional use or internal short circuit, and the thermal runaway can be slowed down to improve the safety of lithium-ion batteries. sex.

为达到上述目的,本发明的技术方案是这样实现的:In order to achieve the above object, technical solution of the present invention is achieved in that way:

一种极片,包括集流体,所述集流体相对的两个表面均固定设置有至少两层活性涂层和至少一层高效导电PTC膜;活性涂层和高效导电PTC膜自集流体表面开始由内至外间隔设置,且最外面一侧为活性涂层;最外层的活性涂层的导电率小于其余各层活性涂层的导电率,和/或,最外层的活性涂层的活性物质采用热稳定性高的活性物质。A pole piece, comprising a current collector, at least two layers of active coatings and at least one layer of high-efficiency conductive PTC film are fixedly arranged on the opposite surfaces of the current collector; the active coating and the high-efficiency conductive PTC film start from the surface of the current collector It is arranged at intervals from the inside to the outside, and the outermost side is an active coating; the conductivity of the outermost active coating is smaller than that of the remaining active coatings, and/or, the outermost active coating has a As the active material, an active material with high thermal stability is used.

进一步的,所有高效导电PTC膜的末端均与集流体表面粘接。Further, the ends of all high-efficiency conductive PTC films are bonded to the surface of the current collector.

进一步的,所有高效导电PTC膜的厚度均为0.1~5μm。Further, the thickness of all high-efficiency conductive PTC films is 0.1-5 μm.

进一步的,集流体为铝箔。Further, the current collector is aluminum foil.

进一步的,高效导电PTC膜为第一导电剂、聚合物的混合物涂层;Further, the high-efficiency conductive PTC film is a mixture coating of the first conductive agent and polymer;

优选的,第一导电剂为具有离域大π键特征的导电无机物或导电聚合物。Preferably, the first conductive agent is a conductive inorganic material or a conductive polymer with the characteristics of delocalized large π bonds.

更优选的,第一导电剂为碳纳米管、石墨烯、导电石墨、导电炭黑、聚乙炔、聚苯胺、聚苯撑、聚苯撑乙烯、聚双炔、聚二苯胺及其衍生物、聚三苯胺及其衍生物、聚吡咯及其衍生物、聚噻吩及其衍生物、聚芴及其衍生物、聚对苯中的一种或几种。More preferably, the first conductive agent is carbon nanotubes, graphene, conductive graphite, conductive carbon black, polyacetylene, polyaniline, polyphenylene, polyphenylene vinylene, polydiyne, polydianiline and derivatives thereof, One or more of polytriphenylamine and its derivatives, polypyrrole and its derivatives, polythiophene and its derivatives, polyfluorene and its derivatives, polyparaphenylene.

优选的,聚合物为聚苯胺改性聚乙烯蜡、聚乙烯-醋酸乙烯酯、聚四氟乙烯、聚苯乙烯、聚烯烃、聚氯乙烯、环氧树脂中的一种或几种。Preferably, the polymer is one or more of polyaniline-modified polyethylene wax, polyethylene-vinyl acetate, polytetrafluoroethylene, polystyrene, polyolefin, polyvinyl chloride, and epoxy resin.

进一步的,高效导电PTC膜的组成中还包括第一粘结剂,第一导电剂、聚合物和第一粘结剂三者的重量比为(95-40):(5-55):(0.01-5)。Further, the composition of the high-efficiency conductive PTC film also includes the first binder, and the weight ratio of the first conductive agent, the polymer and the first binder is (95-40):(5-55):( 0.01-5).

进一步的,所有高效导电PTC膜和最外层的活性涂层的形成方式为凹版印刷、丝网印刷、挤压涂布、化学气相沉积、磁控溅射中的一种。Further, all highly efficient conductive PTC films and the outermost active coating are formed by one of gravure printing, screen printing, extrusion coating, chemical vapor deposition, and magnetron sputtering.

进一步的,所有活性涂层均为活性物质、第二导电剂和第二粘结剂的混合物涂层。Further, all the active coatings are mixture coatings of the active material, the second conductive agent and the second binder.

优选的,所述活性物质为镍钴锰酸锂、钴酸锂、锰酸锂、磷酸铁锂、磷酸锰锂中的一种或几种。Preferably, the active material is one or more of nickel-cobalt lithium manganese oxide, lithium cobalt oxide, lithium manganate, lithium iron phosphate, and lithium manganese phosphate.

优选的,第二导电剂为导电炭黑、碳纳米管、石墨烯中的一种或几种。Preferably, the second conductive agent is one or more of conductive carbon black, carbon nanotubes, and graphene.

优选的,第二粘结剂为聚四氟乙烯、聚酰亚胺、聚丙酸、聚丙烯腈中的一种或几种。Preferably, the second binder is one or more of polytetrafluoroethylene, polyimide, polypropionic acid, and polyacrylonitrile.

优选的,最外层的活性涂层中导电剂的含量小于其余各层活性涂层中导电剂的含量。Preferably, the content of the conductive agent in the outermost active coating layer is less than the content of the conductive agent in the active coating layers of the remaining layers.

优选的,热稳定性高的活性物质为磷酸铁锂及其衍生物、锰酸锂中的一种或几种。Preferably, the active material with high thermal stability is one or more of lithium iron phosphate and its derivatives, and lithium manganate.

本发明还涉及所述的极片作为正极极片在电池中的应用。The present invention also relates to the application of the pole piece as the positive pole piece in batteries.

本发明的另一目的在于提出一种低温升高安全性锂离子电池,以应用上述极片,具有低温升、高安全性的特性。Another object of the present invention is to propose a low-temperature rise safety lithium-ion battery, which has the characteristics of low temperature rise and high safety, using the above-mentioned pole piece.

为达到上述目的,本发明的技术方案是这样实现的:In order to achieve the above object, technical solution of the present invention is achieved in that way:

一种低温升高安全性锂离子电池,包括正极极片、隔膜和负极极片,所述正极极片为如上所述的极片。A lithium-ion battery with elevated safety at low temperature comprises a positive pole piece, a diaphragm and a negative pole piece, and the positive pole piece is the above pole piece.

相对于现有技术,本发明所述的极片具有以下优势:Compared with the prior art, the pole piece of the present invention has the following advantages:

本发明所述的极片,其内部温度分布更均匀、电池常规使用或内短路的温升降低,减缓热失控从而提高锂离子电池的安全性(现有常规电芯不具备以上技术优势,在发生内短时更容易出现热失控)。具体来说,本发明的优势体现在:The pole piece of the present invention has a more uniform internal temperature distribution, lowers the temperature rise of the battery in conventional use or internal short circuit, and slows down thermal runaway so as to improve the safety of lithium-ion batteries (the existing conventional batteries do not have the above technical advantages. more prone to thermal runaway when internal short-circuits occur). Specifically, the advantages of the present invention are reflected in:

(1)高效导电PTC膜的存在一方面可以使涂层内部导电膜附近内的电流密度分布更均匀,减小不均匀极化和不均匀发热,另一方面当内部温度升高超过PTC材料阈值温度时,其电阻迅速增大而减弱电子传输。(1) The existence of highly efficient conductive PTC film can make the current density distribution in the vicinity of the conductive film inside the coating more uniform on the one hand, reduce uneven polarization and uneven heating, on the other hand, when the internal temperature rises beyond the threshold of the PTC material When the temperature is high, its resistance increases rapidly and the electron transport is weakened.

(2)各层高效导电PTC膜与集流体粘接并联,可减小涂层垂直于集流体方向的欧姆极化,不但可以传导电流而且可以传导热量,内部温度升高可以传输部分热量到极耳处。(2) Each layer of high-efficiency conductive PTC film is bonded in parallel with the current collector, which can reduce the ohmic polarization of the coating perpendicular to the direction of the current collector. It can not only conduct current but also conduct heat. The increase in internal temperature can transfer part of the heat to the pole. ear.

(3)最外层涂层降低电导率或/且使用热稳定性高的活性材料,发生内短路时一方面可以减小短路电流而降低产热,另一方面热稳定性高的活性物质可以吸收更多的热量减缓热失控。(3) The outermost coating reduces the electrical conductivity or/and uses an active material with high thermal stability. When an internal short circuit occurs, it can reduce the short-circuit current and reduce heat generation on the one hand. On the other hand, the active material with high thermal stability can Absorb more heat to slow down thermal runaway.

(4)可显著降低锂离子电池充放电温升和内短路温升(在后续实施例中,使用该发明的电芯在倍率放电温升及其均匀性均好于对比例,针刺测试(内短路模型)的温升也低于对比例)。(4) It can significantly reduce the temperature rise of lithium-ion battery charge and discharge and the temperature rise of internal short circuit (in the following examples, the electric core using the invention is better than the comparison example in the rate discharge temperature rise and its uniformity, and the acupuncture test ( The temperature rise of the internal short circuit model) is also lower than that of the comparative example).

所述低温升高安全性锂离子电池与上述极片相对于现有技术所具有的优势相同,在此不再赘述。The low-temperature elevated safety lithium-ion battery has the same advantages as the above-mentioned pole piece over the prior art, and will not be repeated here.

附图说明Description of drawings

图1为实施例1正极极片的结构示意图;Fig. 1 is the structural representation of embodiment 1 positive pole piece;

图2为实施例2正极极片的结构示意图;Fig. 2 is the schematic structural representation of embodiment 2 positive pole piece;

图3为实施例3正极极片的结构示意图;Fig. 3 is the schematic structural representation of embodiment 3 positive pole piece;

图4为对比例2正极极片的结构示意图;Fig. 4 is the structural schematic diagram of comparative example 2 positive electrode sheet;

图5为实施例1电芯局部结构示意图;Fig. 5 is a schematic diagram of the local structure of the battery cell in embodiment 1;

图6为实施例2电芯局部结构示意图;Fig. 6 is a schematic diagram of the local structure of the cell in Embodiment 2;

图7为实施例3电芯局部结构示意图;Fig. 7 is a schematic diagram of the local structure of the battery cell in embodiment 3;

图8为对比例1、对比例3电芯局部结构示意图;Fig. 8 is a schematic diagram of the local structure of the cells of Comparative Example 1 and Comparative Example 3;

图9为对比例2电芯局部结构示意图。FIG. 9 is a schematic diagram of a partial structure of a cell in Comparative Example 2. FIG.

附图标记:Reference signs:

1-第一集流体;2-第一活性涂层;3-第一高效导电PTC膜;4-第二活性涂层;5-第二高效导电PTC膜;6-第三活性涂层;7-第三高效导电PTC膜;8-第四活性涂层;9-正极极片;10-负极极片;11-隔膜;12-第二集流体;13-负极浆料涂层;14-正极浆料涂层。1-the first current collector; 2-the first active coating; 3-the first high-efficiency conductive PTC film; 4-the second active coating; 5-the second high-efficiency conductive PTC film; 6-the third active coating; 7 -The third high-efficiency conductive PTC film; 8-the fourth active coating; 9-positive pole piece; 10-negative pole piece; 11-diaphragm; 12-second current collector; 13-negative slurry coating; 14-positive pole Slurry coating.

具体实施方式Detailed ways

除有定义外,以下实施例中所用的技术术语具有与本发明所属领域技术人员普遍理解的相同含义。以下实施例中所用的试验试剂,如无特殊说明,均为常规化学试剂;所述实验方法,如无特殊说明,均为常规方法。Unless otherwise defined, the technical terms used in the following embodiments have the same meaning as commonly understood by those skilled in the art to which the present invention belongs. The test reagents used in the following examples are conventional chemical reagents unless otherwise specified; the experimental methods are conventional methods unless otherwise specified.

名词解释:PTC材料为电阻率随温度升高而升高的材料。Explanation of terms: PTC material is a material whose resistivity increases with temperature.

一种极片,包括集流体,所述集流体相对的两个表面均固定设置有至少两层活性涂层和至少一层高效导电PTC膜;活性涂层和高效导电PTC膜自集流体表面开始由内至外间隔设置,且最外面一侧为活性涂层。其中,集流体可以采用铝箔。A pole piece, comprising a current collector, at least two layers of active coatings and at least one layer of high-efficiency conductive PTC film are fixedly arranged on the opposite surfaces of the current collector; the active coating and the high-efficiency conductive PTC film start from the surface of the current collector It is arranged at intervals from the inside to the outside, and the outermost side is an active coating. Wherein, aluminum foil can be used as the current collector.

其中,所有高效导电PTC膜的末端均与集流体表面粘接并联,不但可以传导电流而且可以传导热量,内部温度升高可以传输部分热量到极耳处。Among them, the ends of all high-efficiency conductive PTC films are bonded in parallel with the surface of the current collector, which can not only conduct current but also conduct heat, and the internal temperature rise can transfer part of the heat to the tab.

其中,所有高效导电PTC膜的厚度均为0.1~5μm。Wherein, the thickness of all highly efficient conductive PTC films is 0.1-5 μm.

其中,高效导电PTC膜为第一导电剂、聚合物的混合物涂层,其中第一导电剂与聚合物的重量比为(95-50):(5-50)。优选的,第一导电剂不限于具有离域大π键特征的导电无机物或导电聚合物,其中导电无机物不限于碳纳米管、石墨烯、导电石墨、导电炭黑等中的一种或几种的组合,导电聚合物不限于聚乙炔、聚苯胺、聚苯撑、聚苯撑乙烯、聚双炔、聚二苯胺及其衍生物、聚三苯胺及其衍生物、聚吡咯及其衍生物、聚噻吩及其衍生物、聚芴及其衍生物、聚对苯中的一种或几种的组合。优选的,聚合物材料不限于聚苯胺改性聚乙烯蜡(PANI-PEW)、聚乙烯-醋酸乙烯酯(EVA)、聚四氟乙烯(PTFE)、聚苯乙烯、聚烯烃、聚氯乙烯、环氧树脂一种或几种组合。根据需要,比如说在第一导电剂中导电剂不具有粘接性时,高效导电PTC膜的组成中还包括第一粘结剂,此时第一导电剂、聚合物和第一粘结剂三者的重量比为(95-40):(5-55):(0.01-5)。Wherein, the high-efficiency conductive PTC film is a mixture coating of the first conductive agent and polymer, wherein the weight ratio of the first conductive agent to the polymer is (95-50):(5-50). Preferably, the first conductive agent is not limited to conductive inorganic substances or conductive polymers with delocalized large π bond characteristics, wherein the conductive inorganic substances are not limited to one or the other of carbon nanotubes, graphene, conductive graphite, conductive carbon black, etc. A combination of several, conductive polymers are not limited to polyacetylene, polyaniline, polyphenylene, polyphenylene vinylene, polydiyne, polydiphenylamine and its derivatives, polytriphenylamine and its derivatives, polypyrrole and its derivatives One or a combination of polythiophene and its derivatives, polyfluorene and its derivatives, and polyparaphenylene. Preferably, the polymer material is not limited to polyaniline-modified polyethylene wax (PANI-PEW), polyethylene-vinyl acetate (EVA), polytetrafluoroethylene (PTFE), polystyrene, polyolefin, polyvinyl chloride, One or several combinations of epoxy resins. According to needs, for example, when the conductive agent in the first conductive agent does not have adhesiveness, the composition of the high-efficiency conductive PTC film also includes the first binder. At this time, the first conductive agent, the polymer and the first binder The weight ratio of the three is (95-40):(5-55):(0.01-5).

本发明中,所有高效导电PTC膜和最外层的活性涂层的形成方式为凹版印刷、丝网印刷、挤压涂布、化学气相沉积、磁控溅射中的一种。In the present invention, all high-efficiency conductive PTC films and the outermost active coating are formed by one of gravure printing, screen printing, extrusion coating, chemical vapor deposition, and magnetron sputtering.

本发明中,所有活性涂层均为活性物质、第二导电剂和第二粘结剂的混合物涂层,如果是极片是正极极片,这里实质上是正极浆料的涂层。优选的,活性物质不限于镍钴锰酸锂、钴酸锂、锰酸锂、磷酸铁锂、磷酸锰锂等具有锂离子脱出功能的材料中的一种或几种的组合;第二导电剂不限于不限于导电炭黑、碳纳米管、石墨烯等具有高电子导电能力的材料中的一种或几种的组合;第二粘结剂不限于聚四氟乙烯、聚酰亚胺、聚丙酸、聚丙烯腈等具有粘接作用的高分子化合物中的一种或几种的组合。In the present invention, all active coatings are mixture coatings of active material, second conductive agent and second binder. If the pole piece is a positive pole piece, it is essentially a coating of positive electrode slurry. Preferably, the active material is not limited to one or a combination of materials with lithium ion extraction functions such as nickel-cobalt lithium manganese oxide, lithium cobalt oxide, lithium manganate, lithium iron phosphate, lithium manganese phosphate; the second conductive agent It is not limited to one or a combination of materials with high electronic conductivity such as conductive carbon black, carbon nanotubes, and graphene; the second binder is not limited to polytetrafluoroethylene, polyimide, polypropylene One or a combination of polymer compounds with adhesive properties such as acid and polyacrylonitrile.

本发明中,最外侧活性涂层降低导电率(优选的,降低配方中第二导电剂含量)或使用热稳定性高的活性物质,或两个因素同时使用,发生内短路时一方面可以减小短路电流而降低产热,另一方面热稳定性高的活性物质可以吸收更多的热量减缓热失控。其中,热稳定性高的活性物质不限于磷酸铁锂及其衍生物(如磷酸锰铁锂、磷酸钴铁锂、磷酸锰钴铁锂等)、锰酸锂等。In the present invention, the outermost active coating reduces the electrical conductivity (preferably, reducing the second conductive agent content in the formula) or uses an active material with high thermal stability, or uses both factors at the same time. When an internal short circuit occurs, on the one hand it can reduce Small short-circuit current reduces heat generation. On the other hand, active materials with high thermal stability can absorb more heat to slow down thermal runaway. Among them, the active material with high thermal stability is not limited to lithium iron phosphate and its derivatives (such as lithium manganese iron phosphate, lithium cobalt iron phosphate, lithium manganese cobalt iron phosphate, etc.), lithium manganate and the like.

本发明中的极片可用于电池生产,尤其是作为正极极片用于电池生产。The pole piece in the present invention can be used in battery production, especially as a positive pole piece for battery production.

一种低温升高安全性锂离子电池,包括正极极片、隔膜和负极极片,所述正极极片为如上所述的极片。负极极片可以是常规的负极极片,负极极片包括负极浆料和负极集流体,负极集流体可以采用铜箔,负极浆料由活性物质、导电剂和粘结剂组成。活性物质不限于石墨材料、硅基材料和钛酸锂等具有锂离子嵌入功能的材料;导电剂不限于不限于导电炭黑、碳纳米管、石墨烯等具有高电子导电能力的材料;粘结剂不限于羧甲基纤维素、丁苯橡胶、聚酰亚胺、聚丙酸、聚丙烯腈等具有粘接作用的高分子化合物。隔膜可以采用PE隔膜。A lithium-ion battery with elevated safety at low temperature comprises a positive pole piece, a diaphragm and a negative pole piece, and the positive pole piece is the above pole piece. The negative electrode sheet can be a conventional negative electrode sheet. The negative electrode sheet includes a negative electrode slurry and a negative electrode collector. The negative electrode collector can be made of copper foil. The negative electrode slurry is composed of an active material, a conductive agent and a binder. Active materials are not limited to graphite materials, silicon-based materials, lithium titanate and other materials with lithium ion intercalation functions; conductive agents are not limited to conductive carbon black, carbon nanotubes, graphene and other materials with high electronic conductivity; bonding The agent is not limited to carboxymethyl cellulose, styrene-butadiene rubber, polyimide, polypropionic acid, polyacrylonitrile and other polymer compounds with bonding effect. The diaphragm can use PE diaphragm.

下面结合实施例及附图来详细说明本发明。The present invention will be described in detail below in conjunction with the embodiments and accompanying drawings.

实施例1Example 1

如图1所示,极片,包括第一集流体1,第一集流体1上表面和下表面设有第一活性涂层2,第一活性涂层2外表面包覆有第一高效导电PTC膜3,第一高效导电PTC膜3远离第一集流体1一侧的表面上设有第二活性涂层4,第一高效导电PTC膜3末端均与集流体粘接固定。所述极片为正极极片。第一集流体1为铝箔集流体。As shown in Figure 1, the pole piece includes a first current collector 1, the upper surface and the lower surface of the first current collector 1 are provided with a first active coating 2, and the outer surface of the first active coating 2 is coated with a first high-efficiency conductive coating. PTC film 3, the surface of the first high-efficiency conductive PTC film 3 away from the first current collector 1 is provided with a second active coating 4, and the ends of the first high-efficiency conductive PTC film 3 are bonded and fixed to the current collector. The pole piece is a positive pole piece. The first current collector 1 is an aluminum foil current collector.

1)正极复合涂层极片(也即正极极片)的制作:1) Production of the positive electrode composite coating pole piece (that is, the positive pole piece):

a.将正极活性物质NCM622、导电剂1(SP)、导电剂2(CNTs)、粘结剂(PVDF)按重量比96:1:1:2,倒入N-甲基-2-吡咯烷酮,混合、搅拌均匀,制得固含量为75%的正极浆料A;a. Pour positive active material NCM622, conductive agent 1 (SP), conductive agent 2 (CNTs), and binder (PVDF) into N-methyl-2-pyrrolidone in a weight ratio of 96:1:1:2, Mix and stir evenly to prepare positive electrode slurry A with a solid content of 75%;

b.将正极活性物质NCM622、导电剂1(SP)、导电剂2(CNTs)、粘结剂(PVDF)按重量比97.5:0.3:0.2:2,倒入N-甲基-2-吡咯烷酮,混合、搅拌均匀,制得固含量为75%的正极浆料B;b. Pour positive electrode active material NCM622, conductive agent 1 (SP), conductive agent 2 (CNTs), and binder (PVDF) into N-methyl-2-pyrrolidone in a weight ratio of 97.5:0.3:0.2:2, Mix and stir evenly to prepare positive electrode slurry B with a solid content of 75%;

c.导电剂1(CNTs-碳纳米管)、导电剂2(GNs-石墨烯)、聚合物(聚苯胺改性聚乙烯蜡-PANI-PEW)、粘结剂(PVDF)按重量比42:42:15:1,倒入N-甲基-2-吡咯烷酮,混合、搅拌分散均匀,制得固含量为8.0%的高效导电PTC浆料C;c. Conductive agent 1 (CNTs-carbon nanotube), conductive agent 2 (GNs-graphene), polymer (polyaniline modified polyethylene wax-PANI-PEW), binder (PVDF) by weight ratio 42: 42:15:1, pour N-methyl-2-pyrrolidone, mix, stir and disperse evenly, and obtain a high-efficiency conductive PTC slurry C with a solid content of 8.0%;

d.将正极浆料A先涂覆在铝箔集流体(也即第一集流体1)的上表面和下表面上,干燥后涂层总负载量为30mg/cm2,形成第一活性涂层2,得到正极极片A;d. Coat the positive electrode slurry A on the upper and lower surfaces of the aluminum foil current collector (that is, the first current collector 1), and after drying, the total loading of the coating is 30 mg/cm 2 to form the first active coating 2. Obtain positive pole piece A;

d.将高效导电PTC浆料C通过凹版辊涂在正极极片A上第一活性涂层2的外表面上形成第一高效导电PTC膜3,控制第一高效导电PTC膜3的厚度在1μm~3μm,得到复合正极极片B;d. Coating the high-efficiency conductive PTC slurry C on the outer surface of the first active coating 2 on the positive electrode sheet A by gravure roller to form the first high-efficiency conductive PTC film 3, and control the thickness of the first high-efficiency conductive PTC film 3 at 1 μm ~3μm, to obtain the composite positive electrode piece B;

e.将正极浆料B涂覆到复合正极极片B的上表面和下表面上,干燥后涂层总负载量为40mg/cm2,形成第二活性涂层4,得到复合正极极片C;e. Coating the positive electrode slurry B on the upper surface and the lower surface of the composite positive electrode sheet B, the total loading of the coating after drying is 40 mg/cm 2 , forming the second active coating 4, and obtaining the composite positive electrode sheet C ;

f.将复合正极极片C碾压到厚度125μm,得目标正极极片9,结构如图1所示。f. Roll the composite positive electrode piece C to a thickness of 125 μm to obtain the target positive electrode piece 9 , the structure of which is shown in FIG. 1 .

2)负极常规极片(也即负极极片)制作:2) Production of negative conventional pole piece (that is, negative pole piece):

负极极片包括第二集流体12及涂覆在第二集流体12上表面和下表面上的负极浆料涂层13,其中第二集流体12为铜箔集流体。The negative electrode sheet includes a second current collector 12 and a negative electrode slurry coating 13 coated on the upper and lower surfaces of the second current collector 12 , wherein the second current collector 12 is a copper foil current collector.

a.将负极活性物质人造石墨、导电剂(SP)、增稠剂羧甲基纤维素钠(CMC)和粘结剂丁苯橡胶(SBR)按重量比94.5:1.5:1.5:2.5,加入水搅拌混合均匀,得到固含量为50%的负极浆料;a. Negative electrode active material artificial graphite, conductive agent (SP), thickener sodium carboxymethylcellulose (CMC) and binder styrene-butadiene rubber (SBR) in a weight ratio of 94.5:1.5:1.5:2.5, add water Stir and mix evenly to obtain a negative electrode slurry with a solid content of 50%;

b.将负极浆料涂覆在铜箔集流体(也即第二集流体12)的上表面和下表面上,干燥后涂层总负载量为24mg/cm2,形成负极浆料涂层13,得到负极极片10;b. Coating the negative electrode slurry on the upper and lower surfaces of the copper foil current collector (i.e. the second current collector 12), the total loading of the coating after drying is 24 mg/cm 2 to form the negative electrode slurry coating 13 , to obtain the negative electrode sheet 10;

c.碾压负极极片10厚度到155μm。c. Rolling the negative pole piece 10 to a thickness of 155 μm.

锂离子电池的制作:Lithium-ion battery production:

a.将上述工艺制得的正极极片9、负极极片10与PE隔膜(也即隔膜11)通过卷绕或者叠片方式制成电池芯,电芯局部结构如图5所示;a. The positive pole piece 9, the negative pole piece 10 and the PE diaphragm (that is, the diaphragm 11) prepared by the above process are made into a battery core by winding or laminating, and the local structure of the battery core is shown in Figure 5;

b.配置电解液:1mol/LLiPF6,溶剂质量配比为EC(碳酸乙烯酯):DMC(碳酸二甲酯):EMC(碳酸甲乙酯)=5:2:3,1wt%VC(碳酸亚乙烯酯),1wt%FEC(氟代碳酸乙烯酯),1wt%1,3-PS(1,3-丙烷磺内酯);b. configuration electrolyte: 1mol/LLiPF6, the solvent mass ratio is EC (ethylene carbonate): DMC (dimethyl carbonate): EMC (ethyl methyl carbonate) = 5: 2: 3, 1wt% VC (ethylene carbonate vinyl ester), 1wt% FEC (fluoroethylene carbonate), 1wt% 1,3-PS (1,3-propane sultone);

c.将上述电解液注入制好的电池芯中,静置、预充化成后,进行相关的安全性能测试。c. Inject the above-mentioned electrolyte into the prepared battery core, let it stand still, pre-charge and form, and conduct related safety performance tests.

实施例2Example 2

如图2所示,本实施例极片也是正极极片,该正极极片的结构与实施例1基本相同,不同之处在于:第二活性涂层4外表面包覆有第二高效导PTC膜5,第二高效导PTC膜5远离第一集流体1一侧表面设有第三活性涂层6,第二高效导PTC膜5的末端也均与第一集流体1粘接固定。As shown in Figure 2, the pole piece of this embodiment is also a positive pole piece, and the structure of the positive pole piece is basically the same as that of Example 1, except that the outer surface of the second active coating 4 is covered with a second high-efficiency conductive PTC The membrane 5 and the second high-efficiency conductive PTC film 5 are provided with a third active coating 6 on the surface away from the first current collector 1 , and the ends of the second high-efficiency conductive PTC film 5 are also bonded and fixed to the first current collector 1 .

1)正极复合涂层极片(也即正极极片)的制作(该实施例为强调降低导电剂含量的情形):1) Fabrication of the positive electrode composite coating pole piece (that is, the positive pole piece) (this embodiment emphasizes the situation of reducing the content of the conductive agent):

a.将正极活性物质NCM622、导电剂1(SP)、导电剂2(CNTs)、粘结剂(PVDF)按重量比96:1:1:2,倒入N-甲基-2-吡咯烷酮,混合、搅拌均匀,制得固含量为75%的正极浆料A;a. Pour positive active material NCM622, conductive agent 1 (SP), conductive agent 2 (CNTs), and binder (PVDF) into N-methyl-2-pyrrolidone in a weight ratio of 96:1:1:2, Mix and stir evenly to prepare positive electrode slurry A with a solid content of 75%;

b.将正极活性物质LiFePO4、导电剂1(SP)、导电剂2(CNTs)、粘结剂(PVDF)按重量比96.8:0.4:0.8:2,倒入N-甲基-2-吡咯烷酮,混合、搅拌均匀,制得固含量为65%的正极浆料B;b. Pour positive electrode active material LiFePO 4 , conductive agent 1 (SP), conductive agent 2 (CNTs), and binder (PVDF) in a weight ratio of 96.8:0.4:0.8:2 into N-methyl-2-pyrrolidone , mixed and stirred uniformly to prepare positive electrode slurry B with a solid content of 65%;

c.导电剂1(CNTs-碳纳米管)、导电剂2(GNs-石墨烯)、聚合物(EVA)、粘结剂(PVDF)按重量比43:43:9:5,倒入N-甲基-2-吡咯烷酮,混合、搅拌分散均匀,制得固含量为8.0%的高效导电PTC浆料C;c. Conductive agent 1 (CNTs-carbon nanotubes), conductive agent 2 (GNs-graphene), polymer (EVA), binder (PVDF) in a weight ratio of 43:43:9:5, pour N- Methyl-2-pyrrolidone, mixing, stirring and dispersing evenly to obtain a high-efficiency conductive PTC slurry C with a solid content of 8.0%;

d.将正极浆料A先涂覆在铝箔集流体(也即第一集流体1)的上表面和下表面上,干燥后涂层总负载量为15mg/cm2,形成第一活性涂层2,得到正极极片A;d. Coat the positive electrode slurry A on the upper and lower surfaces of the aluminum foil current collector (that is, the first current collector 1), and after drying, the total loading of the coating is 15 mg/cm 2 to form the first active coating 2. Obtain positive pole piece A;

e.将高效导电PTC浆料C通过凹版辊涂在正极极片A上第一活性涂层2的外表面上形成第一高效导电PTC膜3,控制第一高效导电PTC膜3的厚度在1μm~3μm,得到复合正极极片B;e. The high-efficiency conductive PTC slurry C is coated on the outer surface of the first active coating 2 on the positive electrode sheet A by a gravure roll to form the first high-efficiency conductive PTC film 3, and the thickness of the first high-efficiency conductive PTC film 3 is controlled at 1 μm ~3μm, to obtain the composite positive electrode piece B;

f.将正极浆料A涂覆在复合正极极片B的上表面和下表面上,干燥后涂层总负载量为36mg/cm2,形成第二活性涂层4,得到复合正极极片C;f. Coating the positive electrode slurry A on the upper surface and the lower surface of the composite positive electrode sheet B, the total loading of the coating after drying is 36 mg/cm 2 to form the second active coating 4, and obtain the composite positive electrode sheet C ;

g.将高效导电PTC浆料C通过凹版辊涂在正极极片C上第二活性涂层4的外表面上形成第二高效导电PTC膜5,控制第二高效导电PTC膜5的厚度在1μm~3μm,得到复合正极极片D;g. the high-efficiency conductive PTC slurry C is coated on the outer surface of the second active coating 4 on the positive pole piece C by gravure roll to form the second high-efficiency conductive PTC film 5, and the thickness of the second high-efficiency conductive PTC film 5 is controlled at 1 μm ~3μm, the composite positive electrode sheet D was obtained;

h.将正极浆料B涂覆到复合正极极片D的上表面和下表面上,干燥后涂层总负载量为42mg/cm2,形成第三活性涂层6,得到复合正极极片E;h. Coating the positive electrode slurry B on the upper surface and the lower surface of the composite positive electrode sheet D, after drying, the total loading of the coating is 42 mg/cm 2 to form the third active coating 6, and obtain the composite positive electrode sheet E ;

h.将复合正极极片E碾压到厚度127μm,得目标正极极片9,结构如图2所示。h. Roll the composite positive pole piece E to a thickness of 127 μm to obtain the target positive pole piece 9 , the structure of which is shown in FIG. 2 .

2)负极常规极片(也即负极极片)制作:2) Production of negative conventional pole piece (that is, negative pole piece):

本实施例的负极极片结构与实施例1的负极极片结构相同。其具体制备方法如下:The structure of the negative pole piece of this embodiment is the same as that of the negative pole piece of Embodiment 1. Its specific preparation method is as follows:

a.将负极活性物质人造石墨、导电剂(SP)、增稠剂羧甲基纤维素钠(CMC)和粘结剂丁苯橡胶(SBR)按重量比94.5:1.5:1.5:2.5,加入水搅拌混合均匀,得到固含量为50%的负极浆料;a. Negative electrode active material artificial graphite, conductive agent (SP), thickener sodium carboxymethylcellulose (CMC) and binder styrene-butadiene rubber (SBR) in a weight ratio of 94.5:1.5:1.5:2.5, add water Stir and mix evenly to obtain a negative electrode slurry with a solid content of 50%;

b.将负极浆料涂覆在铜箔集流体(也即第二集流体12)的上表面和下表面上,干燥后涂层总负载量为24mg/cm2,形成负极浆料涂层13,得到负极极片10;b. Coating the negative electrode slurry on the upper and lower surfaces of the copper foil current collector (i.e. the second current collector 12), the total loading of the coating after drying is 24 mg/cm 2 to form the negative electrode slurry coating 13 , to obtain the negative electrode sheet 10;

c.碾压负极极片10厚度到155μm。c. Rolling the negative pole piece 10 to a thickness of 155 μm.

锂离子电池的制作:Lithium-ion battery production:

a.将上述工艺制得的正极极片9、负极极片10与PE隔膜(也即隔膜11)通过卷绕或者叠片方式制成电池芯,电芯局部结构如图6所示;a. The positive pole piece 9, the negative pole piece 10 and the PE diaphragm (that is, the diaphragm 11) prepared by the above process are made into a battery core by winding or laminating, and the local structure of the battery core is shown in Figure 6;

b.配置电解液:1mol/LLiPF6,溶剂质量配比为EC:DMC:EMC=5:2:3,1wt%VC,1wt%FEC,1wt%1,3-PS;b. Configure the electrolyte: 1mol/LLiPF6, the solvent mass ratio is EC:DMC:EMC=5:2:3, 1wt% VC, 1wt% FEC, 1wt% 1,3-PS;

c.将上述电解液注入制好的电池芯中,静置、预充化成后,进行相关的安全性能测试。c. Inject the above-mentioned electrolyte into the prepared battery core, let it stand still, pre-charge and form, and conduct related safety performance tests.

对比例1Comparative example 1

正极极片,包括第一集流体1,第一集流体1上表面和下表面均设有正极浆料涂层14。第一集流体1为铝箔集流体。The positive electrode sheet includes a first current collector 1 , and the upper surface and the lower surface of the first current collector 1 are provided with a positive electrode slurry coating 14 . The first current collector 1 is an aluminum foil current collector.

1)正极极片的制作:1) Production of positive pole piece:

a.将正极活性物质NCM622、导电剂1(SP)、导电剂2(CNTs)、粘结剂(PVDF)按重量比96:1:1:2,倒入N-甲基-2-吡咯烷酮,混合、搅拌均匀,制得固含为75%的正极浆料;a. Pour positive active material NCM622, conductive agent 1 (SP), conductive agent 2 (CNTs), and binder (PVDF) into N-methyl-2-pyrrolidone in a weight ratio of 96:1:1:2, Mix and stir evenly to obtain a positive electrode slurry with a solid content of 75%;

b.将正极浆料涂覆在铝箔集流体的上表面和下表面上,干燥后涂层总负载量为40mg/cm2,形成正极浆料涂层14,得到正极极片9;b. Coating the positive electrode slurry on the upper surface and the lower surface of the aluminum foil current collector, the total loading of the coating after drying is 40 mg/cm 2 , forming the positive electrode slurry coating 14, and obtaining the positive electrode sheet 9;

c.碾压正极极片9厚度到125μm。c. Rolling the positive pole piece 9 to a thickness of 125 μm.

2)负极极片的制作:2) Production of negative pole piece:

负极极片10结构与实施例1的负极极片10结构相同。其具体制备方法如下:a.将负极活性物质人造石墨、导电剂(SP)、增稠剂羧甲基纤维素钠(CMC)和粘结剂丁苯橡胶(SBR)按重量比94.5:1.5:1.5:2.5,加入水搅拌混合均匀,得到固含量为50%的负极浆料;The structure of the negative electrode sheet 10 is the same as that of the negative electrode sheet 10 in the first embodiment. Its specific preparation method is as follows: a. Negative electrode active material artificial graphite, conductive agent (SP), thickener sodium carboxymethylcellulose (CMC) and binding agent styrene-butadiene rubber (SBR) are by weight 94.5:1.5: 1.5:2.5, add water and stir to mix evenly to obtain a negative electrode slurry with a solid content of 50%;

b.将负极浆料涂覆在铜箔集流体(也即第二集流体12)上,干燥后涂层总负载量为24mg/cm2,形成负极浆料涂层13,得到负极极片10;b. Coating the negative electrode slurry on the copper foil current collector (that is, the second current collector 12), the total loading of the coating after drying is 24 mg/cm 2 , forming the negative electrode slurry coating 13, and obtaining the negative electrode sheet 10 ;

c.碾压负极极片厚度到155μm。c. Roll the thickness of the negative pole piece to 155μm.

3)锂离子电池的制作:3) Production of lithium-ion batteries:

a.将上述工艺制得的正极极片9、负极极片10与PE隔膜(也即隔膜11)通过卷绕或者叠片方式制成电池芯,电芯局部结构如图8所示;a. The positive pole piece 9, the negative pole piece 10 and the PE diaphragm (that is, the diaphragm 11) prepared by the above process are made into a battery core by winding or laminating, and the local structure of the battery core is shown in Figure 8;

b.配置电解液:1mol/LLiPF6,溶剂质量配比为EC:DMC:EMC=5:2:3,1wt%VC,1wt%FEC,1wt%1,3-PS;b. Configure the electrolyte: 1mol/LLiPF6, the solvent mass ratio is EC:DMC:EMC=5:2:3, 1wt% VC, 1wt% FEC, 1wt% 1,3-PS;

c.将上述电解液注入制好的电池芯中,静置、预充化成后,进行相关的性能测试。c. Inject the above-mentioned electrolyte into the prepared battery core, let it stand still, pre-charge and form, and then conduct relevant performance tests.

对比例2Comparative example 2

本对比例的正极极片和负极极片的结构如下:The structures of the positive pole piece and the negative pole piece of this comparative example are as follows:

如图图4所示,正极极片,包括第一集流体1,第一集流体1为铝箔,第一集流体1上表面和下表面均设有第一高效导电PTC膜3,第一高效导电PTC膜3远离第一集流体1一侧表面均设有第一活性涂层2。第一集流体1和其两侧的第一高效导电PTC膜3构成底涂集流体。As shown in Figure 4, the positive electrode sheet includes a first current collector 1, the first current collector 1 is aluminum foil, and the first high-efficiency conductive PTC film 3 is provided on the upper and lower surfaces of the first current collector 1, and the first high-efficiency The surface of the conductive PTC film 3 away from the first current collector 1 is provided with a first active coating 2 . The first current collector 1 and the first high-efficiency conductive PTC film 3 on both sides thereof constitute an undercoated current collector.

负极极片结构与实施例1负极极片结构相同。The structure of the negative pole piece is the same as that of the negative pole piece in Example 1.

具体正极极片和负极极片的制备方法如下:The preparation method of concrete positive pole piece and negative pole piece is as follows:

1)正极极片的制作:1) Production of positive pole piece:

a.将正极活性物质NCM622、导电剂1(SP)、导电剂2(CNTs)、粘结剂(PVDF)按重量比96:1:1:2,倒入N-甲基-2-吡咯烷酮,混合、搅拌均匀,制得固含量为75%的正极浆料;a. Pour positive active material NCM622, conductive agent 1 (SP), conductive agent 2 (CNTs), and binder (PVDF) into N-methyl-2-pyrrolidone in a weight ratio of 96:1:1:2, Mix and stir evenly to prepare positive electrode slurry with a solid content of 75%;

b.导电剂1(CNTs-碳纳米管)、导电剂2(GNs-石墨烯)、聚合物(聚苯胺改性聚乙烯蜡-PANI-PEW)、粘结剂(PVDF)按重量比42:42:15:1,倒入N-甲基-2-吡咯烷酮,混合、搅拌分散均匀,制得固含量为8.0%的高效导电PTC浆料;b. Conductive agent 1 (CNTs-carbon nanotube), conductive agent 2 (GNs-graphene), polymer (polyaniline modified polyethylene wax-PANI-PEW), binder (PVDF) by weight ratio 42: 42:15:1, pour N-methyl-2-pyrrolidone, mix, stir and disperse evenly, and obtain a high-efficiency conductive PTC slurry with a solid content of 8.0%;

c.将高效导电PTC浆料通过凹版辊涂在铝箔(也即第一集流体1)的上表面和下表面上形成第一高效导电PTC膜3,控制第一高效导电PTC膜3的厚度在1μm~3μm,得到底涂集流体;c. The high-efficiency conductive PTC slurry is coated on the upper surface and the lower surface of the aluminum foil (that is, the first current collector 1) by a gravure roll to form the first high-efficiency conductive PTC film 3, and the thickness of the first high-efficiency conductive PTC film 3 is controlled at 1 μm ~ 3 μm, to obtain the undercoat current collector;

d.将正极浆料涂覆在底涂集流体上,干燥后涂层总负载量为40mg/cm2,形成第一活性涂层2,得到复合正极极片;d. Coating the positive electrode slurry on the base coating current collector, the total loading of the coating after drying is 40 mg/cm 2 , forming the first active coating layer 2, and obtaining the composite positive electrode sheet;

e.将复合正极极片碾压到厚度125μm,即得本对比例的正极极片9,结构如图4所示。e. Roll the composite positive electrode sheet to a thickness of 125 μm to obtain the positive electrode sheet 9 of this comparative example, the structure of which is shown in FIG. 4 .

2)负极常规极片(也即负极极片)制作:2) Production of negative conventional pole piece (that is, negative pole piece):

a.将负极活性物质人造石墨、导电剂(SP)、增稠剂羧甲基纤维素钠(CMC)和粘结剂丁苯橡胶(SBR)按重量比94.5:1.5:1.5:2.5,加入水搅拌混合均匀,得到固含量为50%的负极浆料;a. Negative electrode active material artificial graphite, conductive agent (SP), thickener sodium carboxymethylcellulose (CMC) and binder styrene-butadiene rubber (SBR) in a weight ratio of 94.5:1.5:1.5:2.5, add water Stir and mix evenly to obtain a negative electrode slurry with a solid content of 50%;

b.将负极浆料涂覆在铜箔集流体上,干燥后涂层总负载量为24mg/cm2,形成负极浆料涂层13,得到负极极片10;b. Coating the negative electrode slurry on the copper foil current collector, the total loading capacity of the coating after drying is 24mg/cm 2 , forming the negative electrode slurry coating 13, and obtaining the negative electrode sheet 10;

c.碾压负极极片10厚度到155μm。c. Rolling the negative pole piece 10 to a thickness of 155 μm.

锂离子电池的制作:Lithium-ion battery production:

a.将上述工艺制得的正极极片9、负极极片10与PE隔膜(也即隔膜11)通过卷绕或者叠片方式制成电池芯,电芯局部结构如图9所示;a. The positive pole piece 9, the negative pole piece 10 and the PE diaphragm (that is, the diaphragm 11) prepared by the above process are made into a battery core by winding or laminating, and the local structure of the battery core is shown in Figure 9;

b.配置电解液:1mol/LLiPF6,溶剂质量配比为EC:DMC:EMC=5:2:3,1wt%VC,1wt%FEC,1wt%1,3-PS;b. Configure the electrolyte: 1mol/LLiPF6, the solvent mass ratio is EC:DMC:EMC=5:2:3, 1wt% VC, 1wt% FEC, 1wt% 1,3-PS;

c.将上述电解液注入制好的电池芯中,静置、预充化成后,进行相关的安全性能测试。c. Inject the above-mentioned electrolyte into the prepared battery core, let it stand still, pre-charge and form, and conduct related safety performance tests.

对实施例1、实施例2和对比例1、对比例2的电池在25℃温度条件下,分别进行6C/4C/2C/1C的倍率放电测试,并记录不同倍率的放电下温升和电芯表面温差(红外成像测温),记录结果如表1。The batteries of Example 1, Example 2 and Comparative Example 1 and Comparative Example 2 were subjected to 6C/4C/2C/1C rate discharge tests at a temperature of 25°C, and the temperature rise and battery life under different rate discharges were recorded. Core surface temperature difference (infrared imaging temperature measurement), the recorded results are shown in Table 1.

表1实施例1、实施例2、对比例1、对比例2电池倍率放电测试结果Table 1 Example 1, Example 2, Comparative Example 1, Comparative Example 2 battery rate discharge test results

Figure BDA0002627860350000141
Figure BDA0002627860350000141

Figure BDA0002627860350000151
Figure BDA0002627860350000151

从表1可以看出,实施例1和实施例2的倍率温升和温差明显低于对比例1和对比例2。同时,通过实施例1和对比例2比较,本发明将高效导电PTC膜放在极片内部并通过两端外漏与集流体链接,既可以传导电流,又可以将极片内部的热量及时传导到极耳散热;在集流体表面的高效导电PTC膜不能实现以上作用。It can be seen from Table 1 that the rate temperature rise and temperature difference of Example 1 and Example 2 are significantly lower than those of Comparative Example 1 and Comparative Example 2. At the same time, through the comparison of Example 1 and Comparative Example 2, the present invention puts the high-efficiency conductive PTC film inside the pole piece and connects it with the current collector through the leakage at both ends, which can not only conduct current, but also conduct heat inside the pole piece in time To dissipate heat from the tabs; the high-efficiency conductive PTC film on the surface of the current collector cannot achieve the above functions.

将实施例1、实施例2和对比例1、对比例2的100%SOC电池进行针刺实验,测试方法为:用一个直径为3mm的耐高温钢钉以80mm/s的速度垂直穿透电芯中心(钢针停留在电芯中300s),测试结果如表2:The 100% SOC batteries of Example 1, Example 2 and Comparative Example 1 and Comparative Example 2 were subjected to acupuncture experiments. The test method was: use a high-temperature-resistant steel nail with a diameter of 3 mm to vertically penetrate the battery at a speed of 80 mm/s. The center of the core (the steel needle stays in the battery for 300s), the test results are shown in Table 2:

表2实施例1、实施例2、对比例1、对比例2电池针刺实验测试结果Table 2 Example 1, Example 2, Comparative Example 1, Comparative Example 2 battery acupuncture test results

Figure BDA0002627860350000152
Figure BDA0002627860350000152

实施例1和实施例2均全部通过针刺测试,且温升较低;对比例1未通过针刺测试;对比例2有2/3通过针刺测试,但温升较高,如在模组内因散热效果差,热失控概率将大大增加。Embodiment 1 and embodiment 2 all pass acupuncture test, and temperature rise is lower; Comparative example 1 does not pass acupuncture test; Comparative example 2 has 2/3 to pass acupuncture test, but temperature rise is higher, as in mold Due to the poor heat dissipation effect in the group, the probability of thermal runaway will be greatly increased.

实施例3Example 3

如图3所示,本实施例极片也是正极极片,该正极极片的机构与实施例2基本相同,不同之处在于:第三活性涂层6外表面包覆有第三高效导电PTC膜7,第三高效导电PTC膜7远离第一集流体1一侧表面设有第四活性涂层8,第三高效导电PTC膜7的末端也均与第一集流体1粘接固定。As shown in Figure 3, the pole piece of this embodiment is also a positive pole piece, and the mechanism of the positive pole piece is basically the same as that of Example 2, except that the outer surface of the third active coating 6 is coated with a third highly efficient conductive PTC The film 7 and the third high-efficiency conductive PTC film 7 are provided with a fourth active coating 8 on the side away from the first current collector 1 , and the ends of the third high-efficiency conductive PTC film 7 are also bonded and fixed to the first current collector 1 .

1)正极复合涂层极片(也即正极极片)的制作:1) Production of the positive electrode composite coating pole piece (that is, the positive pole piece):

a.将正极活性物质NCM811、导电剂1(SP)、导电剂2(CNTs)、粘结剂(PVDF)按重量比96.9:0.8:0.8:1.5,倒入N-甲基-2-吡咯烷酮,混合、搅拌均匀,制得固含量为75%的正极浆料A;a. Pour positive active material NCM811, conductive agent 1 (SP), conductive agent 2 (CNTs), and binder (PVDF) into N-methyl-2-pyrrolidone in a weight ratio of 96.9:0.8:0.8:1.5, Mix and stir evenly to prepare positive electrode slurry A with a solid content of 75%;

b.将正极活性物质LMO、导电剂1(SP)、粘结剂(PVDF)按重量比97.0:1.0:2.0,倒入N-甲基-2-吡咯烷酮,混合、搅拌均匀,制得固含量为75%的正极浆料B;b. Pour positive electrode active material LMO, conductive agent 1 (SP), and binder (PVDF) into N-methyl-2-pyrrolidone in a weight ratio of 97.0:1.0:2.0, mix and stir evenly, and obtain a solid content 75% positive electrode slurry B;

c.导电剂1(CNTs-碳纳米管)、导电剂2(GNs-石墨烯)、聚合物(PTFE)按重量比46:46:8,倒入N-甲基-2-吡咯烷酮,混合、搅拌分散均匀,制得固含量为8.0%的高效导电PTC浆料C;c. Conductive agent 1 (CNTs-carbon nanotubes), conductive agent 2 (GNs-graphene), polymer (PTFE) in a weight ratio of 46:46:8, pour N-methyl-2-pyrrolidone, mix, Stir and disperse evenly to prepare a high-efficiency conductive PTC slurry C with a solid content of 8.0%;

d.将正极浆料A先涂覆在铝箔集流体(也即第一集流体1)的上表面和下表面上,干燥后涂层总负载量为9mg/cm2,形成第一活性涂层2,得到正极极片A;d. Coat the positive electrode slurry A on the upper and lower surfaces of the aluminum foil current collector (that is, the first current collector 1), and after drying, the total loading of the coating is 9 mg/cm 2 to form the first active coating 2. Obtain positive pole piece A;

e.将高效导电PTC浆料C通过凹版辊涂在正极极片A上第一活性涂层2的外表面上形成第一高效导电PTC膜3,控制第一高效导电PTC膜3的厚度在1μm~3μm,得到复合正极极片B;e. The high-efficiency conductive PTC slurry C is coated on the outer surface of the first active coating 2 on the positive electrode sheet A by a gravure roll to form the first high-efficiency conductive PTC film 3, and the thickness of the first high-efficiency conductive PTC film 3 is controlled at 1 μm ~3μm, to obtain the composite positive electrode piece B;

f.将正极浆料A涂覆在复合正极极片B的上表面和下表面上,干燥后涂层总负载量为18mg/cm2,形成第二活性涂层4,得到复合正极极片C;f. Coating the positive electrode slurry A on the upper surface and the lower surface of the composite positive electrode sheet B, the total loading of the coating after drying is 18 mg/cm 2 to form the second active coating 4, and obtain the composite positive electrode sheet C ;

g.将高效导电PTC浆料C通过凹版辊涂在正极极片C上第二活性涂层4的外表面上形成第二高效导电PTC膜5,控制第二高效导电PTC膜5的厚度在1μm~3μm,得到复合正极极片D;g. the high-efficiency conductive PTC slurry C is coated on the outer surface of the second active coating 4 on the positive pole piece C by gravure roll to form the second high-efficiency conductive PTC film 5, and the thickness of the second high-efficiency conductive PTC film 5 is controlled at 1 μm ~3μm, the composite positive electrode sheet D was obtained;

h.将正极浆料B涂覆到复合正极极片D的上表面和下表面上,干燥后涂层总负载量为27mg/cm2,形成第三活性涂层6,得到复合正极极片E;h. Coating the positive electrode slurry B on the upper surface and the lower surface of the composite positive electrode sheet D, after drying, the total loading of the coating is 27 mg/cm 2 to form the third active coating 6, and obtain the composite positive electrode sheet E ;

i.将高效导电PTC浆料C通过凹版辊涂在正极极片E上第三活性涂层6的外表面上形成第三高效导电PTC膜7,控制第三高效导电PTC膜7的厚度在1μm~3μm,得到复合正极极片F;i. The high-efficiency conductive PTC slurry C is coated on the outer surface of the third active coating 6 on the positive electrode sheet E by a gravure roll to form the third high-efficiency conductive PTC film 7, and the thickness of the third high-efficiency conductive PTC film 7 is controlled at 1 μm ~3μm, to obtain the composite positive electrode sheet F;

j.将正极浆料B涂覆到复合正极极片F的上表面和下表面上,干燥后涂层总负载量为36mg/cm2,形成第四活性涂层8,得到复合正极极片G;j. Coating the positive electrode slurry B on the upper surface and the lower surface of the composite positive electrode sheet F, the total loading of the coating after drying is 36 mg/cm 2 , forming the fourth active coating layer 8, and obtaining the composite positive electrode sheet G ;

k.将复合正极极片E碾压到厚度122μm,即得目标正极极片9,结构如图3所示。k. Roll the composite positive pole piece E to a thickness of 122 μm to obtain the target positive pole piece 9 , the structure of which is shown in FIG. 3 .

2)负极常规极片(也即负极极片)制作:2) Production of negative conventional pole piece (that is, negative pole piece):

a.将负极活性物质人造石墨、导电剂(SP)、增稠剂羧甲基纤维素钠(CMC)和粘结剂丁苯橡胶(SBR)按重量比95.5:1.0:1.3:2.2,加入水搅拌混合均匀,得到固含量为50%的负极浆料;a. Negative electrode active material artificial graphite, conductive agent (SP), thickener sodium carboxymethylcellulose (CMC) and binder styrene-butadiene rubber (SBR) in a weight ratio of 95.5:1.0:1.3:2.2, add water Stir and mix evenly to obtain a negative electrode slurry with a solid content of 50%;

b.将负极浆料涂覆在铜箔集流体(也即第二集流体12)上,干燥后涂层总负载量为22mg/cm2,形成负极浆料层,得到负极极片10;b. Coating the negative electrode slurry on the copper foil current collector (that is, the second current collector 12), the total loading of the coating after drying is 22 mg/cm 2 , forming a negative electrode slurry layer, and obtaining the negative electrode sheet 10;

c.碾压负极极片10厚度到145μm。c. Rolling the negative pole piece 10 to a thickness of 145 μm.

锂离子电池的制作:Lithium-ion battery production:

a.将上述工艺制得的正极极片9、负极极片10与PE隔膜(也即隔膜11)通过卷绕或者叠片方式制成电池芯,电芯局部结构如图7所示;a. The positive pole piece 9, the negative pole piece 10 and the PE diaphragm (that is, the diaphragm 11) prepared by the above process are made into a battery core by winding or stacking, and the local structure of the battery core is shown in Figure 7;

b.配置电解液:1mol/LLiPF6,溶剂质量配比为EC:DMC:EMC=5:2:3,1wt%VC,1wt%FEC,1wt%1,3-PS;b. Configure the electrolyte: 1mol/LLiPF6, the solvent mass ratio is EC:DMC:EMC=5:2:3, 1wt% VC, 1wt% FEC, 1wt% 1,3-PS;

c.将上述电解液注入制好的电池芯中,静置、预充化成后,进行相关的安全性能测试。c. Inject the above-mentioned electrolyte into the prepared battery core, let it stand still, pre-charge and form, and conduct related safety performance tests.

对比例3Comparative example 3

本对比例的正极极片和负极极片结构分别与对比例1的正极极片和负极极片结构相同,其具体制备方法如下:The structure of the positive pole piece and the negative pole piece of this comparative example is the same as that of the positive pole piece and the negative pole piece of Comparative Example 1 respectively, and its specific preparation method is as follows:

1)正极极片的制作:1) Production of positive pole piece:

a.将正极活性物质NCM622、导电剂1(SP)、导电剂2(CNTs)、粘结剂(PVDF)按重量比96.9:0.8:0.8:1.5,倒入N-甲基-2-吡咯烷酮,混合、搅拌均匀,制得固含量为75%的正极浆料;a. Pour positive electrode active material NCM622, conductive agent 1 (SP), conductive agent 2 (CNTs), and binder (PVDF) into N-methyl-2-pyrrolidone in a weight ratio of 96.9:0.8:0.8:1.5, Mix and stir evenly to prepare positive electrode slurry with a solid content of 75%;

b.将正极浆料涂覆在铝箔集流体(也即第一集流体1)上,干燥后涂层总负载量为36mg/cm2,形成正极浆料涂层14,得到正极极片9;b. Coating the positive electrode slurry on the aluminum foil current collector (that is, the first current collector 1), the total loading of the coating after drying is 36 mg/cm 2 , forming the positive electrode slurry coating 14, and obtaining the positive electrode sheet 9;

c.碾压正极极片9厚度到122μm。c. Rolling the positive pole piece 9 to a thickness of 122 μm.

2)负极极片的制作:2) Production of negative pole piece:

a.将负极活性物质人造石墨、导电剂(SP)、增稠剂羧甲基纤维素钠(CMC)和粘结剂丁苯橡胶(SBR)按重量比95.5:1.0:1.3:2.2,加入水搅拌混合均匀,得到固含量为50%的负极浆料;a. Negative electrode active material artificial graphite, conductive agent (SP), thickener sodium carboxymethylcellulose (CMC) and binder styrene-butadiene rubber (SBR) in a weight ratio of 95.5:1.0:1.3:2.2, add water Stir and mix evenly to obtain a negative electrode slurry with a solid content of 50%;

b.将负极浆料涂覆在铜箔集流体(也即第二集流体12)上,干燥后涂层总负载量为22mg/cm2,形成负极浆料涂层13,得到负极极片10;b. Coating the negative electrode slurry on the copper foil current collector (that is, the second current collector 12), the total loading of the coating after drying is 22 mg/cm 2 , forming the negative electrode slurry coating 13, and obtaining the negative electrode sheet 10 ;

c.碾压负极极片10厚度到145μm。c. Rolling the negative pole piece 10 to a thickness of 145 μm.

3)锂离子电池的制作:3) Production of lithium-ion batteries:

a.将上述工艺制得的正极极片9、负极极片10与PE隔膜(也即隔膜11)通过卷绕或叠片方式制成电池芯,电芯局部结构如图8所示;a. The positive pole piece 9, the negative pole piece 10 and the PE diaphragm (that is, the diaphragm 11) prepared by the above process are made into a battery core by winding or laminating, and the local structure of the battery core is shown in Figure 8;

b.配置电解液:1mol/LLiPF6,溶剂质量配比为EC:DMC:EMC=5:2:3,1wt%VC,1wt%FEC,1wt%1,3-PS;b. Configure the electrolyte: 1mol/LLiPF6, the solvent mass ratio is EC:DMC:EMC=5:2:3, 1wt% VC, 1wt% FEC, 1wt% 1,3-PS;

c.将上述电解液注入制好的电池芯中,静置、预充化成后,进行相关的性能测试。c. Inject the above-mentioned electrolyte into the prepared battery core, let it stand still, pre-charge and form, and then conduct relevant performance tests.

对实施例3和对比例3的电池在25℃温度条件下,分别进行6C/4C/2C/1C的倍率放电测试,并记录不同倍率的放电下温升和表面温差(红外成像测温),记录结果如表3。The batteries of Example 3 and Comparative Example 3 were subjected to 6C/4C/2C/1C rate discharge tests at a temperature of 25°C, and the temperature rise and surface temperature difference under different rate discharges were recorded (infrared imaging temperature measurement), Record the results as in Table 3.

表3实施例3和对比例3电池倍率放电测试结果Table 3 embodiment 3 and comparative example 3 battery rate discharge test results

Figure BDA0002627860350000191
Figure BDA0002627860350000191

从表3可以看出,实施例3的倍率温升明显低于对比例3。It can be seen from Table 3 that the rate temperature rise of Example 3 is significantly lower than that of Comparative Example 3.

将实施例3、和对比例2的100%SOC电池进行针刺实验,测试方法为:用一个直径为3mm的耐高温钢钉以80mm/s的速度垂直穿透电芯中心(钢针停留在电芯中300s),测试结果如表4:The 100% SOC batteries of Example 3 and Comparative Example 2 were subjected to acupuncture experiments. The test method was: use a high-temperature-resistant steel nail with a diameter of 3 mm to penetrate the center of the battery cell vertically at a speed of 80 mm/s (the steel needle stays on the 300s in the battery), the test results are shown in Table 4:

表4实施例3和对比例3电池针刺实验测试结果Table 4 Example 3 and Comparative Example 3 battery acupuncture test results

Figure BDA0002627860350000192
Figure BDA0002627860350000192

从表3可以看出,实施例3通过针刺测试,且实施例3的温升较低;对比例2未通过针刺测试。As can be seen from Table 3, Example 3 passed the acupuncture test, and the temperature rise of Example 3 was low; Comparative Example 2 failed the acupuncture test.

需要说明的是,本发明中“第一导电剂”、“第一粘结剂”、“第二导电剂”、“第二粘结剂”等中的“第一”、“第二”只是为了区分说明不同组分,其本质还是导电剂或粘结剂;同样,“第一集流体”、“第一活性涂层”、“第一高效导电PTC膜”、“第二活性涂层”、“第二高效导电PTC膜”、“第三活性涂层”、“第三高效导电PTC膜”、“第四活性涂层”、“第二集流体”等中的“第一”、“第二”、“第三”、“第四”,也是为了在结构中对各层进行区分说明,其本质上还是各自结构中的“集流体”、“活性涂层”、“高效导电PTC膜”。It should be noted that the "first" and "second" in the "first conductive agent", "first binder", "second conductive agent", "second binder" in the present invention are only In order to distinguish and illustrate different components, its essence is still a conductive agent or a binder; similarly, "the first current collector", "the first active coating", "the first high-efficiency conductive PTC film", and "the second active coating" , "Second Efficient Conductive PTC Film", "Third Active Coating", "Third Efficient Conductive PTC Film", "Fourth Active Coating", "Second Current Collector", etc. "First", " The second", "third", and "fourth" are also for the purpose of distinguishing and explaining the various layers in the structure, which are essentially "collectors", "active coatings", and "high-efficiency conductive PTC films" in their respective structures. ".

此外,本发明中各高效导电PTC膜实质上是“高效导电PTC多孔膜”,主要原因在于:根据锂离子电池的工作原理,最后实施例的电池可以工作,并且温升和循环性能优于对比例,说明本发明中各高效导电PTC膜可以透过Li+,即具备多孔功能,温升降低说明欧姆电阻降低是缘于膜的高效导电。In addition, each high-efficiency conductive PTC film in the present invention is essentially a "high-efficiency conductive PTC porous film". The ratio shows that each high-efficiency conductive PTC film in the present invention can pass through Li+, that is, it has a porous function, and the decrease in temperature rise shows that the decrease in ohmic resistance is due to the high-efficiency conduction of the film.

综上本发明中,采用在涂层内部夹杂一层或多层高效导电PTC膜,一方面不会影响由于导电剂增加而带来的匀浆分散困难,另一方面,高效导电PTC多孔膜的存在并与集流体粘接,可以涂层内部导电涂层附近的电流密度更加均匀,发热更均匀,还可以起到导电和散热的作用;温度高于PTC材料阈值时可显著降低电化学反应电流。In summary, in the present invention, adopting one or more layers of high-efficiency conductive PTC film inside the coating will not affect the difficulty of homogenate dispersion caused by the increase of conductive agent on the one hand, and on the other hand, the high-efficiency conductive PTC porous film Existing and bonding with the current collector, the current density near the conductive coating inside the coating can be more uniform, the heat generation can be more uniform, and it can also play the role of conduction and heat dissipation; when the temperature is higher than the threshold of the PTC material, the electrochemical reaction current can be significantly reduced .

以上所述仅为本发明的较佳实施例而已,并不用以限制本发明,凡在本发明的精神和原则之内,所作的任何修改、等同替换、改进等,均应包含在本发明的保护范围之内。The above descriptions are only preferred embodiments of the present invention, and are not intended to limit the present invention. Any modifications, equivalent replacements, improvements, etc. made within the spirit and principles of the present invention shall be included in the scope of the present invention. within the scope of protection.

Claims (12)

1. A pole piece, characterized in that: the solar cell comprises a first current collector, wherein first active coatings are arranged on the upper surface and the lower surface of the first current collector, a first efficient conductive PTC film is coated on the outer surface of the first active coating, a second active coating is arranged on the surface of one side, far away from the first current collector, of the first efficient conductive PTC film, a second efficient conductive PTC film is coated on the surface of the second active coating, a third active coating is arranged on the surface of one side, far away from the first current collector, of the second efficient conductive PTC film, the tail ends of the first efficient conductive PTC film are all fixedly adhered to the current collector, the tail ends of the second efficient conductive PTC film are also fixedly adhered to the first current collector, the pole piece is an anode pole piece, and the first current collector is an aluminum foil current collector;
wherein, the conductivity of the active coating of the outermost layer is smaller than that of the other active coatings, and the active material of the active coating of the outermost layer adopts the active material with high thermal stability;
the forming mode of all the high-efficiency conductive PTC films and the active coating of the outermost layer is one of gravure printing, screen printing, extrusion coating, chemical vapor deposition and magnetron sputtering;
the high-efficiency conductive PTC film is a mixture coating of a first conductive agent and a polymer, wherein the polymer is one or more of polyaniline modified polyethylene wax, polyethylene-vinyl acetate, polytetrafluoroethylene, polystyrene, polyolefin, polyvinyl chloride and epoxy resin;
the high-efficiency conductive PTC film also comprises a first adhesive, wherein the weight ratio of the first conductive agent to the polymer to the first adhesive is (95-40) (5-55) (0.01-5);
the first binder is PVDF.
2. A pole piece according to claim 1, characterized in that: the thickness of all the high-efficiency conductive PTC films is 0.1-5 mu m;
and/or the current collector is aluminum foil.
3. A pole piece according to claim 1 or 2, characterized in that: the first conductive agent is a conductive inorganic or conductive polymer having delocalized large pi-bond characteristics.
4. A pole piece according to claim 1 or 2, characterized in that: the first conductive agent is one or more of carbon nano tube, graphene, conductive graphite, conductive carbon black, polyacetylene, polyaniline, polyphenylene ethylene, polydiacetylene, polydianiline and derivatives thereof, polytrianiline and derivatives thereof, polypyrrole and derivatives thereof, polythiophene and derivatives thereof, polyfluorene and derivatives thereof, and polyparaphenylene.
5. A pole piece according to claim 1 or 2, characterized in that: all active coatings are coatings of a mixture of active material, second conductive agent and second binder.
6. A pole piece according to claim 5, characterized in that: the active substance is one or more of nickel cobalt lithium manganate, lithium cobaltate, lithium manganate, lithium iron phosphate and lithium manganese phosphate.
7. A pole piece according to claim 5, characterized in that: the second conductive agent is one or more of conductive carbon black, carbon nano tube and graphene.
8. A pole piece according to claim 5, characterized in that: the second binder is one or more of polytetrafluoroethylene, polyimide, poly-propionic acid and polyacrylonitrile.
9. A pole piece according to claim 5, characterized in that: the content of the conductive agent in the active coating of the outermost layer is smaller than the content of the conductive agent in the active coating of each other layer.
10. A pole piece according to claim 1, characterized in that: the active substance with high thermal stability is one or more of lithium iron phosphate, derivatives thereof and lithium manganate.
11. Use of a pole piece according to any of claims 1 to 10 as positive pole piece in a battery.
12. The utility model provides a low temperature rise high security lithium ion battery, includes positive pole piece, diaphragm and negative pole piece, its characterized in that: the positive electrode sheet is the sheet according to any one of claims 1 to 10.
CN202010802351.XA 2020-08-11 2020-08-11 Pole piece and application, low-temperature elevated safety lithium-ion battery containing the pole piece Active CN111785925B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN202010802351.XA CN111785925B (en) 2020-08-11 2020-08-11 Pole piece and application, low-temperature elevated safety lithium-ion battery containing the pole piece

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN202010802351.XA CN111785925B (en) 2020-08-11 2020-08-11 Pole piece and application, low-temperature elevated safety lithium-ion battery containing the pole piece

Publications (2)

Publication Number Publication Date
CN111785925A CN111785925A (en) 2020-10-16
CN111785925B true CN111785925B (en) 2023-06-02

Family

ID=72761778

Family Applications (1)

Application Number Title Priority Date Filing Date
CN202010802351.XA Active CN111785925B (en) 2020-08-11 2020-08-11 Pole piece and application, low-temperature elevated safety lithium-ion battery containing the pole piece

Country Status (1)

Country Link
CN (1) CN111785925B (en)

Families Citing this family (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN112186273B (en) * 2020-10-29 2022-03-29 珠海冠宇电池股份有限公司 Winding core capable of reducing internal temperature rise for winding type lithium ion battery
CN114520303B (en) * 2020-11-19 2024-10-18 宁德新能源科技有限公司 Electrochemical device and electronic device
CN112864474B (en) * 2021-01-05 2022-10-11 国联汽车动力电池研究院有限责任公司 High-safety battery structure and battery
CN113036148B (en) * 2021-02-26 2022-04-26 烯晶碳能电子科技无锡有限公司 Energy storage system based on conductivity-controllable polymer current collector and preparation process thereof
CN114270561B (en) * 2021-03-31 2024-08-27 宁德新能源科技有限公司 Electrochemical device and electronic device
KR20220153273A (en) * 2021-05-11 2022-11-18 에스케이온 주식회사 Electrode structure and secondary battery including the same
CN114094057A (en) * 2021-11-16 2022-02-25 惠州亿纬锂能股份有限公司 Ternary positive electrode plate of composite polytriphenylamine and preparation method and application thereof
CN116964843A (en) 2022-01-30 2023-10-27 宁德时代新能源科技股份有限公司 Battery pack and electricity utilization device
CN115101712A (en) * 2022-07-20 2022-09-23 厦门海辰储能科技股份有限公司 Positive pole piece, electrolyte, battery pack and power utilization device
CN119768450A (en) * 2022-10-19 2025-04-04 株式会社Lg化学 Copolymer

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105098193A (en) * 2015-09-24 2015-11-25 宁德时代新能源科技有限公司 Positive plate and lithium ion battery comprising same
CN105336916A (en) * 2014-06-20 2016-02-17 东莞新能源科技有限公司 Lithium ion battery pole piece and preparation method thereof
CN108539252A (en) * 2017-03-05 2018-09-14 谷涛 A kind of high security lithium ion battery
CN110364681A (en) * 2019-07-27 2019-10-22 珠海冠宇电池有限公司 A triple-protected high-safety lithium-ion battery cathode
CN110556538A (en) * 2018-06-01 2019-12-10 宁德时代新能源科技股份有限公司 Positive plate and lithium ion battery

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US10964934B2 (en) * 2014-08-25 2021-03-30 Nissan Motor Co., Ltd. Laminate type battery and method for producing the same

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105336916A (en) * 2014-06-20 2016-02-17 东莞新能源科技有限公司 Lithium ion battery pole piece and preparation method thereof
CN105098193A (en) * 2015-09-24 2015-11-25 宁德时代新能源科技有限公司 Positive plate and lithium ion battery comprising same
CN108539252A (en) * 2017-03-05 2018-09-14 谷涛 A kind of high security lithium ion battery
CN110556538A (en) * 2018-06-01 2019-12-10 宁德时代新能源科技股份有限公司 Positive plate and lithium ion battery
CN110364681A (en) * 2019-07-27 2019-10-22 珠海冠宇电池有限公司 A triple-protected high-safety lithium-ion battery cathode

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
《电工材料应用手册》编委会.PTC材料.《电工材料应用手册》.机械工业出版社,1999,第587页. *

Also Published As

Publication number Publication date
CN111785925A (en) 2020-10-16

Similar Documents

Publication Publication Date Title
CN111785925B (en) Pole piece and application, low-temperature elevated safety lithium-ion battery containing the pole piece
WO2022037092A1 (en) Current collector, pole piece and battery
US20220376265A1 (en) Positive electrode plate and lithium-ion battery
WO2020098787A1 (en) Positive pole piece and electrochemical apparatus
JP7590414B2 (en) Secondary battery, device including secondary battery, method for producing secondary battery, and adhesive composition
CN103311500A (en) Lithium-ion battery negative pole piece and production method
CN114709422A (en) Composite current collector, preparation method and lithium ion battery
WO2023155604A1 (en) Composite separator and electrochemical device
CN114824260A (en) Safety lithium ion battery
WO2020098788A1 (en) Positive pole piece and electrochemical apparatus
CN106169617A (en) A kind of space safety high power lithium ion accumulator
CN111564634A (en) Conductive adhesive, cylindrical lithium ion secondary battery and preparation method thereof
WO2023082036A1 (en) Current collector and preparation method therefor, secondary battery, battery module, battery pack, and electrical device
WO2023123087A1 (en) Aqueous positive electrode plate, secondary battery including same, and electric apparatus
CN114497566A (en) Positive plate and lithium ion battery
CN111786040A (en) Pole piece, application thereof and low-temperature-rise long-life lithium ion battery containing pole piece
CN111883765A (en) Lithium battery positive active material, preparation method thereof and lithium battery
WO2023004633A1 (en) Battery, battery module, battery pack, and electrical device
WO2022241096A1 (en) Configuring cell performance using specific anode, cathode, and separator combinations
CN113113603A (en) Lithium ion battery electrode plate, preparation method thereof and lithium ion battery
WO2022156459A1 (en) Negative electrode sheet of lithium ion battery, lithium ion battery and electronic device
CN116632368B (en) Secondary battery and electronic device
WO2023246704A1 (en) Lithium-ion battery electrode plate and preparation method therefor
WO2024046274A1 (en) Positive electrode sheet, secondary battery and electric device
CN102723458A (en) Lithium ion battery and cathode pole piece thereof

Legal Events

Date Code Title Description
PB01 Publication
PB01 Publication
SE01 Entry into force of request for substantive examination
SE01 Entry into force of request for substantive examination
GR01 Patent grant
GR01 Patent grant
PP01 Preservation of patent right

Effective date of registration: 20241021

Granted publication date: 20230602

PP01 Preservation of patent right