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CN115960378A - Polymer-based membrane for composite current collector, preparation method and application - Google Patents

Polymer-based membrane for composite current collector, preparation method and application Download PDF

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CN115960378A
CN115960378A CN202211727981.0A CN202211727981A CN115960378A CN 115960378 A CN115960378 A CN 115960378A CN 202211727981 A CN202211727981 A CN 202211727981A CN 115960378 A CN115960378 A CN 115960378A
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current collector
composite
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base film
composite current
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郑军华
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李旭东
林逢建
任梦强
李云明
高飞
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Svolt Energy Technology Co Ltd
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Abstract

本发明涉及复合集流体用聚合物基膜、复合集流体及制备方法和应用,属于集流体技术领域。聚合物基膜的材料为n型导电聚合物,n型导电聚合物结构的重复单元为式(1)所示:

Figure DDA0004025648590000011
R相同或不同,各自独立的选自氢、卤素、硝基、氰基、C1‑C10卤素取代的烷基、C2‑C10的烯基、C2‑C10的炔基和硅保护的乙烯基。该n型导电聚合物具有高导电性,因而无需增加导电层或添加导电剂,可作为一种极简高性能复合集流体基膜材料;且能够避免复合集流体溶胀问题的同时满足镀层粘附力要求。

Figure 202211727981

The invention relates to a polymer base film for a composite current collector, a composite current collector, a preparation method and an application thereof, and belongs to the technical field of current collectors. The material of the polymer base film is an n-type conductive polymer, and the repeating unit of the n-type conductive polymer structure is shown in formula (1):

Figure DDA0004025648590000011
R is the same or different, each independently selected from hydrogen, halogen, nitro, cyano, C1-C10 halogen-substituted alkyl, C2-C10 alkenyl, C2-C10 alkynyl and silicon-protected vinyl. The n-type conductive polymer has high conductivity, so there is no need to add a conductive layer or add a conductive agent, and it can be used as a minimalist high-performance composite current collector base film material; and it can avoid the swelling problem of the composite current collector while satisfying the adhesion of the coating Force demands.

Figure 202211727981

Description

复合集流体用聚合物基膜、复合集流体及制备方法和应用Polymer base film for composite current collector, composite current collector, preparation method and application

技术领域technical field

本发明涉及集流体技术领域,具体涉及复合集流体用聚合物基膜、复合集流体及制备方法和应用。The invention relates to the technical field of current collectors, in particular to polymer base films for composite current collectors, composite current collectors, preparation methods and applications.

背景技术Background technique

复合集流体包含基膜层和基膜两侧表面的金属层。金属层的材质为铜、铝等金属,其厚度要求一般为1μm左右。通过真空蒸镀或磁控溅射+水电镀工艺在基膜两侧形成金属层,制备复合集流体,适用于锂电池集流体。The composite current collector includes a base film layer and metal layers on both sides of the base film. The material of the metal layer is metal such as copper and aluminum, and its thickness requirement is generally about 1 μm. A metal layer is formed on both sides of the base film by vacuum evaporation or magnetron sputtering + water electroplating process to prepare a composite current collector, which is suitable for lithium battery current collectors.

但由于基膜层大多采用聚对苯二甲酸乙二醇酯(PET)等高分子材料,而这些高分子材料几乎都是绝缘体,导电性极差,导致集流体阻值剧增,影响电池内阻和功率性能发挥。为了解决PET等导电性极差高分子基膜引起的上述诸多问题,目前主要采用以下两种方法:一是在基材中中加入无机或有机高分子导电剂;二是在基材上增加导电层。但以上方法都会大大增加复合集流体的制备工序环节数和制备难度、提高制备成本、降低生产效率,不利于大规模量产导入电芯应用。However, since the base film layer mostly uses polymer materials such as polyethylene terephthalate (PET), and these polymer materials are almost insulators, the conductivity is extremely poor, resulting in a sharp increase in the resistance of the current collector, which affects the internal battery life. resistance and power performance. In order to solve the above problems caused by the extremely poor conductivity polymer base film such as PET, the following two methods are mainly used at present: one is to add inorganic or organic polymer conductive agents to the substrate; the other is to increase the conductivity of the substrate on the substrate. layer. However, the above methods will greatly increase the number of preparation steps and difficulty of preparation of the composite current collector, increase the preparation cost, and reduce the production efficiency, which is not conducive to large-scale mass production and introduction of battery applications.

除了内阻问题外,PET等含氧基团基膜材料,含有大量的酯基,易发生溶胀现象。电池中的电解液与PET等含氧基团基膜材料接触后,PET等含氧基团基膜材料中的酯基基团与电解液中的酯基基团相遇,发生相溶,导致电池在长期的使用过程中基膜层容易出现溶胀现象,破坏了金属层与基膜客户案号层之间的化学键,从而导致复合集流体的金属层与基膜层之间的剥离力不断变差,容易出现金属层与基膜层发生脱落现象,进而影响电池内部的正负极界面,导致电池的电性能变差,同时也影响电池的安全性。而高分子材料溶解后进入电解液内部后,也会增加电解液的粘度,使得离子传输阻碍增加,导致电池后期电池内阻增加。而改用聚丙烯(PP)作为基膜,虽然可以在一定程度上缓解溶胀问题,但PP材质由于分子结构几乎无含氧基团等其它非CH基团存在,容易出现与金属层结合力不足的情况,导致基膜两侧金属层/金属镀层存在金属镀层剥离、涂布拉伸时金属镀层褶皱,以及与锂电活性物质叠片后活性物质被隔膜剥离等其它问题,造成电池良率大大下降,因此也不利于工业化大规模推广使用。In addition to the problem of internal resistance, PET and other oxygen-containing group-based film materials contain a large number of ester groups, which is prone to swelling. After the electrolyte in the battery is in contact with the oxygen-containing base film material such as PET, the ester group in the PET and other oxygen-containing base film materials meets the ester group in the electrolyte and dissolves, causing the battery to During long-term use, the base film layer is prone to swelling, which destroys the chemical bond between the metal layer and the base film customer case number layer, resulting in the continuous deterioration of the peeling force between the metal layer and the base film layer of the composite current collector. , it is easy for the metal layer and the base film layer to fall off, which will affect the positive and negative interface inside the battery, resulting in the deterioration of the electrical performance of the battery and also affecting the safety of the battery. After the polymer material dissolves and enters the electrolyte, it will also increase the viscosity of the electrolyte, which will increase the resistance to ion transmission and lead to an increase in the internal resistance of the battery in the later stage of the battery. The use of polypropylene (PP) as the base film can alleviate the swelling problem to a certain extent, but the molecular structure of PP material has almost no oxygen-containing groups and other non-CH groups, so it is prone to insufficient bonding force with the metal layer. In some cases, the metal layer/metal coating on both sides of the base film has problems such as peeling of the metal coating, wrinkles of the metal coating when coating and stretching, and the separation of the active material by the separator after lamination with the lithium electroactive material, resulting in a significant drop in battery yield. Therefore, it is not conducive to the large-scale promotion and use of industrialization.

发明内容Contents of the invention

因此,本发明要解决的技术问题在于克服现有PET基膜层存在导电性极差,加入导电剂或增加导电层的方式存在成本高、降低生产效率,以及PET基膜存在溶胀问题,导致电池循环性能较差,PP基膜虽能缓解溶胀但存在与金属层结合力不足的问题,从而提供一种复合集流体用聚合物基膜、复合集流体及制备方法和应用。Therefore, the technical problem to be solved by the present invention is to overcome the extremely poor conductivity of the existing PET base film layer, the high cost of adding a conductive agent or the addition of a conductive layer, the reduction of production efficiency, and the swelling problem of the PET base film, resulting in battery The cycle performance is poor, and although the PP base film can relieve swelling, it has the problem of insufficient bonding force with the metal layer, thereby providing a polymer base film for a composite current collector, a composite current collector, a preparation method, and an application.

本发明的技术方案:Technical scheme of the present invention:

一种复合集流体用聚合物基膜,其特征在于,所述聚合物基膜的材料为n型导电聚合物,n型导电聚合物结构的重复单元为式(1)所示;A polymer base film for a composite current collector, characterized in that the material of the polymer base film is an n-type conductive polymer, and the repeating unit of the n-type conductive polymer structure is shown in formula (1);

Figure BDA0004025648570000031
Figure BDA0004025648570000031

其中,R相同或不同,各自独立的选自氢、卤素、硝基、氰基、C1-C10卤素取代的烷基、C2-C10的烯基、C2-C10的炔基和硅保护的乙烯基。Wherein, R is the same or different, each independently selected from hydrogen, halogen, nitro, cyano, C1-C10 halogen-substituted alkyl, C2-C10 alkenyl, C2-C10 alkynyl and silicon-protected vinyl .

R相同或不同,各自独立的选自氢、卤素、硝基、氰基、C1-C5卤素取代的烷基、C2-C5的烯基、C2-C5的炔基和硅保护的乙烯基;优选的,R相同或不同,各自独立的选自氢、卤素、硝基、氰基中的一种;更优选的,R选自氢。R is the same or different, each independently selected from hydrogen, halogen, nitro, cyano, C1-C5 halogen-substituted alkyl, C2-C5 alkenyl, C2-C5 alkynyl and silicon-protected vinyl; preferably Yes, R is the same or different, each independently selected from one of hydrogen, halogen, nitro, cyano; more preferably, R is selected from hydrogen.

所述n型导电聚合物的结构为式(2)所示;The structure of the n-type conductive polymer is shown in formula (2);

Figure BDA0004025648570000032
Figure BDA0004025648570000032

其中n选自1-1000000的整数,优选为1-10000的整数,更优选为1-1000的整数。Where n is selected from an integer of 1-1,000,000, preferably an integer of 1-10,000, more preferably an integer of 1-1,000.

一种复合集流体,包括所述的一种复合集流体用聚合物基膜形成的聚合物基膜层和位于所述聚合物基膜层两侧表面的金属层。A composite current collector comprises a polymer base film layer formed by using a polymer base film for the composite current collector and metal layers located on both sides of the polymer base film layer.

每侧所述金属层的厚度为0.3μm-1.0μm,优选为0.5μm;The thickness of the metal layer on each side is 0.3 μm-1.0 μm, preferably 0.5 μm;

所述金属层的材质为铜、铝或锡中任一种;优选为铜或铝。The material of the metal layer is any one of copper, aluminum or tin; preferably copper or aluminum.

所述复合集流体为复合正极集流体,所述金属层的材质为铝,所述聚合物基膜层的厚度为2.7-12μm;优选为6μm;所述复合正极集流体的厚度为3.7μm-14μm,优选为6-8μm。The composite current collector is a composite positive current collector, the material of the metal layer is aluminum, the thickness of the polymer base film layer is 2.7-12 μm; preferably 6 μm; the thickness of the composite positive current collector is 3.7 μm- 14 μm, preferably 6-8 μm.

所述复合集流体为复合负极集流体,所述金属层的材质为铜,所述聚合物基膜层的厚度为2.7-12μm;优选为4μm;所述复合负极集流体的厚度为3.7μm-14μm,优选为5-7μm。The composite current collector is a composite negative current collector, the material of the metal layer is copper, the thickness of the polymer base film layer is 2.7-12 μm; preferably 4 μm; the thickness of the composite negative current collector is 3.7 μm- 14 μm, preferably 5-7 μm.

一种复合集流体的制备方法,采用真空蒸镀法在所述聚合物基膜的两侧表面镀金属层,包括以下步骤:将金属靶材及待镀的聚合物基膜装入真空蒸镀设备内,并对所述真空蒸镀设备进行抽真空至设备内真空度小于1×10-2Pa;对所述真空蒸镀设备内加热至所述金属靶材的蒸发温度,并在所述聚合物基膜的两侧表面镀上所述金属层,得到所述复合集流体;A method for preparing a composite current collector, using a vacuum evaporation method to coat metal layers on both sides of the polymer base film, comprising the following steps: loading a metal target and a polymer base film to be plated into a vacuum evaporation inside the equipment, and vacuumize the vacuum evaporation equipment until the vacuum degree in the equipment is less than 1×10 -2 Pa; heat the inside of the vacuum evaporation equipment to the evaporation temperature of the metal target, and The metal layer is plated on both sides of the polymer base film to obtain the composite current collector;

所述复合集流体为复合正极集流体,所述金属靶材为铝靶材;所述聚合物基膜的传输移动速率为50-150m/min,优选为100m/min;The composite current collector is a composite positive current collector, and the metal target is an aluminum target; the transfer rate of the polymer base film is 50-150m/min, preferably 100m/min;

或,所述复合集流体为复合负极集流体,所述金属靶材为铜靶材,所述金属层为铜层;所述聚合物基膜的传输移动速率为30-120m/min,优选为90m/min。Or, the composite current collector is a composite negative current collector, the metal target is a copper target, and the metal layer is a copper layer; the transmission rate of the polymer base film is 30-120m/min, preferably 90m/min.

所述金属靶材的纯度为99.9%;和/或,所述金属靶材的蒸发温度为600-1600℃,优选为1100℃。The purity of the metal target is 99.9%; and/or, the evaporation temperature of the metal target is 600-1600°C, preferably 1100°C.

一种极片,包括极片材料以及所述的复合集流体或所述的制备方法得到的复合集流体;A pole piece, including a pole piece material and the composite current collector or the composite current collector obtained by the preparation method;

优选的,所述极片材料为正极材料,所述复合集流体为复合正极集流体其压实保持3.0-3.8g/cm3,优选为3.65g/cm3Preferably, the electrode sheet material is a positive electrode material, and the composite current collector is a composite positive electrode current collector with a compression retention of 3.0-3.8 g/cm 3 , preferably 3.65 g/cm 3 .

优选的,所述极片材料为负极材料,所述复合集流体为复合负极集流体其压实保持1.5-1.8g/cm3,优选为1.65g/cm3Preferably, the electrode sheet material is a negative electrode material, and the composite current collector is a composite negative electrode current collector with a compaction retention of 1.5-1.8 g/cm 3 , preferably 1.65 g/cm 3 .

所述的极片在制备锂离子电池中的应用。The application of the pole piece in the preparation of lithium-ion batteries.

本发明技术方案,具有如下优点:The technical solution of the present invention has the following advantages:

1、本发明的一种复合集流体用聚合物基膜,采用n型高导电聚合物基膜材料,该n型高导电聚合物为苯并二呋喃二酮及其衍生物,其结构的重复单元具有式(1)所示。具有式(1)所示的聚(苯并二呋喃二酮)等n型高导电聚合物的大而刚性的共轭框架,使得(双)极化子和链内载流子能轻松离域,导电性和导热性较高,因此将其用于制备复合集流体的工序中,无需在基膜上额外增加导电层、无需在基膜材料中添加导电剂,可作为一种极简高性能复合集流体基膜材料;同时,聚(苯并二呋喃二酮)等n型高导电聚合物由于含有环内酯上的酮基,与常规碳酸酯类电解液相容性较低,可以很好的避免基膜制备得到的复合集流体在长期锂电循环过程中溶胀的问题,确保循环可以达到锂电设计循环目标值;而且聚(苯并二呋喃二酮)等n型高导电聚合物又具备一定数量的含氧基团,在高能状态下,可很好地与溅射在基膜上的Cu/Al等金属原子结合,组成金属氧化物种子过渡层,从而提升基膜与金属镀层/金属层的粘附力,满足镀层粘附力要求。1. A polymer base film for a composite current collector of the present invention adopts an n-type high-conductivity polymer base film material, and the n-type high-conductivity polymer is benzodifurandione and its derivatives, and its structure repeats The unit has the formula (1). Large and rigid conjugated frameworks with n-type highly conductive polymers such as poly(benzodifurandiones) represented by formula (1), allowing easy delocalization of (bi)polarons and intrachain carriers , high conductivity and thermal conductivity, so it is used in the process of preparing composite current collectors, without adding an additional conductive layer on the base film, without adding a conductive agent to the base film material, and can be used as a minimalist high-performance Composite current collector base film material; at the same time, n-type highly conductive polymers such as poly(benzodifurandione) contain ketone groups on cyclic lactones, which have low compatibility with conventional carbonate electrolytes and can be easily It is good to avoid the problem of swelling of the composite current collector prepared by the base film during the long-term lithium battery cycle, and ensure that the cycle can reach the target value of the lithium battery design cycle; and n-type high-conductivity polymers such as poly(benzodifurandione) have A certain number of oxygen-containing groups, in a high-energy state, can be well combined with metal atoms such as Cu/Al sputtered on the base film to form a metal oxide seed transition layer, thereby improving the base film and metal coating/metal Layer adhesion, to meet the coating adhesion requirements.

2、聚(苯并二呋喃二酮)(PBFDO)是一种电导率为2000S cm-1的高导电聚合物分子,比非结构(1)所示的常规n型聚合物导电性高10倍,能缓解聚合物基膜带来的集流体内阻增大问题,降低极片和电池内阻,减少电芯产热量。2. Poly(benzodifurandione) (PBFDO) is a highly conductive polymer molecule with a conductivity of 2000S cm -1 , which is 10 times more conductive than the conventional n-type polymer shown in non-structure (1) , can alleviate the problem of increasing the internal resistance of the current collector caused by the polymer base film, reduce the internal resistance of the pole piece and the battery, and reduce the heat generated by the battery cell.

3、采用聚(苯并二呋喃二酮)等n型高导电聚合物作为基膜的集流体,在保证电阻性基本不变的情况下,可降低复合集流体金属镀层/金属层厚度,可以由常规的0.6-1.2um(优选0.8um),降低至0.3-1.0um(优选0.5um),节约镀层时间和材料费用,提升产品竞争性。3. Using n-type highly conductive polymers such as poly(benzodifurandione) as the current collector of the base film can reduce the thickness of the metal coating/metal layer of the composite current collector while ensuring that the electrical resistance is basically unchanged. Reduce from the conventional 0.6-1.2um (preferably 0.8um) to 0.3-1.0um (preferably 0.5um), save plating time and material costs, and improve product competitiveness.

4、采用聚(苯并二呋喃二酮)等n型高导电聚合物基膜材料,导热性提升,导致基膜在蒸镀或电磁溅射过程中,耐热温度升高,可进一步加快基膜的的镀层传输速度,镀铝聚合物基膜(复合正极集流体)的传输移动速率为50-150m/min,优选为100m/min;镀铜聚合物基膜(复合负极集流体)的传输移动速率为30-120m/min,优选为90m/min。4. Using n-type highly conductive polymer base film materials such as poly(benzodifurandione), the thermal conductivity is improved, resulting in an increase in the heat-resistant temperature of the base film during evaporation or electromagnetic sputtering, which can further accelerate the base film. The coating transmission speed of the film, the transmission moving speed of the aluminum-plated polymer base film (composite positive current collector) is 50-150m/min, preferably 100m/min; the transmission of the copper-plated polymer base film (composite negative current collector) The moving speed is 30-120 m/min, preferably 90 m/min.

5、因聚(苯并二呋喃二酮)等n型高导电聚合物基膜材料与金属镀层/金属层粘结力提升,正负极均可采用蒸镀方式来实现镀膜;而且金属镀层和基材在高压实时不易剥离,镀铝聚合物基膜(复合正极集流体)做成极片后,复合正极集流体压实保持3.0-3.8g/cm3,优选为3.65g/cm3,大于常规的3.4g/cm3,进而提升电芯质量和体积能量密度。提升箔材压实上限。5. Due to the improved adhesion between n-type highly conductive polymer base film materials such as poly(benzodifurandione) and the metal coating/metal layer, the positive and negative electrodes can be coated by evaporation; and the metal coating and The base material is not easy to peel off under high pressure in real time. After the aluminized polymer base film (composite positive current collector) is made into a pole piece, the composite positive current collector is compacted and maintained at 3.0-3.8g/cm 3 , preferably 3.65g/cm 3 , greater than The conventional 3.4g/cm 3 , thereby improving the quality and volumetric energy density of the cell. Increased foil compaction limit.

6、采用聚(苯并二呋喃二酮)等n型高导电聚合物为基膜的复合集流体,得到电池极片,进入焊接环节,可无需增加焊接转焊片,直接连超声波接焊接连接片上,减少焊接工艺材料,以及降低电极连接片数,缩减极耳在电芯壳体中体积,提升电芯体积能量密度。6. Using n-type high-conductivity polymers such as poly(benzodifurandione) as the composite current collector of the base film, the battery pole pieces are obtained, and when entering the welding process, there is no need to add welding transfer sheets, and they can be directly connected by ultrasonic welding. On-chip, reduce welding process materials, reduce the number of electrode connections, reduce the volume of tabs in the cell shell, and increase the volumetric energy density of the cell.

7、采用聚(苯并二呋喃二酮)等n型高导电聚合物为基膜的复合集流体,能助力复合集流体快速导入电芯,顺利通过5mm钢针刺穿、150度熱箱和热蔓延等安全性能验证,大大拓宽电池应用范围,推动新能源产业发展。7. The composite current collector using n-type high-conductivity polymer such as poly(benzodifurandione) as the base film can help the composite current collector to be quickly introduced into the battery cell, and can pass through the 5mm steel needle, 150-degree heat box and Safety performance verification such as heat spread greatly expands the application range of batteries and promotes the development of new energy industries.

附图说明Description of drawings

为了更清楚地说明本发明具体实施方式或现有技术中的技术方案,下面将对具体实施方式或现有技术描述中所需要使用的附图作简单地介绍,显而易见地,下面描述中的附图是本发明的一些实施方式,对于本领域普通技术人员来讲,在不付出创造性劳动的前提下,还可以根据这些附图获得其他的附图。In order to more clearly illustrate the specific implementation of the present invention or the technical solutions in the prior art, the following will briefly introduce the accompanying drawings that need to be used in the specific implementation or description of the prior art. Obviously, the accompanying drawings in the following description The drawings show some implementations of the present invention, and those skilled in the art can obtain other drawings based on these drawings without any creative work.

图1为实施例1与对比例1的电池循环40周的容量保持率曲线图;Fig. 1 is the capacity retention curve graph of the battery cycle 40 weeks of embodiment 1 and comparative example 1;

图2为实施例1与对比例1的复合正极集流体EIS内阻测试曲线图。2 is an EIS internal resistance test curve of the composite positive current collectors of Example 1 and Comparative Example 1.

具体实施方式Detailed ways

实施例1Example 1

一种复合正极集流体,为复合箔材,包括导电聚合物基膜层和位于所述导电聚合物基膜层两侧表面的金属层;组成所述导电聚合物基膜层的导电聚合物基膜的材料为聚(苯并二呋喃二酮)(PBFDO),其结构式如式(2)所示,其中n为500。基膜层的厚度为6μm。所述金属层的材质为铝,每侧铝层的厚度为0.5μm。A composite positive current collector, which is a composite foil, includes a conductive polymer base film layer and metal layers located on both sides of the conductive polymer base film layer; the conductive polymer base layer that forms the conductive polymer base film layer The material of the membrane is poly(benzodifurandione) (PBFDO), and its structural formula is shown in formula (2), wherein n is 500. The thickness of the base film layer was 6 μm. The material of the metal layer is aluminum, and the thickness of each side of the aluminum layer is 0.5 μm.

Figure BDA0004025648570000071
Figure BDA0004025648570000071

上述一种复合正极集流体的制备方法,采用真空蒸镀法镀金属层,包括以下步骤:将6μm的基膜及99.9%纯度的金属靶材装入真空蒸镀设备内,并对所述真空蒸镀设备进行抽真空至设备内真空度小于1×10-2Pa;对所述真空蒸镀设备内加热至1100℃使得铝靶材蒸发,保持所述基膜的传输移动速率为100m/min,在基膜层两侧的表面镀上厚度为0.5μm的金属铝层,即可得到厚度为7μm的复合铝集流体/复合正极集流体/复合箔材。在镀铝复合集流体制备完成后,对其进行表面氧化层处理,进行惰性保护,然后进行分切收卷以及真空包装作业。The preparation method of the above-mentioned composite positive electrode current collector adopts the vacuum evaporation method to plate a metal layer, comprising the following steps: loading a 6 μm base film and a metal target with a purity of 99.9% into a vacuum evaporation equipment, and applying the vacuum Vacuumize the evaporation equipment until the vacuum degree in the equipment is less than 1×10 -2 Pa; heat the vacuum evaporation equipment to 1100°C to evaporate the aluminum target, and keep the transmission moving speed of the base film at 100m/min , plate a metal aluminum layer with a thickness of 0.5 μm on both sides of the base film layer to obtain a composite aluminum current collector/composite positive electrode current collector/composite foil with a thickness of 7 μm. After the aluminum-coated composite current collector is prepared, the surface oxide layer is treated for inert protection, and then slitting, winding and vacuum packaging operations are performed.

电池制备工艺:将上述得到的复合箔材,用作正极集流体进行软包电池匀浆涂布,匀浆涂布按活性物质(NCM811):导电剂SP(导电炭黑):粘结剂PVDF(聚偏二氟乙烯)=96.8:1.2:2的质量比配比进行,烘干后得到对应活性物质涂布的正极极片。正极极片进行压实处理,因镀层粘结力较强,压实保持3.65g/cm3。对正极极片进行分切叠片后,将复合正极集流体极耳直接焊接至连接片,接着进行注液、封装、预充化成等工序得到软包电池。Battery preparation process: The composite foil obtained above is used as the positive electrode current collector for homogenate coating of soft pack batteries, and the homogenate coating is based on active material (NCM811): conductive agent SP (conductive carbon black): binder PVDF (polyvinylidene fluoride) = 96.8:1.2:2 mass ratio ratio, after drying to obtain the corresponding active material coated positive electrode sheet. The positive pole pieces are compacted, and the compaction is maintained at 3.65g/cm 3 due to the strong bonding force of the coating. After slitting and laminating the positive pole piece, the composite positive current collector lug is directly welded to the connecting piece, and then liquid injection, packaging, pre-charging and other processes are performed to obtain a pouch battery.

实施例2Example 2

一种复合负极集流体,为复合箔材,包括导电聚合物基膜层和位于所述导电聚合物基膜层两侧表面的金属层;组成所述导电聚合物基膜层的导电聚合物基膜的材料为聚(苯并二呋喃二酮)(PBFDO),其结构式如式(2)所示,其中n为500。基膜层的厚度为4μm。所述金属层的材质为铜,每侧铜层的厚度为0.5μm。A composite negative current collector, which is a composite foil, includes a conductive polymer base film layer and metal layers located on both sides of the conductive polymer base film layer; the conductive polymer base layer that forms the conductive polymer base film layer The material of the membrane is poly(benzodifurandione) (PBFDO), and its structural formula is shown in formula (2), wherein n is 500. The thickness of the base film layer was 4 μm. The metal layer is made of copper, and the thickness of the copper layer on each side is 0.5 μm.

Figure BDA0004025648570000091
Figure BDA0004025648570000091

上述一种复合负极集流体的制备方法,采用真空蒸镀法镀金属层,包括以下步骤:将4μm的基膜及99.9%纯度的金属靶材装入真空蒸镀设备内,并对所述真空蒸镀设备进行抽真空至设备内真空度小于1×10-2Pa;对所述真空蒸镀设备内加热至1100℃使得铜靶材蒸发,保持所述基膜的传输移动速率为90m/min,在基膜层两侧的表面镀上厚度为0.5μm的金属铜层,即可得到厚度为5μm的复合铜集流体/复合负极集流体/复合箔材。在复合铜集流体制备完成后,对其进行表面氧化层处理,进行惰性保护,然后进行分切收卷以及真空包装作业。The preparation method of the above-mentioned composite negative electrode current collector adopts the vacuum evaporation method to plate a metal layer, comprising the following steps: loading a 4 μm base film and a metal target with a purity of 99.9% into a vacuum evaporation equipment, and applying the vacuum Vacuumize the evaporation equipment until the vacuum degree in the equipment is less than 1×10 -2 Pa; heat the inside of the vacuum evaporation equipment to 1100°C to evaporate the copper target, and keep the transfer rate of the base film at 90m/min , plate a metal copper layer with a thickness of 0.5 μm on both sides of the base film layer to obtain a composite copper current collector/composite negative electrode current collector/composite foil with a thickness of 5 μm. After the composite copper current collector is prepared, the surface oxide layer is treated for inert protection, and then slitting, winding and vacuum packaging are performed.

电池制备工艺:将上述得到的复合箔材,用作正极集流体进行软包电池匀浆涂布,匀浆涂布比例按活性物质(石墨):导电剂SP(导电炭黑):粘结剂SBR(丁苯橡胶):粘结剂CMC(羧甲基纤维素钠)=97.3:1.2:0.5:1.0配比进行,烘干后得到对应活性物质涂布的负极极片。负极极片进行压实处理,因镀层粘结力较强,压实保持1.65g/cm3。对负极极片进行分切叠片后,将复合箔材极耳直接焊接至连接片,接着进行注液、封装、预充化成等工序得到软包电池。Battery preparation process: The composite foil obtained above is used as the positive electrode current collector for homogenate coating of soft-pack batteries, and the proportion of homogenate coating is active material (graphite): conductive agent SP (conductive carbon black): binder SBR (styrene-butadiene rubber): binder CMC (sodium carboxymethyl cellulose) = 97.3:1.2:0.5:1.0, after drying, a negative electrode sheet coated with a corresponding active material is obtained. The negative pole piece is subjected to compaction treatment, and due to the strong bonding force of the coating, the compaction is maintained at 1.65g/cm 3 . After slitting and stacking the negative pole pieces, the composite foil tabs are directly welded to the connection piece, followed by liquid injection, packaging, pre-filling and other processes to obtain a pouch battery.

实施例3Example 3

一种复合正极集流体,为复合箔材,包括导电聚合物基膜层和位于所述导电聚合物基膜层两侧表面的金属层;组成所述导电聚合物基膜层的导电聚合物基膜的材料为聚(二硝基苯并二呋喃二酮),其结构式如式(4)所示,其中n为500。基膜层的厚度为2.7μm。所述金属层的材质为铝,每侧铝层的厚度为1.0μm。A composite positive current collector, which is a composite foil, includes a conductive polymer base film layer and metal layers located on both sides of the conductive polymer base film layer; the conductive polymer base layer that forms the conductive polymer base film layer The material of the membrane is poly(dinitrobenzodifurandione), and its structural formula is shown in formula (4), wherein n is 500. The thickness of the base film layer was 2.7 μm. The metal layer is made of aluminum, and the thickness of the aluminum layer on each side is 1.0 μm.

Figure BDA0004025648570000101
Figure BDA0004025648570000101

上述一种复合正极集流体的制备方法,采用真空蒸镀法镀金属层,包括以下步骤:将2.7μm的基膜及99.9%纯度的金属靶材装入真空蒸镀设备内,并对所述真空蒸镀设备进行抽真空至设备内真空度小于1×10-2Pa;对所述真空蒸镀设备内加热至1100℃使得铝靶材蒸发,保持所述基膜的传输移动速率为50m/min,在基膜层两侧的表面镀上厚度为1.0μm的金属铝层,即可得到厚度为4.7μm的复合铝集流体/复合正极集流体。在复合铝集流体制备完成后,对其进行表面氧化层处理,进行惰性保护,然后进行分切收卷以及真空包装作业。The preparation method of the above-mentioned composite positive current collector adopts the vacuum evaporation method to plate a metal layer, comprising the following steps: loading a 2.7 μm base film and a metal target with a purity of 99.9% into a vacuum evaporation equipment, and depositing the The vacuum evaporation equipment is evacuated until the vacuum degree in the equipment is less than 1×10 -2 Pa; the vacuum evaporation equipment is heated to 1100°C to evaporate the aluminum target, and the transmission movement rate of the base film is kept at 50m/ min, a metal aluminum layer with a thickness of 1.0 μm is plated on both sides of the base film layer to obtain a composite aluminum current collector/composite positive electrode current collector with a thickness of 4.7 μm. After the composite aluminum current collector is prepared, the surface oxide layer is treated for inert protection, and then slitting, winding and vacuum packaging are performed.

电池制备工艺:将上述得到的复合箔材,用作正极集流体进行软包电池匀浆涂布,按活性物质(NCM811):导电剂SP(导电炭黑):粘结剂PVDF(聚偏二氟乙烯)=96.8:1.2:2的质量比配比进行,烘干后得到对应活性物质涂布的正极极片。正极极片进行压实处理,因镀层粘结力较强,压实保持3.65g/cm3。对正极极片进行分切叠片后,将复合箔材极耳直接焊接至连接片,接着进行注液、封装、预充化成等工序得到软包电池。Battery preparation process: The composite foil obtained above is used as the positive electrode current collector for soft pack battery homogenate coating, according to the active material (NCM811): conductive agent SP (conductive carbon black): binder PVDF (poly Vinyl fluoride)=96.8:1.2:2 mass ratio proportioning, after drying, obtain the positive electrode sheet coated with the corresponding active material. The positive pole pieces are compacted, and the compaction is maintained at 3.65g/cm 3 due to the strong bonding force of the coating. After slitting and stacking the positive pole piece, the composite foil tab is directly welded to the connecting piece, followed by liquid injection, packaging, pre-filling and other processes to obtain a pouch battery.

实施例4Example 4

一种复合正极集流体,为复合箔材,包括导电聚合物基膜层和位于所述导电聚合物基膜层两侧表面的金属层;组成所述导电聚合物基膜层的导电聚合物基膜的材料为聚(苯并二呋喃二酮),其结构式如式(2)所示,其中n为500。基膜层的厚度为12μm。所述金属层的材质为铝,每侧铝层的厚度为0.3μm。A composite positive current collector, which is a composite foil, includes a conductive polymer base film layer and metal layers located on both sides of the conductive polymer base film layer; the conductive polymer base layer that forms the conductive polymer base film layer The material of the membrane is poly(benzodifurandione), and its structural formula is shown in formula (2), wherein n is 500. The thickness of the base film layer was 12 μm. The material of the metal layer is aluminum, and the thickness of each side of the aluminum layer is 0.3 μm.

Figure BDA0004025648570000111
Figure BDA0004025648570000111

上述一种复合正极集流体的制备方法,采用真空蒸镀法镀金属层,包括以下步骤:将12μm的基膜及99.9%纯度的金属靶材装入真空蒸镀设备内,并对所述真空蒸镀设备进行抽真空至设备内真空度小于1×10-2Pa;对所述真空蒸镀设备内加热至1100℃使得铝靶材蒸发,保持所述基膜的传输移动速率为150m/min,在基膜层两侧的表面镀上厚度为0.3um的金属铝层,即可得到厚度为12.6μm的复合铝集流体/复合正极集流体。在复合铝集流体制备完成后,对其进行表面氧化层处理,进行惰性保护,然后进行分切收卷以及真空包装作业。The preparation method of the above-mentioned composite positive current collector adopts the vacuum evaporation method to deposit a metal layer, comprising the following steps: loading a 12 μm base film and a metal target with a purity of 99.9% into a vacuum evaporation equipment, and applying the vacuum Vacuumize the evaporation equipment until the vacuum degree in the equipment is less than 1×10 -2 Pa; heat the vacuum evaporation equipment to 1100°C to evaporate the aluminum target, and keep the transmission moving speed of the base film at 150m/min , plate a metal aluminum layer with a thickness of 0.3um on both sides of the base film layer to obtain a composite aluminum current collector/composite positive electrode current collector with a thickness of 12.6μm. After the composite aluminum current collector is prepared, the surface oxide layer is treated for inert protection, and then slitting, winding and vacuum packaging are performed.

电池制备工艺:将上述得到的复合箔材,用作正极集流体进行软包电池匀浆涂布,按活性物质(NCM811):导电剂SP(导电炭黑):粘结剂PVDF(聚偏二氟乙烯)=96.8:1.2:2的质量比配比进行,烘干后得到对应活性物质涂布的正极极片。正极极片进行压实处理,因其镀层粘结力较强,压实保持3.65g/cm3。对正极极片进行分切叠片后,将复合箔材极耳直接焊接至连接片,接着进行注液、封装、预充化成等工序得到软包电池。Battery preparation process: The composite foil obtained above is used as the positive electrode current collector for soft pack battery homogenate coating, according to the active material (NCM811): conductive agent SP (conductive carbon black): binder PVDF (poly Vinyl fluoride)=96.8:1.2:2 mass ratio proportioning, after drying, obtain the positive electrode sheet coated with the corresponding active material. The positive pole piece is subjected to compaction treatment, because of the strong bonding force of the coating, the compaction maintains 3.65g/cm 3 . After slitting and stacking the positive pole piece, the composite foil tab is directly welded to the connecting piece, followed by liquid injection, packaging, pre-filling and other processes to obtain a pouch battery.

对比例1Comparative example 1

一种复合正极集流体,为复合箔材,包括PET基膜层和位于所述基膜层两侧表面的金属层;所述基膜层的厚度为6μm。所述金属层的材质为铝,每侧铝层的厚度为0.8μm。A composite positive current collector is a composite foil, including a PET base film layer and metal layers located on both sides of the base film layer; the thickness of the base film layer is 6 μm. The metal layer is made of aluminum, and the thickness of each side of the aluminum layer is 0.8 μm.

上述一种复合正极集流体的制备方法,采用真空蒸镀法镀金属层,包括以下步骤:将6μm的基膜及99.9%纯度的金属靶材装入真空蒸镀设备内,并对所述真空蒸镀设备进行抽真空至设备内真空度小于1×10-2Pa;对所述真空蒸镀设备内加热至1100℃使得铝靶材蒸发,保持所述基膜的传输移动速率为50m/min,在基膜层两侧的表面镀上厚度为0.8um的金属铝层,即可得到厚度为7.6um的复合铝集流体/复合正极集流体。在复合铝集流体制备完成后,对其进行表面氧化层处理,进行惰性保护,然后进行分切收卷以及真空包装作业。The preparation method of the above-mentioned composite positive electrode current collector adopts the vacuum evaporation method to plate a metal layer, comprising the following steps: loading a 6 μm base film and a metal target with a purity of 99.9% into a vacuum evaporation equipment, and applying the vacuum Vacuumize the evaporation equipment until the vacuum degree in the equipment is less than 1×10 -2 Pa; heat the vacuum evaporation equipment to 1100°C to evaporate the aluminum target, and keep the transmission moving speed of the base film at 50m/min , plate a metal aluminum layer with a thickness of 0.8um on both sides of the base film layer to obtain a composite aluminum current collector/composite positive electrode current collector with a thickness of 7.6um. After the composite aluminum current collector is prepared, the surface oxide layer is treated for inert protection, and then slitting, winding and vacuum packaging are performed.

电池制备工艺:将上述得到的复合箔材,作为正极集流体进行软包电池匀浆涂布,按活性物质(NCM811):导电剂SP(导电炭黑):粘结剂PVDF(聚偏二氟乙烯)=96.8:1.2:2的质量比配比进行,烘干后得到对应活性物质涂布的正极极片。正极极片进行压实处理,压实保持3.4g/cm3。对正极极片进行分切叠片后,焊接时将复合正极集流体转接极耳再焊至连接片上。接着进行注液、封装、预充化成等工序得到软包电池。Battery preparation process: The composite foil obtained above is used as the positive current collector for soft pack battery homogenate coating, according to the active material (NCM811): conductive agent SP (conductive carbon black): binder PVDF (polyylidene difluoride Ethylene)=96.8:1.2:2 mass ratio proportioning is carried out, obtains the positive pole sheet that corresponding active material coats after drying. The positive pole piece is subjected to compaction treatment, and the compaction is maintained at 3.4g/cm 3 . After slitting and laminating the positive pole piece, the composite positive current collector is transferred to the lug and then welded to the connecting piece during welding. Then, liquid injection, encapsulation, pre-filling and formation are performed to obtain a pouch battery.

对比例2Comparative example 2

一种复合正极集流体,为复合箔材,包括PP基膜层和位于所述基膜层两侧表面的金属层;所述基膜层的厚度为6μm。所述金属层的材质为铝,每侧铝层的厚度为0.8μm。A composite positive current collector is a composite foil, including a PP base film layer and metal layers located on both sides of the base film layer; the thickness of the base film layer is 6 μm. The metal layer is made of aluminum, and the thickness of each side of the aluminum layer is 0.8 μm.

上述一种复合正极集流体的制备方法,采用真空蒸镀法镀金属层,包括以下步骤:将6μm的基膜及99.9%纯度的金属靶材装入真空蒸镀设备内,并对所述真空蒸镀设备进行抽真空至设备内真空度小于1×10-2Pa;对所述真空蒸镀设备内加热至1100℃使得铝靶材蒸发,保持所述基膜的传输移动速率为50m/min,在基膜层两侧的表面镀上厚度为0.8um的金属铝层,即可得到厚度为7.6um的复合铝集流体/复合正极集流体。在镀铝复合集流体制备完成后,对复合集流体进行表面氧化层处理,进行惰性保护,然后进行分切收卷以及真空包装作业。The preparation method of the above-mentioned composite positive electrode current collector adopts the vacuum evaporation method to plate a metal layer, comprising the following steps: loading a 6 μm base film and a metal target with a purity of 99.9% into a vacuum evaporation equipment, and applying the vacuum Vacuumize the evaporation equipment until the vacuum degree in the equipment is less than 1×10 -2 Pa; heat the vacuum evaporation equipment to 1100°C to evaporate the aluminum target, and keep the transmission moving speed of the base film at 50m/min , plate a metal aluminum layer with a thickness of 0.8um on both sides of the base film layer to obtain a composite aluminum current collector/composite positive electrode current collector with a thickness of 7.6um. After the aluminum-coated composite current collector is prepared, the surface oxide layer of the composite current collector is treated for inert protection, and then slitting, winding and vacuum packaging operations are performed.

电池制备工艺:将上述得到的复合箔材,作为正极集流体进行软包电池匀浆涂布,按活性物质(NCM811):导电剂SP(导电炭黑):粘结剂PVDF(聚偏二氟乙烯)=96.8:1.2:2的质量比配比进行,烘干后得到对应活性物质涂布的正极极片。正极极片进行压实处理,压实保持3.4g/cm3。对正极极片进行分切叠片后,焊接时将复合正极集流体转接极耳再焊至连接片上。接着进行注液、封装、预充化成等工序得到软包电池。Battery preparation process: The composite foil obtained above is used as the positive current collector for soft pack battery homogenate coating, according to the active material (NCM811): conductive agent SP (conductive carbon black): binder PVDF (polyylidene difluoride Ethylene)=96.8:1.2:2 mass ratio proportioning is carried out, obtains the positive pole sheet that corresponding active material coats after drying. The positive pole piece is subjected to compaction treatment, and the compaction is maintained at 3.4g/cm 3 . After slitting and laminating the positive pole piece, the composite positive current collector is transferred to the lug and then welded to the connecting piece during welding. Then, liquid injection, encapsulation, pre-filling and formation are performed to obtain a pouch battery.

测试例test case

循环性能测试:分别对实施例和对比例获得的软包电池进行循环测试,充放电条件为0.33C/1C,温度为25℃,并测试循环过程中的容量保持率数据,结果如表1和图1所示,同时电芯循环后进行拆解得到对应极片,测试极片溶胀程度程度,结果如表1所示。Cycle performance test: Cycle test was carried out on the pouch batteries obtained in the examples and comparative examples respectively, the charge and discharge conditions were 0.33C/1C, the temperature was 25°C, and the capacity retention data during the test cycle was tested. The results are shown in Table 1 and As shown in Figure 1, at the same time, the cell was disassembled after cycling to obtain the corresponding pole piece, and the degree of swelling of the pole piece was tested. The results are shown in Table 1.

表1.测试数据Table 1. Test data

Figure BDA0004025648570000141
Figure BDA0004025648570000141

备注:极片溶胀程度=(W2-W1)/W1×100%,W2为浸泡后质量,W1为浸泡前质量。Remarks: pole piece swelling degree = (W2-W1)/W1×100%, W2 is the mass after immersion, W1 is the mass before immersion.

如图1和表1所示,实施例1-4的PBFDO基膜和聚(二硝基苯并二呋喃二酮)基膜集流体循环性能,优于对比例1的PET基膜的复合集流体和对比例2的PP基膜的复合集流体,这是由于PBFDO含有环内酯上的酮基,与常规碳酸酯类电解液相容性较低,可以很好的避免基膜制备得到的复合集流体,在长期锂电循环过程中溶胀的问题,确保循环可以达到锂电设计循环目标值。As shown in Figure 1 and Table 1, the PBFDO base film of embodiment 1-4 and poly (dinitrobenzodifurandione) base film current collector circulation performance, is better than the composite collection of the PET base film of comparative example 1 Fluid and the composite current collector of the PP base film of Comparative Example 2, this is because PBFDO contains ketone groups on the cyclic lactone, which is less compatible with conventional carbonate electrolytes, and can well avoid the preparation of the base film The problem of swelling of the composite current collector during the long-term lithium battery cycle ensures that the cycle can reach the target value of the lithium battery design cycle.

EIS(电化学阻抗谱)内阻测试:分别对实施例1和对比例1获得的扣式电池进行EIS内阻测试。在扣式电池化成后第3圈,保持50%SOC(电池剩余容量)情况下,在100KHz至10mHz的频率范围内以5mV的电势幅度循环之后立即进行阻抗测量。如图2所示,实施例1的PBFDO基膜内阻测试优于对比例1的PET基膜。EIS (Electrochemical Impedance Spectroscopy) internal resistance test: EIS internal resistance test was performed on the button cells obtained in Example 1 and Comparative Example 1 respectively. Impedance measurement was performed immediately after cycling with a potential amplitude of 5 mV in the frequency range from 100 KHz to 10 mHz at 50% SOC (battery remaining capacity) on the 3rd cycle after the coin cell was formed. As shown in FIG. 2 , the internal resistance test of the PBFDO base film of Example 1 is better than that of the PET base film of Comparative Example 1.

剥离力测试:分别对实施例1和对比例1、2获得的复合正极集流体/复合箔材进行剥离力测试。剥离力测试方法和过程为:1、裁切复合箔材,用刀模裁切待测试复合箔材至尺寸为300mm×30mm。2、粘贴固定复合箔材,取一块尺寸为400mm×40mm且平整的薄钢板,首先在钢板中心贴上一条双面胶(其长度大于复合箔材的测试长度即可,与复合箔材等宽),用力抚平,保证双面胶紧密贴合在钢板中心。揭开双面胶,将待测试复合箔材一侧表面的金属镀层的下部表面贴合在胶条上,必须保证贴胶部分的复合箔材与胶纸完成匹配贴合。3、安装测试,拉力机上有上下两个夹子,将已粘贴固定复合箔材的钢板插入下夹内,垂直固定,贴胶部分的复合箔材在下、未贴胶部分的复合箔材在上,将未贴胶部分的复合箔材插入上夹内固定,保持复合箔材竖直放置,即使贴胶部分的复合箔材与未贴胶部分的复合箔材成180°。固定好测试样品后,首先校准清零,设定测试宽度为23mm,极片剥离长度75mm,剥离速150mm/min,然后开始测试,结果见表2。Peeling force test: The peeling force test was carried out on the composite positive current collector/composite foil obtained in Example 1 and Comparative Examples 1 and 2 respectively. The peel force test method and process are as follows: 1. Cut the composite foil, and use a die to cut the composite foil to be tested to a size of 300mm×30mm. 2. Paste and fix the composite foil, take a flat thin steel plate with a size of 400mm×40mm, first paste a double-sided adhesive tape on the center of the steel plate (the length should be greater than the test length of the composite foil, and the same width as the composite foil) ), and smooth it with force to ensure that the double-sided adhesive sticks tightly to the center of the steel plate. Uncover the double-sided adhesive tape, and attach the lower surface of the metal coating on one side of the composite foil to be tested to the adhesive strip. It is necessary to ensure that the composite foil on the glued part is matched with the adhesive paper. 3. Installation test. There are two upper and lower clips on the tensile machine. Insert the steel plate pasted and fixed with the composite foil into the lower clip and fix it vertically. The composite foil of the glued part is on the bottom and the composite foil of the unglued part is on the top. Insert the composite foil of the unglued part into the upper clip to fix it, and keep the composite foil vertically, even if the composite foil of the glued part is 180° from the composite foil of the unglued part. After fixing the test sample, first calibrate and clear, set the test width to 23mm, the stripping length of the pole piece to 75mm, and the stripping speed to 150mm/min, and then start the test. The results are shown in Table 2.

表2.剥离力测试数据Table 2. Peel force test data

Figure BDA0004025648570000151
Figure BDA0004025648570000151

如表2所示,实施例1的PBFDO基膜剥离强度好于对比例2的PP基膜,接近于对比例1的PET基膜,能够满足镀层粘附力要求。As shown in Table 2, the peel strength of the PBFDO base film of Example 1 is better than that of the PP base film of Comparative Example 2, close to that of the PET base film of Comparative Example 1, and can meet the adhesion requirements of the coating.

显然,上述实施例仅仅是为清楚地说明所作的举例,而并非对实施方式的限定。对于所属领域的普通技术人员来说,在上述说明的基础上还可以做出其它不同形式的变化或变动。这里无需也无法对所有的实施方式予以穷举。而由此所引伸出的显而易见的变化或变动仍处于本发明创造的保护范围之中。Apparently, the above-mentioned embodiments are only examples for clear description, rather than limiting the implementation. For those of ordinary skill in the art, other changes or changes in different forms can be made on the basis of the above description. It is not necessary and impossible to exhaustively list all the implementation manners here. And the obvious changes or changes derived therefrom are still within the scope of protection of the present invention.

Claims (10)

1. The polymer-based film for the composite current collector is characterized in that the material of the polymer-based film is an n-type conductive polymer, and the repeating unit of the n-type conductive polymer structure is shown in a formula (1);
Figure FDA0004025648560000011
wherein R is the same or different and is independently selected from hydrogen, halogen, nitro, cyano, C1-C10 halogen substituted alkyl, C2-C10 alkenyl, C2-C10 alkynyl and silicon protected vinyl.
2. The polymer-based film for the composite current collector as claimed in claim 1, wherein R is the same or different and is independently selected from hydrogen, halogen, nitro, cyano, C1-C5 halogen substituted alkyl, C2-C5 alkenyl, C2-C5 alkynyl and silicon protected vinyl;
preferably, R is the same or different and is independently selected from one of hydrogen, halogen, nitro and cyano;
more preferably, R is selected from hydrogen.
3. The polymer-based film for a composite current collector as claimed in claim 1 or 2, wherein the structure of the n-type conductive polymer is represented by formula (2);
Figure FDA0004025648560000012
wherein n is selected from the group consisting of integers from 1 to 1000000, preferably from 1 to 10000, more preferably from 1 to 1000.
4. A composite current collector comprising a polymer-based film layer formed from the polymer-based film for a composite current collector according to any one of claims 1 to 3, and metal layers on both side surfaces of the polymer-based film layer.
5. The composite current collector of claim 4, wherein the thickness of the metal layer on each side is between 0.3 μm and 1.0 μm, preferably 0.5 μm;
the metal layer is made of any one of copper, aluminum or tin; preferably copper or aluminium.
6. The composite current collector of claim 5, wherein the composite current collector is a composite positive electrode current collector, the metal layer is made of aluminum, and the polymer-based film layer has a thickness of 2.7-12 μm; preferably 6 μm.
Or the composite current collector is a composite negative current collector, the metal layer is made of copper, and the thickness of the polymer-based film layer is 2.7-12 mu m; preferably 4 μm.
7. The method of any one of claims 4 to 6, wherein the metal layers are plated on both surfaces of the polymer-based film by vacuum evaporation;
preferably, the method comprises the following steps: metal target material and metal target materialLoading the plated polymer base film into a vacuum evaporation device, and vacuumizing the vacuum evaporation device until the vacuum degree in the device is less than 1 multiplied by 10 -2 Pa; heating the interior of the vacuum evaporation equipment to the evaporation temperature of the metal target, and plating the metal layers on the two side surfaces of the polymer base film to obtain the composite current collector;
the composite current collector is a composite positive current collector, and the metal target is an aluminum target; the transmission moving speed of the polymer base film is 50-150m/min, preferably 100m/min;
or the composite current collector is a composite negative current collector, and the metal target is a copper target; the transport rate of the polymer-based film is 30-120m/min, preferably 90m/min.
8. The method according to claim 7, wherein the purity of the metal target material is 99.9%;
and/or the evaporation temperature of the metal target material is 600-1600 ℃, preferably 1100 ℃.
9. A pole piece, which is characterized by comprising a pole piece material and the composite current collector of any one of claims 3 to 6 or the composite current collector obtained by the preparation method of claim 7 or 8;
preferably, the pole piece material is a positive pole material, the composite current collector is a composite positive pole current collector, and the compaction and maintenance of the composite positive pole current collector are 3.0-3.8g/cm 3 Preferably 3.65g/cm 3
Or the pole piece material is a negative electrode material, and the composite current collector is a composite negative electrode current collector which is compacted and kept at 1.5-1.8g/cm 3 Preferably 1.65g/cm 3
10. Use of the pole piece of claim 9 in the manufacture of a lithium ion battery.
CN202211727981.0A 2022-12-29 2022-12-29 Polymer-based membrane for composite current collector, preparation method and application Pending CN115960378A (en)

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