CN115832212A - Negative pole piece and secondary battery, battery module, battery pack and electric device comprising same - Google Patents

Negative pole piece and secondary battery, battery module, battery pack and electric device comprising same Download PDF

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CN115832212A
CN115832212A CN202210538481.6A CN202210538481A CN115832212A CN 115832212 A CN115832212 A CN 115832212A CN 202210538481 A CN202210538481 A CN 202210538481A CN 115832212 A CN115832212 A CN 115832212A
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film layer
negative electrode
layer
electrode sheet
battery
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CN115832212B (en
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王育文
叶永煌
吴益扬
武宝珍
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Contemporary Amperex Technology Co Ltd
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Abstract

本申请提供了一种单层涂布的负极极片,通过限定负极膜层中碳微米管和导电剂的质量分数满足一定的关系,从而提高锂离子在负极膜层的扩散能力,改善电池的充电性能。本申请还提供了一种双层涂布的负极极片,通过在第一膜层和第二膜层中的至少一层包含碳微米管,达到改善电池的充电性能的目的。此外,本申请也涉及包含上述单层涂布和双层涂布的负极极片的二次电池、电池模块、电池包和用电装置。The application provides a single-layer coated negative electrode sheet, which satisfies a certain relationship by limiting the mass fraction of carbon microtubes and conductive agents in the negative electrode film layer, thereby improving the diffusion capacity of lithium ions in the negative electrode film layer and improving the performance of the battery. Charging performance. The present application also provides a double-coated negative electrode sheet, by including carbon microtubes in at least one of the first film layer and the second film layer, so as to achieve the purpose of improving the charging performance of the battery. In addition, the present application also relates to a secondary battery, a battery module, a battery pack, and an electrical device comprising the above-mentioned single-layer coated and double-layer coated negative electrode sheets.

Description

负极极片及包含其的二次电池、电池模块、电池包、用电装置Negative electrode sheet and secondary battery containing it, battery module, battery pack, electrical device

技术领域technical field

本申请涉及锂电池技术领域,尤其涉及一种单层涂布的负极极片和双层涂布的负极极片,以及包含其的二次电池、电池模块、电池包和用电装置。The present application relates to the technical field of lithium batteries, in particular to a single-layer coated negative electrode sheet and a double-layer coated negative electrode sheet, as well as secondary batteries, battery modules, battery packs and electrical devices containing them.

背景技术Background technique

近年来,随着二次电池的应用范围越来越广泛,二次电池广泛应用于水力、火力、风力和太阳能电站等储能电源系统,以及电动工具、电动自行车、电动摩托车、电动汽车、军事装备、航空航天等多个领域。In recent years, as the application range of secondary batteries has become more and more extensive, secondary batteries have been widely used in energy storage power systems such as hydraulic, thermal, wind and solar power plants, as well as electric tools, electric bicycles, electric motorcycles, electric vehicles, Military equipment, aerospace and other fields.

但是,在二次电池具有厚的涂布重量(例如至少为9mg/cm2)的电极时,电池的快速充电性能较低;电芯内部极化增加,电芯寿命恶化,并且出现析锂等引发安全隐患的因素。因此,具有厚涂布的二次电池的电化学性能仍有待改进,尤其是改善其快速充电性能。However, when the secondary battery has an electrode with a thick coating weight (for example, at least 9mg/cm 2 ), the fast charging performance of the battery is low; the internal polarization of the battery increases, the life of the battery deteriorates, and lithium precipitation occurs. Factors that cause safety hazards. Therefore, the electrochemical performance of secondary batteries with thick coatings still needs to be improved, especially to improve their fast charging performance.

发明内容Contents of the invention

本申请是鉴于上述课题而进行的,其目的在于,提供一种能够改善二次电池的充电能力的负极极片,并提供包括本申请负极极片的二次电池、电池模块、电池包和用电装置。The present application is made in view of the above-mentioned problems, and its purpose is to provide a negative electrode sheet capable of improving the chargeability of a secondary battery, and to provide a secondary battery, a battery module, a battery pack, and a battery for use including the negative electrode sheet of the present application. electric device.

为了实现上述目的,本申请的第一方面提供了一种单层涂布的负极极片,其包括集流体以及设置在集流体的至少一个表面上的负极膜层,该负极膜层包含负极活性物质和碳微米管,任选地包含导电剂;其中,碳微米管在负极膜层的质量分数W1与导电剂在负极膜层的质量分数W2满足:当0.2%≤W1≤2%时,则W1+W2≤2%;当W1>2%时,则0≤W2≤0.5%,基于负极膜层的总重量计。In order to achieve the above object, the first aspect of the present application provides a single-layer coated negative electrode sheet, which includes a current collector and a negative electrode film layer arranged on at least one surface of the current collector, the negative electrode film layer contains negative active The substance and carbon microtubes optionally contain a conductive agent; wherein, the mass fraction W1 of the carbon microtubes in the negative electrode film layer and the mass fraction W2 of the conductive agent in the negative electrode film layer meet: when 0.2%≤W1≤2%, then W1+W2≤2%; when W1>2%, then 0≤W2≤0.5%, based on the total weight of the negative film layer.

本申请通过在负极膜层中加入碳微米管,并且限定碳微米管和导电剂在负极膜层中的质量分数满足一定的关系,以提高负极膜层的保液能力,促进锂离子在负极膜层的扩散能力,从而改善二次电池的充电性能。This application adds carbon microtubes to the negative electrode film layer, and limits the mass fraction of carbon microtubes and conductive agent in the negative electrode film layer to meet a certain relationship, so as to improve the liquid retention capacity of the negative electrode film layer and promote lithium ion in the negative electrode film. The diffusion ability of the layer, thereby improving the charging performance of the secondary battery.

在任意实施方式中,在单层涂布的负极极片中,碳微米管在负极膜层的质量分数W1为0.2%至5%。由此进一步优化负极膜层的组分,提高二次电池的充电性能。In any embodiment, in the single-layer coated negative electrode sheet, the mass fraction W1 of carbon microtubes in the negative electrode film layer is 0.2% to 5%. In this way, the components of the negative electrode film layer are further optimized to improve the charging performance of the secondary battery.

在任意实施方式中,在单层涂布的负极极片中,碳微米管的内径为0.2μm至12μm,可选2μm至10μm;可选地,长径比为2-20;进一步可选地,碳微米管的管壁厚度为0.01μm至1μm。通过限定碳微米管的规格,碳微米管可以在负极膜层中充分发挥其储液和保液的作用,提高液相扩散能力,从而充分利用负极膜膜层的活性物质,改善电池的充电性能。In any embodiment, in the single-layer coated negative electrode sheet, the inner diameter of the carbon microtube is 0.2 μm to 12 μm, optionally 2 μm to 10 μm; optionally, the aspect ratio is 2-20; further optionally , the wall thickness of carbon microtubes is 0.01 μm to 1 μm. By limiting the specifications of the carbon microtubes, the carbon microtubes can fully play the role of liquid storage and liquid retention in the negative electrode film layer, improve the liquid phase diffusion ability, and thus make full use of the active material of the negative electrode film layer to improve the charging performance of the battery .

在任意实施方式中,在单层涂布的负极极片中,负极活性物质包括人造石墨、天然石墨、硅基材料中的至少一种;可选地,导电剂包括导电剂sp、KS-6、导电石墨、碳纳米管、石墨烯、碳纤维VGCF中的至少一种。In any embodiment, in the single-layer coated negative electrode sheet, the negative active material includes at least one of artificial graphite, natural graphite, and silicon-based materials; optionally, the conductive agent includes conductive agent sp, KS-6 , conductive graphite, carbon nanotubes, graphene, carbon fiber VGCF at least one.

本申请的第二方面提供了一种双层涂布的负极极片,其包括集流体、第一膜层和第二膜层;其中,第一膜层设置在集流体的至少一个表面上,第二膜层设置在第一膜层的外表面上;第一膜层位于集流体和第二膜层之间;以及,第一膜层包含第一负极活性物质,第二膜层包含第二负极活性物质;第一膜层和第二膜层中的至少一层包含碳微米管;并且,第一膜层和第二膜层之间至少在负极活性物质、是否包括碳微米管,这二者之一不同。The second aspect of the present application provides a double-coated negative electrode sheet, which includes a current collector, a first film layer, and a second film layer; wherein the first film layer is disposed on at least one surface of the current collector, The second film layer is arranged on the outer surface of the first film layer; the first film layer is located between the current collector and the second film layer; and, the first film layer contains the first negative electrode active material, and the second film layer contains the second film layer negative electrode active material; at least one layer of the first film layer and the second film layer contains carbon microtubes; one of them is different.

本申请通过在双层涂布的负极极片的膜层中引入碳微米管,提升了膜层的储液能力,保证了锂离子在整个膜层中的扩散,达到充分利用膜层中活性物质的目的,从而改善二次电池的电化学性能,尤其是充电性能。This application introduces carbon microtubes into the film layer of the double-coated negative electrode sheet, which improves the liquid storage capacity of the film layer, ensures the diffusion of lithium ions in the entire film layer, and makes full use of the active materials in the film layer. The purpose of improving the electrochemical performance of the secondary battery, especially the charging performance.

在任意实施方式中,在双层涂布的负极极片中,第一膜层不包含碳微米管,第二膜层包含碳微米管。由此,通过进一步限定碳微米管的分布,实现第二膜层(上层)具有充足的电解液的目的,从而促进锂离子向第一膜层(下层)的扩散,以充分利用负极活性物质。In any embodiment, in the double-coated negative electrode sheet, the first film layer does not contain carbon microtubes, and the second film layer contains carbon microtubes. Thus, by further limiting the distribution of carbon microtubes, the second film layer (upper layer) has sufficient electrolyte solution, thereby promoting the diffusion of lithium ions to the first film layer (lower layer) to make full use of the negative electrode active material.

在任意实施方式中,在双层涂布的负极极片中,第一膜层和第二膜层均包含碳微米管。由此,这两层膜层的保液能力增加,锂离子通道贯穿整个膜层,以进一步提升锂离子的扩散能力。In any embodiment, in the double-coated negative electrode sheet, both the first film layer and the second film layer contain carbon microtubes. As a result, the liquid retention capacity of the two layers of film is increased, and the lithium ion channel runs through the entire film layer to further improve the diffusion capacity of lithium ions.

在任意实施方式中,在双层涂布的负极极片中,第一膜层和第二膜层中,所述碳微米管的总质量分数W3为0.2%至5%,基于所述第一膜层和第二膜层的总重量计。由此,进一步限定碳微米管在双膜层的质量分数,以优化负极极片的电化学性能,从而提高电池的充电能力。In any embodiment, in the double-coated negative electrode sheet, in the first film layer and the second film layer, the total mass fraction W3 of the carbon microtubes is 0.2% to 5%, based on the first The total weight of the film layer and the second film layer. Thus, the mass fraction of carbon microtubes in the double film layer is further limited to optimize the electrochemical performance of the negative electrode sheet, thereby improving the charging capacity of the battery.

在任意实施方式中,在双层涂布的负极极片中,第一膜层和第二膜层中,任选地还包含导电剂,所述碳微米管的总质量分数W3与所述导电剂的总质量分数W4满足:当0.2%≤W3≤2%时,则W3+W4≤2%;当W3>2%时,则0≤W4≤0.5%,基于所述第一膜层和第二膜层的总质量计。当碳微米管和导电剂的总质量分数满足特定的关系时,能够实现负载物(碳微米管和导电剂)的量、能量密度和充电性能之间的平衡,提升快速充电能力。In any embodiment, in the double-coated negative electrode sheet, the first film layer and the second film layer optionally also contain a conductive agent, and the total mass fraction W3 of the carbon microtubes is related to the conductive material. The total mass fraction W4 of the agent satisfies: when 0.2%≤W3≤2%, then W3+W4≤2%; when W3>2%, then 0≤W4≤0.5%, based on the first film layer and the second The total mass of the two film layers. When the total mass fraction of carbon microtubes and conductive agent satisfies a specific relationship, the balance between the amount of load (carbon microtubes and conductive agent), energy density and charging performance can be achieved, and the fast charging ability can be improved.

在任意实施方式中,在双层涂布的负极极片中,碳微米管在所述第二膜层的质量相对于所述碳微米管的总质量为50-100%。通过碳微米管全部或大部分地存在于第二膜层中,有利于更多的含锂离子的电解液扩散到上层,以提供充足的锂离子达到上层与下层的界面处、以及下层与集流体界面处,实现充分利用下层活性物质的目的。In any embodiment, in the double-coated negative electrode sheet, the mass of the carbon microtubes in the second film layer is 50-100% relative to the total mass of the carbon microtubes. All or most of the carbon microtubes exist in the second film layer, which is conducive to the diffusion of more lithium-ion-containing electrolytes to the upper layer, so as to provide sufficient lithium ions to reach the interface between the upper layer and the lower layer, and the lower layer and the collector. At the fluid interface, the purpose of making full use of the active material in the lower layer is achieved.

在任意实施方式中,在双层涂布的负极极片中,碳微米管的直径为0.2μm至12μm,可选2μm至10μm;长径比为2-20;所述碳微米管的管壁厚度为0.01μm至1μm。通过限定合适规格的碳微米管,实现孔径分布的均一性,膜层的储液、保液能力增强,锂离子扩散能力得以提升。In any embodiment, in the double-coated negative electrode sheet, the diameter of the carbon microtube is 0.2 μm to 12 μm, optionally 2 μm to 10 μm; the aspect ratio is 2-20; the tube wall of the carbon microtube The thickness is 0.01 μm to 1 μm. By limiting the carbon microtubes with appropriate specifications, the uniformity of pore size distribution is realized, the liquid storage and liquid retention capacity of the membrane layer are enhanced, and the lithium ion diffusion capacity is improved.

在任意实施方式中,在双层涂布的负极极片中,只有第一膜层包含碳微米管的条件下,在所述第一膜层和第二膜层中,任选地还包含导电剂;所述第二膜层中的所述碳微米管的质量分数为0.4%至10%,以及所述导电剂的质量分数为0%至4%,可选地0%至1.6%,基于第二膜层的重量计;所述第一膜层中的所述导电剂的质量分数为0%至4%,可选地0%至2%,基于第一膜层的重量计。In any embodiment, in the double-coated negative electrode sheet, under the condition that only the first film layer contains carbon microtubes, the first film layer and the second film layer optionally also contain conductive agent; the mass fraction of the carbon microtubes in the second film layer is 0.4% to 10%, and the mass fraction of the conductive agent is 0% to 4%, optionally 0% to 1.6%, based on The weight of the second film layer; the mass fraction of the conductive agent in the first film layer is 0% to 4%, optionally 0% to 2%, based on the weight of the first film layer.

在任意实施方式中,在双层涂布的负极极片中,在第一和第二膜层均包含碳微米管的条件下,第一膜层和第二膜层中任选地还包含导电剂;所述碳微米管在各膜层中的质量分数为0.2%至5%,并且所述导电剂在各膜层中的质量分数为0%至2%,基于各膜层的重量计。In any embodiment, in the double-coated negative electrode sheet, under the condition that the first and second film layers both contain carbon microtubes, the first film layer and the second film layer optionally further contain conductive agent; the mass fraction of the carbon microtubes in each film layer is 0.2% to 5%, and the mass fraction of the conductive agent in each film layer is 0% to 2%, based on the weight of each film layer.

通过进一步限定碳微米管和导电剂在各膜层中的质量含量,以优化负极膜层的组成和结构,从而达到最佳的快充能力。By further limiting the mass content of carbon microtubes and conductive agents in each film layer, the composition and structure of the negative electrode film layer are optimized, so as to achieve the best fast charging capability.

在任意实施方式中,在双层涂布的负极极片中,在第一和第二膜层均包含碳微米管的条件下,碳微米管在所述第二膜层与在第一膜层中的质量分数比10:3至1:1。In any embodiment, in the double-coated negative electrode sheet, under the condition that both the first and the second film layers contain carbon microtubes, the carbon microtubes in the second film layer and in the first film layer The mass fraction ratio in 10:3 to 1:1.

在任意实施方式中,在双层涂布的负极极片中,第二膜层与第一膜层的重量比为1:4至4:1。由此,上层与下层的扩散性能达到最佳的配比,进一步改善电池的快充能力。In any embodiment, in the double-coated negative electrode sheet, the weight ratio of the second film layer to the first film layer is 1:4 to 4:1. As a result, the diffusion performance of the upper layer and the lower layer reaches an optimal ratio, further improving the fast charging capability of the battery.

在任意实施方式中,在双层涂布的负极极片中,第一和第二负极活性物质可为相同或不同的,包括人造石墨、天然石墨、硅基材料中的至少一种。In any embodiment, in the double-coated negative electrode sheet, the first and second negative electrode active materials may be the same or different, including at least one of artificial graphite, natural graphite, and silicon-based materials.

在任意实施方式中,在双层涂布的负极极片中,导电剂在第一膜层和第二膜层中可为相同或不同的,包括导电剂sp、KS-6、导电石墨、碳纳米管、石墨烯、碳纤维VGCF中的至少一种。In any embodiment, in the double-coated negative electrode sheet, the conductive agent can be the same or different in the first film layer and the second film layer, including conductive agent sp, KS-6, conductive graphite, carbon At least one of nanotubes, graphene, carbon fiber VGCF.

本申请的第三方面提供一种二次电池,其中,包括本申请第一方面所述的单层涂布的负极极片和本申请第二方面所述的双层涂布的负极极片。The third aspect of the present application provides a secondary battery, which includes the single-layer coated negative electrode sheet described in the first aspect of the present application and the double-layer coated negative electrode sheet described in the second aspect of the present application.

本申请的第四方面提供一种电池模块,其包括本申请第三方面所述的二次电池。A fourth aspect of the present application provides a battery module, which includes the secondary battery described in the third aspect of the present application.

本申请的第五方面提供一种电池包,其包括本申请第四方面所述的电池模块。A fifth aspect of the present application provides a battery pack, which includes the battery module described in the fourth aspect of the present application.

本申请的第六方面提供一种用电装置,其包括本申请第三方面所述的二次电池、本申请第四方面所述的电池模块或本申请第五方面所述的电池包中的至少一种。The sixth aspect of the present application provides an electric device, which includes the secondary battery described in the third aspect of the present application, the battery module described in the fourth aspect of the present application, or the battery pack described in the fifth aspect of the present application. at least one.

本申请通过在二次电池的负极极片中使用碳微米管,同时限定碳微米管和导电剂的质量分数满足一定的关系,使二次电池的快充能力得以提升。相应地,本申请提供的电池包、电池模块和用电装置具有改善的快充能力。This application uses carbon microtubes in the negative electrode sheet of the secondary battery, and at the same time limits the mass fraction of the carbon microtubes and the conductive agent to satisfy a certain relationship, so that the fast charging capability of the secondary battery is improved. Correspondingly, the battery pack, battery module and electric device provided by the present application have improved fast charging capability.

附图说明Description of drawings

图1为本申请一实施方式的单层涂布的负极极片的示意图。FIG. 1 is a schematic diagram of a single-layer coated negative electrode sheet according to an embodiment of the present application.

图2为本申请一实施方式的双层涂布的负极极片的示意图Figure 2 is a schematic diagram of a double-coated negative electrode sheet according to an embodiment of the present application

图3是本申请一实施方式的二次电池的示意图。FIG. 3 is a schematic diagram of a secondary battery according to an embodiment of the present application.

图4是图3所示的本申请一实施方式的二次电池的分解图。FIG. 4 is an exploded view of the secondary battery according to one embodiment of the present application shown in FIG. 3 .

图5是本申请一实施方式的电池模块的示意图。FIG. 5 is a schematic diagram of a battery module according to an embodiment of the present application.

图6是本申请一实施方式的电池包的示意图。FIG. 6 is a schematic diagram of a battery pack according to an embodiment of the present application.

图7是图6所示的本申请一实施方式的电池包的分解图。FIG. 7 is an exploded view of the battery pack according to one embodiment of the present application shown in FIG. 6 .

图8是本申请一实施方式的二次电池用作用电装置的示意图。FIG. 8 is a schematic diagram of a secondary battery used as a power consumption device according to an embodiment of the present application.

附图标记说明:Explanation of reference signs:

1电池包;2上箱体;3下箱体;4电池模块;5二次电池;51壳体;52电极组件;53顶盖组件;6集流体;7单层负极膜层;8第一膜层;9第二膜层。1 battery pack; 2 upper box; 3 lower box; 4 battery module; 5 secondary battery; 51 shell; 52 electrode assembly; 53 top cover assembly; 6 current collector; film layer; 9 second film layer.

具体实施方式Detailed ways

以下,适当地参照附图详细说明具体公开了本申请的负极极片及其制造方法、正极极片、二次电池、电池模块、电池包和电学装置的实施方式。但是会有省略不必要的详细说明的情况。例如,有省略对已众所周知的事项的详细说明、实际相同结构的重复说明的情况。这是为了避免以下的说明不必要地变得冗长,便于本领域技术人员的理解。此外,附图及以下说明是为了本领域技术人员充分理解本申请而提供的,并不旨在限定权利要求书所记载的主题。Hereinafter, embodiments of the negative electrode sheet and its manufacturing method, positive electrode sheet, secondary battery, battery module, battery pack, and electrical device of the present application will be disclosed in detail with appropriate reference to the accompanying drawings. However, unnecessary detailed description may be omitted. For example, detailed descriptions of well-known items and repeated descriptions of substantially the same configurations may be omitted. This is to avoid the following description from becoming unnecessarily lengthy and to facilitate the understanding of those skilled in the art. In addition, the drawings and the following descriptions are provided for those skilled in the art to fully understand the present application, and are not intended to limit the subject matter described in the claims.

本申请所公开的“范围”以下限和上限的形式来限定,给定范围是通过选定一个下限和一个上限进行限定的,选定的下限和上限限定了特别范围的边界。这种方式进行限定的范围可以是包括端值或不包括端值的,并且可以进行任意地组合,即任何下限可以与任何上限组合形成一个范围。例如,如果针对特定参数列出了60-120和80-110的范围,理解为60-110和80-120的范围也是预料到的。此外,如果列出的最小范围值1和2,和如果列出了最大范围值3,4和5,则下面的范围可全部预料到:1-3、1-4、1-5、2-3、2-4和2-6。在本申请中,除非有其他说明,数值范围“a-b”表示a到b之间的任意实数组合的缩略表示,其中a和b都是实数。例如数值范围“0-5”表示本文中已经全部列出了“0-5”之间的全部实数,“0-5”只是这些数值组合的缩略表示。另外,当表述某个参数为≥2的整数,则相当于公开了该参数为例如整数2、3、4、5、6、7、8、9、10、11、12等。A "range" disclosed herein is defined in terms of lower and upper limits, and a given range is defined by selecting a lower limit and an upper limit that define the boundaries of the particular range. Ranges defined in this manner may be inclusive or exclusive and may be combined arbitrarily, ie any lower limit may be combined with any upper limit to form a range. For example, if ranges of 60-120 and 80-110 are listed for a particular parameter, it is understood that ranges of 60-110 and 80-120 are contemplated. Additionally, if the minimum range values 1 and 2 are listed, and if the maximum range values 3, 4, and 5 are listed, the following ranges are all expected: 1-3, 1-4, 1-5, 2- 3, 2-4 and 2-6. In this application, unless otherwise stated, the numerical range "a-b" represents an abbreviated representation of any combination of real numbers between a and b, where a and b are both real numbers. For example, the numerical range "0-5" indicates that all real numbers between "0-5" have been listed in this article, and "0-5" is only an abbreviated representation of the combination of these values. In addition, when expressing that a certain parameter is an integer ≥ 2, it is equivalent to disclosing that the parameter is an integer such as 2, 3, 4, 5, 6, 7, 8, 9, 10, 11, 12, etc.

如果没有特别的说明,本申请的所有实施方式以及可选实施方式可以相互组合形成新的技术方案。If there is no special description, all the implementation modes and optional implementation modes of the present application can be combined with each other to form new technical solutions.

如果没有特别的说明,本申请的所有技术特征以及可选技术特征可以相互组合形成新的技术方案。If there is no special description, all the technical features and optional technical features of the present application can be combined with each other to form a new technical solution.

如果没有特别的说明,本申请的所有步骤可以顺序进行,也可以随机进行,优选是顺序进行的。例如,所述方法包括步骤(a)和(b),表示所述方法可包括顺序进行的步骤(a)和(b),也可以包括顺序进行的步骤(b)和(a)。例如,所述提到所述方法还可包括步骤(c),表示步骤(c)可以任意顺序加入到所述方法,例如,所述方法可以包括步骤(a)、(b)和(c),也可包括步骤(a)、(c)和(b),也可以包括步骤(c)、(a)和(b)等。Unless otherwise specified, all steps in the present application can be performed sequentially or randomly, preferably sequentially. For example, the method includes steps (a) and (b), which means that the method may include steps (a) and (b) performed in sequence, and may also include steps (b) and (a) performed in sequence. For example, mentioning that the method may also include step (c) means that step (c) may be added to the method in any order, for example, the method may include steps (a), (b) and (c) , may also include steps (a), (c) and (b), may also include steps (c), (a) and (b) and so on.

如果没有特别的说明,本申请所提到的“包括”和“包含”表示开放式,也可以是封闭式。例如,所述“包括”和“包含”可以表示还可以包括或包含没有列出的其他组分,也可以仅包括或包含列出的组分。If there is no special description, the "comprising" and "comprising" mentioned in this application mean open or closed. For example, the "comprising" and "comprising" may mean that other components not listed may be included or included, or only listed components may be included or included.

如果没有特别的说明,在本申请中,术语“或”是包括性的。举例来说,短语“A或B”表示“A,B,或A和B两者”。更具体地,以下任一条件均满足条件“A或B”:A为真(或存在)并且B为假(或不存在);A为假(或不存在)而B为真(或存在);或A和B都为真(或存在)。In this application, the term "or" is inclusive unless otherwise stated. For example, the phrase "A or B" means "A, B, or both A and B." More specifically, the condition "A or B" is satisfied by either of the following: A is true (or exists) and B is false (or does not exist); A is false (or does not exist) and B is true (or exists) ; or both A and B are true (or exist).

随着新能源的快速发展,对锂离子电池的要求也越来越高,在追求能量密度的同时,为了缓解用户的里程焦虑,需要同时提高锂离子电池的充电能力。对于当前的体系,液相扩散是快速充电的瓶颈,因此大幅提升液相扩散对于改善充电能力至关重要。With the rapid development of new energy sources, the requirements for lithium-ion batteries are getting higher and higher. While pursuing energy density, in order to alleviate users' mileage anxiety, it is necessary to improve the charging capacity of lithium-ion batteries at the same time. For the current system, liquid phase diffusion is the bottleneck of fast charging, so a substantial increase in liquid phase diffusion is crucial to improve the charging capability.

现有的提高快充能力的方法有打孔和造孔技术,以及碳纳米管技术,但是均存在能量密度损失较大,储液、保液作用较小,比表面积大、副反应多等问题。Existing methods to improve fast charging capacity include drilling and hole-making technology, and carbon nanotube technology, but there are problems such as large energy density loss, small liquid storage and liquid retention, large specific surface area, and many side reactions. .

本发明人发现,通过在负极膜层中引入碳微米管,可以充分发挥储液、保液作用,从而提高液相扩散能力,实现锂离子贯穿整个负极膜层,以充分利用负极活性物质,尤其是靠近集流体的负极活性物质,达到改善电池的充电能力的目的。The inventors found that by introducing carbon microtubes into the negative electrode film, the liquid storage and liquid retention functions can be fully exerted, thereby improving the liquid phase diffusion ability, and realizing lithium ions running through the entire negative electrode film layer, so as to make full use of the negative electrode active material, especially It is a negative electrode active material close to the current collector to achieve the purpose of improving the charging capacity of the battery.

[负极极片][Negative pole piece]

本申请的第一方面提供了一种单层涂布的负极极片,其包括集流体以及设置在所述集流体的至少一个表面上的负极膜层,所述负极膜层包含负极活性物质和碳微米管,任选地包含导电剂;其中,碳微米管在负极膜层的质量分数W1与导电剂在负极膜层的质量分数W2满足:当0.2%≤W1≤2%时,则W1+W2≤2%;当W1>2%时,可选2%<W1<5.8%,则0≤W2≤0.5%,基于负极膜层的总重量计。The first aspect of the present application provides a single-layer coated negative electrode sheet, which includes a current collector and a negative electrode film layer arranged on at least one surface of the current collector, and the negative electrode film layer includes a negative electrode active material and Carbon microtubes, optionally including a conductive agent; wherein, the mass fraction W1 of the carbon microtubes in the negative electrode film layer and the mass fraction W2 of the conductive agent in the negative electrode film layer meet: when 0.2%≤W1≤2%, then W1+ W2≤2%; when W1>2%, optional 2%<W1<5.8%, then 0≤W2≤0.5%, based on the total weight of the negative film layer.

通过在本申请的负极膜层中加入碳微米管,能够改善负极膜层的保液能力,促进液相扩散,使活性物质被充分利用;同时,限定碳微米管和导电剂在负极膜层中的质量分数的配比,使电池具有良好的能量密度,电池的充电能力得以提升。本申请的单层涂布的负极极片如图1所示。By adding carbon microtubes in the negative electrode film layer of the present application, the liquid retention capacity of the negative electrode film layer can be improved, the liquid phase diffusion can be promoted, and the active material can be fully utilized; at the same time, carbon microtubes and conductive agents are limited in the negative electrode film layer The ratio of the mass fraction of the battery makes the battery have a good energy density, and the charging capacity of the battery is improved. The single-layer coated negative electrode sheet of the present application is shown in FIG. 1 .

在一些实施方式中,碳微米管在负极膜层的质量分数W1为0.2-5%。通过进一步限定碳微米管在负极膜层的质量分数,以优化负极膜层的组分,改善电池的快充能力。In some embodiments, the mass fraction W1 of carbon microtubes in the negative electrode film layer is 0.2-5%. By further limiting the mass fraction of carbon microtubes in the negative electrode film layer, the components of the negative electrode film layer are optimized to improve the fast charging capability of the battery.

在一些实施方式中,碳微米管的内径(即中空内腔的直径)为0.2μm至12μm,可选2μm至10μm;可选地,长径比(即碳纳米管的长度与内径的比例)为2-20;进一步可选地,碳微米管的管壁厚度为0.01μm至1μm。其中,碳微米管的内径还可选为1μm至12μm,或者2μm至4μm。In some embodiments, the inner diameter of the carbon nanotube (i.e. the diameter of the hollow cavity) is 0.2 μm to 12 μm, optionally 2 μm to 10 μm; optionally, the aspect ratio (i.e. the ratio of the length of the carbon nanotube to the inner diameter) is 2-20; further optionally, the wall thickness of the carbon microtubes is 0.01 μm to 1 μm. Wherein, the inner diameter of the carbon microtubes may also be 1 μm to 12 μm, or 2 μm to 4 μm.

上述规格的碳微米管类似于直通孔,其优点在于能够充分发挥储液和保液的作用,提高液相扩散能力,从而充分利用负极膜膜层的活性物质,提升电池的快充能力;而且,与现有技术中使用的造孔和打孔技术(内径为几十微米)相比,本申请的碳微米管的内径更小,甚至是几微米,其优势在于,碳微米管之间的距离较小且分布均匀,能够改善孔径分布的一致性,使得电芯内部的极化分布均匀,避免出现局部析锂的现象,同时也有效地起到保液的作用,整体提升充电能力,减小能量密度损失。与现有技术中使用的碳纳米管技术相比,本申请的碳微米管的内径较小,能够起到储液、保液的作用,提高锂离子的扩散能力。The carbon microtubes of the above specifications are similar to through-holes, and their advantages are that they can fully play the role of liquid storage and liquid retention, improve the liquid phase diffusion capacity, thereby making full use of the active material of the negative electrode film layer, and improving the fast charging capacity of the battery; and , compared with the pore-forming and punching technology used in the prior art (the inner diameter is tens of microns), the inner diameter of the carbon microtubes of the present application is smaller, even several microns, and its advantage is that the carbon microtubes The distance is small and the distribution is uniform, which can improve the consistency of the pore size distribution, make the polarization distribution inside the battery uniform, avoid the phenomenon of local lithium precipitation, and also effectively play the role of liquid retention, improve the charging capacity as a whole, reduce the Small energy density loss. Compared with the carbon nanotube technology used in the prior art, the inner diameter of the carbon nanotube of the present application is smaller, which can play the role of liquid storage and retention, and improve the diffusion capacity of lithium ions.

在一些实施方式中,负极膜层包含的负极活性物质包括人造石墨、天然石墨、硅基材料中的至少一种,可选地选自人造石墨;导电剂包括导电剂sp、KS-6、导电石墨、碳纳米管、石墨烯、碳纤维VGCF中的至少一种,可选导电剂sp。In some embodiments, the negative electrode active material contained in the negative electrode film layer includes at least one of artificial graphite, natural graphite, and silicon-based materials, optionally selected from artificial graphite; the conductive agent includes conductive agent sp, KS-6, conductive At least one of graphite, carbon nanotubes, graphene, carbon fiber VGCF, optional conductive agent sp.

在本申请的单层涂布的负极极片中,进一步可选地,负极膜层包含内径为2μm至4μm的碳微米管,所述碳微米管在所述负极膜层的质量分数W1与所述导电剂在所述负极膜层的质量分数W2满足:当1.5%≤W1≤2%时,则1.6%≤W1+W2≤2%;当2.5%≤W1≤3%时,则0≤W2≤0.5%,基于负极膜层的总重量计。In the single-layer coated negative electrode sheet of the present application, further optionally, the negative electrode film layer includes carbon microtubes with an inner diameter of 2 μm to 4 μm, and the mass fraction W1 of the carbon microtubes in the negative electrode film layer is equal to the The mass fraction W2 of the conductive agent in the negative electrode film layer satisfies: when 1.5%≤W1≤2%, then 1.6%≤W1+W2≤2%; when 2.5%≤W1≤3%, then 0≤W2 ≤0.5%, based on the total weight of the negative film layer.

本申请的第二方面提供了一种双层涂布的负极极片,其包括集流体、第一膜层和第二膜层,其中,第一膜层设置在集流体的至少一个表面上,第二膜层设置在第一膜层的外表面上;第一膜层位于所述集流体和所述第二膜层之间;而且,第一膜层包含第一负极活性物质;第二膜层包含第二负极活性物质;第一膜层和第二膜层中的至少一层包含碳微米管;以及第一膜层和第二膜层之间至少在负极活性物质、是否包括碳微米管,这二者之一不同。The second aspect of the present application provides a double-coated negative electrode sheet, which includes a current collector, a first film layer, and a second film layer, wherein the first film layer is disposed on at least one surface of the current collector, The second film layer is arranged on the outer surface of the first film layer; the first film layer is located between the current collector and the second film layer; and the first film layer contains the first negative active material; the second film The layer comprises the second negative electrode active material; at least one layer in the first film layer and the second film layer comprises carbon microtubes; , one of the two is different.

在本申请中,任选地,在集流体和第一膜层之间还包括中间涂层。该中间涂层用于增强负极活性物质和集流体之间的粘结力,加强电子的传输,降低极化。中间涂层的厚度不大于6μm,包括导电剂和粘结剂。其中,导电剂包括导电剂sp、KS-6、导电石墨、碳纳米管、石墨烯、碳纤维VGCF中的至少一种,粘结剂包括丁苯橡胶(SBR)、聚丙烯酸酯、乙丙橡胶、丁腈橡胶、聚偏氟丁烯(PVDF)中的至少一种。In this application, optionally, an intermediate coating is further included between the current collector and the first film layer. The intermediate coating is used to enhance the binding force between the negative electrode active material and the current collector, enhance electron transport, and reduce polarization. The thickness of the intermediate coating is not more than 6 μm, including conductive agent and binder. Wherein, the conductive agent includes at least one of conductive agent sp, KS-6, conductive graphite, carbon nanotubes, graphene, carbon fiber VGCF, and the binder includes styrene-butadiene rubber (SBR), polyacrylate, ethylene-propylene rubber, At least one of nitrile rubber and polybutylene fluoride (PVDF).

在本申请中,采用双层涂布工艺制成具有第一膜层和第二膜层的双层结构的负极膜层,如图2所示。该负极膜层的总厚度为25-110μm。In this application, a double-layer coating process is used to form a negative electrode film layer with a double-layer structure of a first film layer and a second film layer, as shown in FIG. 2 . The total thickness of the negative film layer is 25-110 μm.

需要说明的是,本申请所用的“第一膜层”、“第一层膜层”和“下层”具有相同的含义,是指靠近集流体的包含活性物质的那一层;“第二膜层”、“第二层膜层”和“上层”具有相同的含义,是指远离集流体的包含活性物质的那一层;“双层膜层”是指第一膜层和第二膜层;“总质量”是指某物质在第一膜层和第二膜层中的总的质量。It should be noted that the "first film layer", "first film layer" and "lower layer" used in this application have the same meaning, and refer to the layer containing the active material near the current collector; "the second film Layer", "second film layer" and "upper layer" have the same meaning, and refer to the layer that contains the active material away from the current collector; "double film layer" refers to the first film layer and the second film layer ; "total mass" refers to the total mass of a substance in the first film layer and the second film layer.

在本申请中,在双层涂布的负极极片中,特别是具有厚涂布重量(至少9mg/cm2)的负极极片中,通过加入碳微米管,有利于改善二次电池的快速充电能力。In the present application, in the double-layer coated negative electrode sheet, especially in the negative electrode sheet with a thick coating weight (at least 9mg/cm 2 ), it is beneficial to improve the rapidity of the secondary battery by adding carbon microtubes. charging capacity.

在一些实施方式中,在双层涂布的负极极片中,第一膜层不包含碳微米管,第二膜层包含碳微米管。这有利于增强电解液在第二膜层的储液能力,使第二膜层(上层)具有充足的电解液,以提高锂离子向第一膜层(下层)的扩散能力,促进锂离子扩散至集流体表面的膜层,达到充分利用负极活性物质的目的,提高电池的充电能力。In some embodiments, in the double-coated negative electrode sheet, the first film layer does not contain carbon microtubes, and the second film layer contains carbon microtubes. This is conducive to enhancing the liquid storage capacity of the electrolyte in the second film layer, so that the second film layer (upper layer) has sufficient electrolyte solution to improve the diffusion ability of lithium ions to the first film layer (lower layer) and promote the diffusion of lithium ions To the film layer on the surface of the current collector, the purpose of making full use of the negative electrode active material is achieved, and the charging capacity of the battery is improved.

在一些实施方式中,在双层涂布的负极极片中,第一膜层和第二膜层均包含碳微米管。由此,在负极极片的双层膜层中形成了通畅的锂离子通道,保证了从上层/电解液界面至下层/集流体界面的锂离子扩散路径,进一步提高锂离子从上层到下层的扩散深度和扩散速度,从而充分利用负极活性物质,提高电池的充电能力。In some embodiments, in the double-layer coated negative electrode sheet, both the first film layer and the second film layer contain carbon microtubes. As a result, a smooth lithium ion channel is formed in the double-layer film of the negative electrode sheet, which ensures the lithium ion diffusion path from the upper layer/electrolyte interface to the lower layer/current collector interface, and further improves the flow rate of lithium ions from the upper layer to the lower layer. Diffusion depth and diffusion speed, so as to make full use of the negative electrode active material and improve the charging capacity of the battery.

在一些实施方式中,在双层涂布的负极极片中,由第一膜层和第二膜层构成的双层膜层中,碳微米管的总质量分数W3为0.2%至5%,可选1.5%至3%,进一步可选1.8%至2.6%,基于第一膜层和第二膜层的总重量计。由此,进一步改善双层涂布的负极极片的充电能力。In some embodiments, in the double-layer coated negative electrode sheet, in the double-layer film layer composed of the first film layer and the second film layer, the total mass fraction W3 of carbon microtubes is 0.2% to 5%, Optionally 1.5% to 3%, further optional 1.8% to 2.6%, based on the total weight of the first film layer and the second film layer. As a result, the charging capability of the double-layer coated negative electrode sheet is further improved.

在一些实施方式中,在双层涂布的负极极片中,第一膜层和第二膜层任选地还包含导电剂;在第一膜层和第二膜层构成的双层膜层中,碳微米管的总质量分数W3与所述导电剂的总质量分数W4满足:当0.2%≤W3≤2%时,则W3+W4≤2%;当W3>2%时,则0≤W4≤0.5%,基于第一膜层和第二膜层的总质量计。In some embodiments, in the double-layer coated negative electrode sheet, the first film layer and the second film layer optionally further comprise a conductive agent; Among them, the total mass fraction W3 of carbon microtubes and the total mass fraction W4 of the conductive agent satisfy: when 0.2%≤W3≤2%, then W3+W4≤2%; when W3>2%, then 0≤ W4≤0.5%, based on the total mass of the first film layer and the second film layer.

通过限定在双层膜层中的碳微米管和导电剂的总质量分数满足特定的关系,二次电池能够在能量密度不受损的情况下,提升快速充电能力。也就是说,实现了负载物(碳微米管和导电剂)的量、能量密度和充电性能之间的平衡。By limiting the total mass fraction of the carbon microtubes and the conductive agent in the double-layer film layer to satisfy a specific relationship, the secondary battery can improve the fast charging capability without compromising the energy density. That is, a balance between the amount of loads (carbon microtubes and conductive agent), energy density, and charging performance is achieved.

在一些实施方式中,双层涂布的负极极片中,碳微米管在第二膜层的质量相对于碳微米管的总质量为50-100%。由此,碳微米管可以全部或大部分地存在于第二膜层中,这有利于更多的含锂离子的电解液扩散到上层,进而达到下层,以提高下层的锂离子扩散能力,实现充分利用下层活性物质的目的。In some embodiments, in the double-coated negative electrode sheet, the mass of the carbon microtubes in the second film layer is 50-100% relative to the total mass of the carbon microtubes. As a result, the carbon microtubes can all or mostly exist in the second film layer, which is conducive to the diffusion of more lithium-ion-containing electrolytes to the upper layer, and then to the lower layer, so as to improve the lithium ion diffusion capacity of the lower layer and realize The purpose of making full use of the active substances in the lower layer.

在一些实施方式中,双层涂布的负极极片中,碳微米管的内径为0.2μm至12μm,或者1μm至12μm,可选2μm至10μm,进一步可选2μm至4μm;其长径比为2-20,以及管壁厚度为0.01μm至1μm。In some embodiments, in the double-layer coated negative electrode sheet, the carbon microtubes have an inner diameter of 0.2 μm to 12 μm, or 1 μm to 12 μm, optionally 2 μm to 10 μm, and further optionally 2 μm to 4 μm; the aspect ratio is 2-20, and the tube wall thickness is 0.01μm to 1μm.

通过选择特定规格的碳微米管,进一步优化碳微米管的储液和保液作用,促进电解液的扩散,从而更加充分地利用负极活性物质,并且加快锂离子的脱嵌,达到进一步提升电池的快充能力的目的。尤其是限定碳微米管地内径为0.2μm至12μm,使碳微米管之间的距离较小且均匀分布,从而保证了孔径分布的均匀,电芯内部的极化分布均匀,避免出现局部析锂的现象,并且能量密度损失较小,充电能力得以进一步提升。By selecting carbon microtubes of specific specifications, the liquid storage and liquid retention functions of carbon microtubes are further optimized, and the diffusion of electrolyte is promoted, so that the negative electrode active material can be more fully utilized, and the deintercalation of lithium ions can be accelerated to further improve the performance of the battery. The purpose of fast charging capability. In particular, the inner diameter of the carbon microtubes is limited to 0.2 μm to 12 μm, so that the distance between the carbon microtubes is small and evenly distributed, thereby ensuring uniform pore size distribution, uniform polarization distribution inside the battery cell, and avoiding localized lithium deposition. The phenomenon, and the loss of energy density is small, and the charging capacity can be further improved.

在一些实施方式中,双层涂布的负极极片中,在只有第二膜层包含碳微米管,并且在第一膜层和第二膜层中任选地还包含导电剂的条件下,第二膜层中碳微米管的质量分数为0.4%至10%,以及导电剂的质量分数为为0%至4%,可选地0%至1.6%,基于第二膜层的重量计;第一膜层中的导电剂的质量分数为0%至4%,可选地0%至2%,又可选地0.4%至2%,基于第一膜层的重量计。In some embodiments, in the double-layer coated negative electrode sheet, under the condition that only the second film layer contains carbon microtubes, and optionally also includes a conductive agent in the first film layer and the second film layer, The mass fraction of carbon microtubes in the second film layer is 0.4% to 10%, and the mass fraction of the conductive agent is 0% to 4%, optionally 0% to 1.6%, based on the weight of the second film layer; The mass fraction of the conductive agent in the first film layer is 0% to 4%, optionally 0% to 2%, and optionally 0.4% to 2%, based on the weight of the first film layer.

在一些实施方式中,双层涂布的负极极片中,在第一膜层和第二膜层中均包含碳微米管,并且在第一膜层和第二膜层中任选地还包含导电剂的条件下,所述碳微米管在各膜层中的质量分数为0.2%至5%,并且所述导电剂在各膜层中的质量分数为0%至2%,基于各膜层的重量计。由此,优化负极极片的组成、结构,实现二次电池的快充能力最佳化。In some embodiments, in the double-layer coated negative electrode sheet, carbon microtubes are included in both the first film layer and the second film layer, and optionally also include carbon microtubes in the first film layer and the second film layer Under the condition of the conductive agent, the mass fraction of the carbon microtubes in each film layer is 0.2% to 5%, and the mass fraction of the conductive agent in each film layer is 0% to 2%, based on each film layer weight gauge. Thus, the composition and structure of the negative pole piece are optimized, and the fast charging capability of the secondary battery is optimized.

可选地,负极极片中的碳微米管在所述第二膜层与在第一膜层中的质量分数比10:3至1:1。通过进一步限定碳微米管在这两层膜层的质量分数配比,使电解液在朝向集流体方向上的扩散的深度增加,同时有效地发挥保液作用,从而达到充分利用负极活性物质的目的,改善电池的快充能力。Optionally, the mass fraction ratio of carbon microtubes in the second film layer to that in the first film layer in the negative electrode sheet is 10:3 to 1:1. By further limiting the mass fraction ratio of carbon microtubes in the two layers of film, the depth of diffusion of the electrolyte in the direction of the current collector is increased, and at the same time, the liquid retention effect is effectively exerted, so as to achieve the purpose of making full use of the negative electrode active material , to improve the fast charging capability of the battery.

可选地,负极极片中的第二膜层与第一膜层的重量比为1:4至4:1。该重量比是指第二膜层与第一膜层的涂布重量之比。由此进一步优化负极极片的结构,使涂布工艺简单、易操作,同时提升电池的快充能力。Optionally, the weight ratio of the second film layer to the first film layer in the negative electrode sheet is 1:4 to 4:1. The weight ratio refers to the ratio of the coating weight of the second film layer to that of the first film layer. In this way, the structure of the negative electrode sheet is further optimized, the coating process is simple and easy to operate, and the fast charging capacity of the battery is improved at the same time.

在一些实施方式中,在第一膜层和第二膜层中,第一和第二负极活性物质可为相同或不同的,包括人造石墨、天然石墨、硅基材料中的至少一种;可选地,第一膜层中的第一负极活性物质可为人造石墨a,中值粒径DV50在20-25μm,第二膜层中的第二负极活性物质可为人造石墨b,中值粒径DV50在10-14μm。In some embodiments, in the first film layer and the second film layer, the first and second negative electrode active materials can be the same or different, including at least one of artificial graphite, natural graphite, and silicon-based materials; Optionally, the first negative electrode active material in the first film layer can be artificial graphite a, with a median particle size DV50 of 20-25 μm, and the second negative electrode active material in the second film layer can be artificial graphite b, with a median particle diameter The diameter DV50 is 10-14μm.

在一些实施方式中,在第一膜层和第二膜层中,任选地包含导电剂的条件下,导电剂可为相同或不同的,包括导电剂sp、KS-6、导电石墨、碳纳米管、石墨烯、碳纤维VGCF中的至少一种。In some embodiments, under the condition that the conductive agent is optionally included in the first film layer and the second film layer, the conductive agent can be the same or different, including conductive agent sp, KS-6, conductive graphite, carbon At least one of nanotubes, graphene, carbon fiber VGCF.

在本申请中,集流体没有特别限制,可采用金属箔片或复合集流体。例如,作为金属箔片,可以采用铜箔。复合集流体可包括高分子材料基层和形成于高分子材料基材至少一个表面上的金属层。复合集流体可通过将金属材料(铜、铜合金、镍、镍合金、钛、钛合金、银及银合金等)形成在高分子材料基材(如聚丙烯(PP)、聚对苯二甲酸乙二醇酯(PET)、聚对苯二甲酸丁二醇酯(PBT)、聚苯乙烯(PS)、聚乙烯(PE)等的基材)上而形成。In this application, the current collector is not particularly limited, and a metal foil or a composite current collector can be used. For example, copper foil can be used as the metal foil. The composite current collector may include a base layer of polymer material and a metal layer formed on at least one surface of the base material of polymer material. Composite current collectors can be formed by metal materials (copper, copper alloys, nickel, nickel alloys, titanium, titanium alloys, silver and silver alloys, etc.) on polymer material substrates (such as polypropylene (PP), polyethylene terephthalic acid It is formed on substrates such as ethylene glycol ester (PET), polybutylene terephthalate (PBT), polystyrene (PS), polyethylene (PE), etc.).

在本申请中,负极膜层、第一膜层和第二膜层还可选地包括粘结剂。所述粘结剂包括丁苯橡胶(SBR)、聚丙烯酸酯、乙丙橡胶、丁腈橡胶、聚偏氟丁烯(PVDF)中的至少一种,可选丁苯橡胶。这有利于获得更好的粘结性能。In the present application, the negative electrode film layer, the first film layer and the second film layer may also optionally include a binder. The binder includes at least one of styrene-butadiene rubber (SBR), polyacrylate, ethylene-propylene rubber, nitrile rubber, and polybutylene fluoride (PVDF), and styrene-butadiene rubber is optional. This facilitates better bonding properties.

在本申请中,负极膜层、第一膜层和第二膜层还可选地包括分散剂。所述分散剂包括羧甲基纤维素钠(CMC-Na)、甲基纤维素、乙基纤维素的至少一种;可选地,羧甲基纤维素钠。这有利于获得更好的分散性能。In the present application, the negative electrode film layer, the first film layer and the second film layer may also optionally include a dispersant. The dispersant includes at least one of carboxymethylcellulose sodium (CMC-Na), methylcellulose, and ethylcellulose; optionally, sodium carboxymethylcellulose. This facilitates better dispersion properties.

制备方法Preparation

在本申请中,碳微米管的制备方法如下:In this application, the preparation method of carbon microtubes is as follows:

将含有聚苯乙烯的前驱液进行静电纺丝,得到纳米纤维丝,将纳米纤维丝均匀分散到含有吡咯等的盐酸溶液中,吡咯和纳米纤维丝的质量比为0.8:1至1.2:1,加入过硫酸铵进行聚合反应,过硫酸铵的质量为纳米纤维丝的1.1-1.3倍,得到表面包覆聚合物的纳米纤维丝,再向上述表面包覆的聚合物纳米纤维丝中加入四氢呋喃,四氢呋喃的质量为纳米纤维丝的8-22倍,充分搅拌,溶解聚苯乙烯,即得到中空的聚合物管,经过280-320℃预烧结1-3h和1100-1300℃炭化3-5h,冷却后就得到微米级碳管。The precursor solution containing polystyrene is electrospun to obtain nanofibers, and the nanofibers are evenly dispersed in a hydrochloric acid solution containing pyrrole, etc., and the mass ratio of pyrrole to nanofibers is 0.8:1 to 1.2:1, Adding ammonium persulfate to carry out polymerization reaction, the quality of ammonium persulfate is 1.1-1.3 times of the nanofiber silk, obtains the nanofiber silk of surface coating polymer, then adds tetrahydrofuran to the polymer nanofiber silk of above-mentioned surface coating, The quality of tetrahydrofuran is 8-22 times that of nanofibers. Stir thoroughly to dissolve polystyrene to obtain a hollow polymer tube. After pre-sintering at 280-320°C for 1-3h and carbonization at 1100-1300°C for 3-5h, cool After that, micron-sized carbon tubes are obtained.

其中,通过采用不同质量比的四氢呋喃与纳米纤维丝,可以得到本申请所述的不同内径的碳微米管。Wherein, the carbon microtubes with different inner diameters described in this application can be obtained by using different mass ratios of tetrahydrofuran and nanofiber filaments.

在本申请中,单层涂布和双层涂布的负极极片按照本领域的常规方法制备。In this application, single-layer coated and double-coated negative electrode sheets are prepared according to conventional methods in the art.

单层涂布的负极极片通过常规的单层涂布工艺制备,具体方法如下:The single-layer coated negative electrode sheet is prepared by a conventional single-layer coating process, and the specific method is as follows:

S1:将负极膜层的原料组分,例如负极活性物质、导电剂、粘结剂、分散剂和/或碳微米管,按照一定比例加入溶剂(例如水或者去离子水)中物混,搅拌均匀后形成负极浆料;S1: Add the raw material components of the negative electrode film layer, such as negative electrode active materials, conductive agents, binders, dispersants and/or carbon microtubes, into a solvent (such as water or deionized water) in a certain proportion, mix, and stir Negative electrode slurry is formed after uniformity;

S2:将负极浆料涂布到负极集流体的至少一个表面上,经过烘干、压实后,即得到本申请的单层涂布的负极极片。S2: Coating the negative electrode slurry on at least one surface of the negative electrode current collector, drying and compacting to obtain the single-layer coated negative electrode sheet of the present application.

其中,上述负极浆料形成的那一层称为负极膜层。Wherein, the layer formed by the above-mentioned negative electrode slurry is called the negative electrode film layer.

任选地,在上述负极集流体和负极膜层之间还可以包括中间涂层,该中间涂层在步骤S2之前形成,通过将导电剂(Sp、KS-6或碳纳米管)与粘结剂(丁苯橡胶(SBR)、聚丙烯酸酯、乙丙橡胶、丁腈橡胶或聚偏氟丁烯(PVDF))按照一定比例混合制成浆料,然后涂覆到集流体的至少一个表面上获得上述中间涂层,其厚度不大于6μm。Optionally, an intermediate coating may also be included between the above-mentioned negative electrode current collector and the negative electrode film layer, and the intermediate coating is formed before step S2 by combining a conductive agent (Sp, KS-6 or carbon nanotubes) with Agent (styrene-butadiene rubber (SBR), polyacrylate, ethylene-propylene rubber, nitrile rubber or polyvinylidene fluoride (PVDF)) is mixed according to a certain proportion to make a slurry, and then coated on at least one surface of the current collector The above-mentioned intermediate coating is obtained, the thickness of which is not more than 6 μm.

在本申请中,双层涂布的负极极片通过常规的双层涂布工艺制备,具体方法如下:In this application, the double-layer coated negative electrode sheet is prepared by a conventional double-layer coating process, and the specific method is as follows:

P1:将制备第一膜层的原料组分,例如第一负极活性物质、导电剂、粘结剂、分散剂和/或碳微米管,按照一定比例加入溶剂(水或者去离子水)中物混,搅拌均匀后形成第一膜层的浆料,也称为下层浆料;P1: The raw material components for preparing the first film layer, such as the first negative electrode active material, conductive agent, binder, dispersant and/or carbon microtubes, are added to the solvent (water or deionized water) in a certain proportion Mix, and form the slurry of the first film layer after stirring evenly, also known as the lower layer slurry;

P2:将制备第二膜层的原料组分,例如负极活性物质、导电剂、粘结剂、分散剂和/或碳微米管,按照一定比例加入溶剂(水或者去离子水)中物混,搅拌均匀后形成第二膜层的浆料,也称为上层浆料;P2: The raw material components for preparing the second film layer, such as negative electrode active material, conductive agent, binder, dispersant and/or carbon microtubes, are mixed in a solvent (water or deionized water) according to a certain proportion, After stirring evenly, the slurry forming the second film layer is also called the upper layer slurry;

P3:将上述P1制备的下层浆料涂布到负极集流体的至少一个表面上,制成第一膜层(下层)。然后将上述P2制备的上层浆料涂布到第一膜层的表面上,经过烘干、压实后,即得到第二膜层(上层)。由此,制备本申请的双层涂布的负极极片。P3: Coating the lower layer slurry prepared in the above P1 on at least one surface of the negative electrode current collector to form the first film layer (lower layer). Then apply the upper layer slurry prepared in P2 above to the surface of the first film layer, and after drying and compacting, the second film layer (upper layer) is obtained. Thus, the double-coated negative electrode sheet of the present application was prepared.

任选地,在上述负极集流体和第一膜层之间还可以包括中间涂层,该中间涂层预先在步骤P3之前形成,通过将导电剂(Sp、KS-6或碳纳米管)与粘结剂(丁苯橡胶(SBR)、聚丙烯酸酯、乙丙橡胶、丁腈橡胶或聚偏氟丁烯(PVDF))按照一定比例混合制成浆料,然后涂覆到集流体的至少一个表面上获得上述中间涂层,其厚度不大于6μm。Optionally, an intermediate coating may also be included between the above-mentioned negative electrode current collector and the first film layer, which is formed before step P3 by mixing a conductive agent (Sp, KS-6 or carbon nanotubes) with The binder (styrene-butadiene rubber (SBR), polyacrylate, ethylene-propylene rubber, nitrile rubber or polyvinylidene fluoride (PVDF)) is mixed in a certain proportion to make a slurry, and then coated on at least one of the current collectors The above-mentioned intermediate coating is obtained on the surface, the thickness of which is not more than 6 μm.

应理解,本申请的负极极片,不仅可以用于二次电池,也可以用于任何其他需要提升快充能力的任何电池、电池模块、电池包或用电装置。It should be understood that the negative electrode sheet of the present application can be used not only for secondary batteries, but also for any other batteries, battery modules, battery packs or electrical devices that need to improve the fast charging capability.

二次电池secondary battery

下文对本申请的二次电池、电池模块、电池包和用电装置进行说明。The secondary battery, battery module, battery pack and electric device of the present application are described below.

二次电池secondary battery

本申请的一个实施方式中,提供一种二次电池,其中包括本申请的负极极片。In one embodiment of the present application, a secondary battery is provided, which includes the negative electrode sheet of the present application.

通常情况下,二次电池包括正极极片、负极极片、电解质和隔离膜。在电池充放电过程中,活性离子在正极极片和负极极片之间往返嵌入和脱出。电解质在正极极片和负极极片之间起到传导离子的作用。隔离膜设置在正极极片和负极极片之间,主要起到防止正负极短路的作用,同时可以使离子通过。Typically, a secondary battery includes a positive pole piece, a negative pole piece, an electrolyte, and a separator. During the charging and discharging process of the battery, active ions are intercalated and extracted back and forth between the positive electrode and the negative electrode. The electrolyte plays the role of conducting ions between the positive pole piece and the negative pole piece. The separator is arranged between the positive pole piece and the negative pole piece, which mainly plays a role in preventing the short circuit of the positive and negative poles, and at the same time allows ions to pass through.

[正极极片][Positive pole piece]

正极极片包括正极集流体以及设置在正极集流体至少一个表面的正极膜层,所述正极膜层包括正极活性材料。The positive electrode sheet includes a positive electrode collector and a positive electrode film layer arranged on at least one surface of the positive electrode collector, and the positive electrode film layer includes a positive electrode active material.

作为示例,正极集流体具有在其自身厚度方向相对的两个表面,正极膜层设置在正极集流体相对的两个表面的其中任意一者或两者上。As an example, the positive electrode current collector has two opposing surfaces in its own thickness direction, and the positive electrode film layer is disposed on any one or both of the two opposing surfaces of the positive electrode current collector.

在一些实施方式中,所述正极集流体可采用金属箔片或复合集流体。例如,作为金属箔片,可采用铝箔。复合集流体可包括高分子材料基层和形成于高分子材料基层至少一个表面上的金属层。复合集流体可通过将金属材料(铝、铝合金、镍、镍合金、钛、钛合金、银及银合金等)形成在高分子材料基材(如聚丙烯(PP)、聚对苯二甲酸乙二醇酯(PET)、聚对苯二甲酸丁二醇酯(PBT)、聚苯乙烯(PS)、聚乙烯(PE)等的基材)上而形成。In some embodiments, the positive electrode current collector can be a metal foil or a composite current collector. For example, aluminum foil can be used as the metal foil. The composite current collector may include a polymer material base and a metal layer formed on at least one surface of the polymer material base. The composite current collector can be formed by forming metal materials (aluminum, aluminum alloy, nickel, nickel alloy, titanium, titanium alloy, silver and silver alloy, etc.) on a polymer material substrate (such as polypropylene (PP), polyethylene terephthalic acid It is formed on substrates such as ethylene glycol ester (PET), polybutylene terephthalate (PBT), polystyrene (PS), polyethylene (PE), etc.).

在一些实施方式中,正极活性材料可采用本领域公知的用于电池的正极活性材料。作为示例,正极活性材料可包括以下材料中的至少一种:橄榄石结构的含锂磷酸盐、锂过渡金属氧化物及其各自的改性化合物。但本申请并不限定于这些材料,还可以使用其他可被用作电池正极活性材料的传统材料。这些正极活性材料可以仅单独使用一种,也可以将两种以上组合使用。其中,锂过渡金属氧化物的示例可包括但不限于锂钴氧化物(如LiCoO2)、锂镍氧化物(如LiNiO2)、锂锰氧化物(如LiMnO2、LiMn2O4)、锂镍钴氧化物、锂锰钴氧化物、锂镍锰氧化物、锂镍钴锰氧化物(如LiNi1/3Co1/3Mn1/3O2(也可以简称为NCM333)、LiNi0.5Co0.2Mn0.3O2(也可以简称为NCM523)、LiNi0.5Co0.25Mn0.25O2(也可以简称为NCM211)、LiNi0.6Co0.2Mn0.2O2(也可以简称为NCM622)、LiNi0.8Co0.1Mn0.1O2(也可以简称为NCM811)、锂镍钴铝氧化物(如LiNi0.85Co0.15Al0.05O2)及其改性化合物等中的至少一种。橄榄石结构的含锂磷酸盐的示例可包括但不限于磷酸铁锂(如LiFePO4(也可以简称为LFP))、磷酸铁锂与碳的复合材料、磷酸锰锂(如LiMnPO4)、磷酸锰锂与碳的复合材料、磷酸锰铁锂、磷酸锰铁锂与碳的复合材料中的至少一种。In some embodiments, the positive electrode active material may be a positive electrode active material known in the art for batteries. As an example, the positive active material may include at least one of the following materials: olivine-structured lithium-containing phosphate, lithium transition metal oxide, and their respective modified compounds. However, the present application is not limited to these materials, and other conventional materials that can be used as positive electrode active materials of batteries can also be used. These positive electrode active materials may be used alone or in combination of two or more. Among them, examples of lithium transition metal oxides may include, but are not limited to, lithium cobalt oxides (such as LiCoO 2 ), lithium nickel oxides (such as LiNiO 2 ), lithium manganese oxides (such as LiMnO 2 , LiMn 2 O 4 ), lithium Nickel cobalt oxide, lithium manganese cobalt oxide, lithium nickel manganese oxide, lithium nickel cobalt manganese oxide (such as LiNi 1/3 Co 1/3 Mn 1/3 O 2 (also referred to as NCM 333 ), LiNi 0.5 Co 0.2 Mn 0.3 O 2 (also abbreviated as NCM 523 ), LiNi 0.5 Co 0.25 Mn 0.25 O 2 (also abbreviated as NCM 211 ), LiNi 0.6 Co 0.2 Mn 0.2 O 2 (also abbreviated as NCM 622 ), LiNi At least one of 0.8 Co 0.1 Mn 0.1 O 2 (also referred to as NCM 811 ), lithium nickel cobalt aluminum oxide (such as LiNi 0.85 Co 0.15 Al 0.05 O 2 ) and its modified compounds. The olivine structure contains Examples of lithium phosphates may include, but are not limited to, lithium iron phosphate (such as LiFePO 4 (also may be abbreviated as LFP)), composite materials of lithium iron phosphate and carbon, lithium manganese phosphate (such as LiMnPO 4 ), lithium manganese phosphate and carbon At least one of a composite material, lithium manganese iron phosphate, and a composite material of lithium manganese iron phosphate and carbon.

在一些实施方式中,正极膜层还可选地包括粘结剂。作为示例,所述粘结剂可以包括聚偏氟乙烯(PVDF)、聚四氟乙烯(PTFE)、偏氟乙烯-四氟乙烯-丙烯三元共聚物、偏氟乙烯-六氟丙烯-四氟乙烯三元共聚物、四氟乙烯-六氟丙烯共聚物及含氟丙烯酸酯树脂中的至少一种。In some embodiments, the positive electrode film layer may further optionally include a binder. As an example, the binder may include polyvinylidene fluoride (PVDF), polytetrafluoroethylene (PTFE), vinylidene fluoride-tetrafluoroethylene-propylene terpolymer, vinylidene fluoride-hexafluoropropylene-tetrafluoroethylene At least one of ethylene terpolymer, tetrafluoroethylene-hexafluoropropylene copolymer and fluorine-containing acrylate resin.

在一些实施方式中,正极膜层还可选地包括导电剂。作为示例,所述导电剂可以包括超导碳、乙炔黑、炭黑、科琴黑、碳点、碳纳米管、石墨烯及碳纳米纤维中的至少一种。In some embodiments, the positive electrode film layer may also optionally include a conductive agent. As an example, the conductive agent may include at least one of superconducting carbon, acetylene black, carbon black, Ketjen black, carbon dots, carbon nanotubes, graphene, and carbon nanofibers.

在一些实施方式中,可以通过以下方式制备正极极片:将上述用于制备正极极片的组分,例如正极活性材料、导电剂、粘结剂和任意其他的组分分散于溶剂(例如N-甲基吡咯烷酮)中,形成正极浆料;将正极浆料涂覆在正极集流体上,经烘干、冷压等工序后,即可得到正极极片。In some embodiments, the positive electrode sheet can be prepared in the following manner: the above-mentioned components used to prepare the positive electrode sheet, such as positive electrode active material, conductive agent, binder and any other components, are dispersed in a solvent (such as N -methylpyrrolidone) to form a positive electrode slurry; the positive electrode slurry is coated on the positive electrode current collector, and after drying, cold pressing and other processes, the positive electrode sheet can be obtained.

[电解质][Electrolyte]

电解质在正极极片和负极极片之间起到传导离子的作用。本申请对电解质的种类没有具体的限制,可根据需求进行选择。例如,电解质可以选自固态电解质及液态电解质(即电解液)中的至少一种。The electrolyte plays the role of conducting ions between the positive pole piece and the negative pole piece. The present application has no specific limitation on the type of electrolyte, which can be selected according to requirements. For example, the electrolyte may be selected from at least one of solid electrolytes and liquid electrolytes (ie, electrolytic solutions).

在一些实施方式中,所述电解质采用电解液。所述电解液包括电解质盐和溶剂。In some embodiments, the electrolyte is an electrolytic solution. The electrolytic solution includes an electrolytic salt and a solvent.

在一些实施方式中,电解质盐可选自六氟磷酸锂(LiPF6)、四氟硼酸锂(LiBF4)、高氯酸锂(LiClO4)、六氟砷酸锂(LiAsF6)、双氟磺酰亚胺锂(LiFSI)、双三氟甲磺酰亚胺锂(LiTFSI)、三氟甲磺酸锂(LiTFS)、二氟草酸硼酸锂(LiDFOB)、二草酸硼酸锂(LiBOB)、二氟磷酸锂(LiPO2F2)、二氟二草酸磷酸锂(LiDFOP)及四氟草酸磷酸锂(LiTFOP)中的一种或几种。In some embodiments, the electrolyte salt may be selected from lithium hexafluorophosphate (LiPF 6 ), lithium tetrafluoroborate (LiBF 4 ), lithium perchlorate (LiClO 4 ), lithium hexafluoroarsenate (LiAsF 6 ), difluorosulfonyl Lithium amide (LiFSI), lithium bistrifluoromethanesulfonyl imide (LiTFSI), lithium trifluoromethanesulfonate (LiTFS), lithium difluorooxalate borate (LiDFOB), lithium difluorooxalate borate (LiBOB), lithium difluorophosphate (LiPO 2 F 2 ), lithium difluorooxalate phosphate (LiDFOP) and lithium tetrafluorooxalate phosphate (LiTFOP).

在一些实施方式中,溶剂可选自碳酸亚乙酯(EC)、碳酸亚丙酯(PC)、碳酸甲乙酯(EMC)、碳酸二乙酯(DEC)、碳酸二甲酯(DMC)、碳酸二丙酯(DPC)、碳酸甲丙酯(MPC)、碳酸乙丙酯(EPC)、碳酸亚丁酯(BC)、氟代碳酸亚乙酯(FEC)、甲酸甲酯(MF)、乙酸甲酯(MA)、乙酸乙酯(EA)、乙酸丙酯(PA)、丙酸甲酯(MP)、丙酸乙酯(EP)、丙酸丙酯(PP)、丁酸甲酯(MB)、丁酸乙酯(EB)、1,4-丁内酯(GBL)、环丁砜(SF)、二甲砜(MSM)、甲乙砜(EMS)及二乙砜(ESE)中的一种或几种。In some embodiments, the solvent may be selected from ethylene carbonate (EC), propylene carbonate (PC), ethyl methyl carbonate (EMC), diethyl carbonate (DEC), dimethyl carbonate (DMC), Dipropyl Carbonate (DPC), Methyl Propyl Carbonate (MPC), Ethyl Propyl Carbonate (EPC), Butylene Carbonate (BC), Fluoroethylene Carbonate (FEC), Methyl Formate (MF), Methyl Acetate Ester (MA), Ethyl Acetate (EA), Propyl Acetate (PA), Methyl Propionate (MP), Ethyl Propionate (EP), Propyl Propionate (PP), Methyl Butyrate (MB) , ethyl butyrate (EB), 1,4-butyrolactone (GBL), sulfolane (SF), dimethyl sulfone (MSM), methyl ethyl sulfone (EMS) and diethyl sulfone (ESE) kind.

在一些实施方式中,电解液中还可选地包括添加剂。例如添加剂可以包括负极成膜添加剂,也可以包括正极成膜添加剂,还可以包括能够改善电池某些性能的添加剂,例如改善电池过充性能的添加剂、改善电池高温性能的添加剂、改善电池低温性能的添加剂等。In some embodiments, additives are optionally included in the electrolyte. For example, additives can include negative electrode film-forming additives, positive electrode film-forming additives, and additives that can improve certain performances of batteries, such as additives that improve battery overcharge performance, additives that improve battery high-temperature performance, and additives that improve battery low-temperature performance. Additives etc.

[隔离膜][Isolation film]

在一些实施方式中,二次电池中还包括隔离膜。隔离膜设置在正极极片和负极极片之间起到隔离的作用。本申请对隔离膜的种类没有特别的限制,可以选用任意公知的具有良好的化学稳定性和机械稳定性的多孔结构隔离膜。In some embodiments, a separator is further included in the secondary battery. The separator is arranged between the positive pole piece and the negative pole piece to play the role of isolation. The present application has no particular limitation on the type of the isolation membrane, and any known porous structure isolation membrane with good chemical stability and mechanical stability can be selected.

在一些实施方式中,隔离膜的材质可选自玻璃纤维、无纺布、聚乙烯、聚丙烯及聚偏二氟乙烯中的至少一种。隔离膜可以是单层薄膜,也可以是多层复合薄膜,没有特别限制。在隔离膜为多层复合薄膜时,各层的材料可以相同或不同,没有特别限制。In some embodiments, the material of the isolation film can be selected from at least one of glass fiber, non-woven fabric, polyethylene, polypropylene and polyvinylidene fluoride. The separator can be a single-layer film or a multi-layer composite film, without any particular limitation. When the separator is a multilayer composite film, the materials of each layer may be the same or different, and there is no particular limitation.

[外包装][outer packaging]

在一些实施方式中,二次电池可以包括外包装,用于封装正极极片、负极极片和电解质。作为一个示例,正极极片、负极极片和隔离膜可经叠片或卷绕形成叠片结构电芯或卷绕结构电芯,电芯封装在外包装内;电解质可采用电解液,电解液浸润于电芯中。二次电池中电芯的数量可以为一个或几个,可以根据需求来调节。In some embodiments, the secondary battery may include an outer package for encapsulating the positive electrode tab, the negative electrode tab, and the electrolyte. As an example, the positive pole piece, the negative pole piece and the separator can be laminated or wound to form a laminated structure cell or a wound structure cell, and the cell is packaged in the outer package; the electrolyte can be electrolyte, and the electrolyte can be infiltrated in the cell. The number of cells in the secondary battery can be one or several, and can be adjusted according to requirements.

在一个实施方式中,本申请提供一种电极组件。在一些实施方式中,正极极片、负极极片和隔离膜可通过卷绕工艺或叠片工艺制成电极组件。所述外包装可用于封装上述电极组件及电解质。In one embodiment, the present application provides an electrode assembly. In some embodiments, the positive pole piece, the negative pole piece and the separator can be made into an electrode assembly through a winding process or a lamination process. The outer packaging can be used to package the above-mentioned electrode assembly and electrolyte.

在一些实施方式中,二次电池的外包装可以是软包,例如袋式软包。软包的材质可以是塑料,如可包括聚丙烯(PP)、聚对苯二甲酸丁二醇酯(PBT)、聚丁二酸丁二醇酯(PBS)等中的一种或几种。在一些实施方式中,二次电池的外包装可以是硬壳,例如硬塑料壳、铝壳、钢壳等。In some embodiments, the outer package of the secondary battery may be a soft bag, such as a pouch-type soft bag. The material of the soft bag can be plastic, such as one or more of polypropylene (PP), polybutylene terephthalate (PBT), polybutylene succinate (PBS), etc. can be included. In some embodiments, the outer packaging of the secondary battery may be a hard case, such as a hard plastic case, aluminum case, steel case, and the like.

二次电池的制备方法Preparation method of secondary battery

在一个实施方式中,本申请提供一种二次电池的制备方法,其中,使用本申请的第一方面和/或第二方面所述的负极极片。In one embodiment, the present application provides a method for preparing a secondary battery, wherein the negative electrode sheet described in the first aspect and/or the second aspect of the present application is used.

二次电池的制备还可以包括将本申请的负极极片、正极极片和电解质组装形成二次电池的步骤。在一些实施方式中,可将正极极片、隔离膜、负极极片按顺序卷绕或叠片,使隔离膜处于正极极片与负极极片之间起到隔离的作用,得到电芯。将电芯置于外包装中,注入电解液并封口,得到二次电池。The preparation of the secondary battery may also include the step of assembling the negative electrode sheet, the positive electrode sheet and the electrolyte of the present application to form a secondary battery. In some embodiments, the positive electrode sheet, the separator, and the negative electrode sheet can be sequentially wound or laminated, so that the separator is placed between the positive electrode sheet and the negative electrode sheet for isolation, and a battery cell is obtained. Put the battery cell in the outer package, inject the electrolyte and seal it to obtain the secondary battery.

在一些实施方式中,二次电池的制备还可以包括制备正极极片的步骤。作为示例,可以将正极活性物质、导电剂和粘结剂分散于溶剂(例如N-甲基吡咯烷酮,简称NMP)中,形成均匀的正极浆料;将正极浆料涂覆在正极集流体上,经烘干、冷压等工序后,得到正极极片。In some embodiments, the preparation of the secondary battery may further include the step of preparing a positive electrode sheet. As an example, the positive electrode active material, conductive agent and binder can be dispersed in a solvent (such as N-methylpyrrolidone, referred to as NMP) to form a uniform positive electrode slurry; the positive electrode slurry is coated on the positive electrode current collector, After drying, cold pressing and other processes, the positive electrode sheet is obtained.

在一些实施方式中,二次电池的制备包括根据本申请所述的方法制备负极极片的步骤。In some embodiments, the preparation of the secondary battery includes the step of preparing a negative electrode sheet according to the method described in this application.

用电装置、电池模块或电池包Electrical device, battery module or battery pack

本申请对二次电池的形状没有特别的限制,其可以是圆柱形、方形或其他任意的形状。例如,图3是作为一个示例的方形结构的二次电池5。The present application has no special limitation on the shape of the secondary battery, which may be cylindrical, square or any other shape. For example, FIG. 3 shows a square-shaped secondary battery 5 as an example.

在一些实施方式中,参照图4,外包装可包括壳体51和盖板53。其中,壳体51可包括底板和连接于底板上的侧板,底板和侧板围合形成容纳腔。壳体51具有与容纳腔连通的开口,盖板53能够盖设于所述开口,以封闭所述容纳腔。正极极片、负极极片和隔离膜可经卷绕工艺或叠片工艺形成电极组件52。电极组件52封装于所述容纳腔内。电解液浸润于电极组件52中。二次电池5所含电极组件52的数量可以为一个或多个,本领域技术人员可根据具体实际需求进行选择。In some embodiments, referring to FIG. 4 , the outer package may include a housing 51 and a cover 53 . Wherein, the housing 51 may include a bottom plate and a side plate connected to the bottom plate, and the bottom plate and the side plates enclose to form an accommodating cavity. The housing 51 has an opening communicating with the accommodating cavity, and the cover plate 53 can cover the opening to close the accommodating cavity. The positive pole piece, the negative pole piece and the separator can be formed into an electrode assembly 52 through a winding process or a lamination process. The electrode assembly 52 is packaged in the accommodating cavity. Electrolyte is infiltrated in the electrode assembly 52 . The number of electrode assemblies 52 contained in the secondary battery 5 can be one or more, and those skilled in the art can select according to specific actual needs.

在一些实施方式中,二次电池可以组装成电池模块,电池模块所含二次电池的数量可以为一个或多个,具体数量本领域技术人员可根据电池模块的应用和容量进行选择。In some embodiments, the secondary battery can be assembled into a battery module, and the number of secondary batteries contained in the battery module can be one or more, and the specific number can be selected by those skilled in the art according to the application and capacity of the battery module.

图5是作为一个示例的电池模块4。参照图5,在电池模块4中,多个二次电池5可以是沿电池模块4的长度方向依次排列设置。当然,也可以按照其他任意的方式进行排布。进一步可以通过紧固件将该多个二次电池5进行固定。FIG. 5 is a battery module 4 as an example. Referring to FIG. 5 , in the battery module 4 , a plurality of secondary batteries 5 may be arranged in sequence along the length direction of the battery module 4 . Of course, it can also be arranged in any other manner. Furthermore, the plurality of secondary batteries 5 may be fixed by fasteners.

可选地,电池模块4还可以包括具有容纳空间的外壳,多个二次电池5容纳于该容纳空间。Optionally, the battery module 4 may also include a case having a housing space in which a plurality of secondary batteries 5 are accommodated.

在一些实施方式中,上述电池模块还可以组装成电池包,电池包所含电池模块的数量可以为一个或多个,具体数量本领域技术人员可根据电池包的应用和容量进行选择。In some embodiments, the above-mentioned battery modules can also be assembled into a battery pack, and the number of battery modules contained in the battery pack can be one or more, and the specific number can be selected by those skilled in the art according to the application and capacity of the battery pack.

图6和图7是作为一个示例的电池包1。参照图6和图7,在电池包1中可以包括电池箱和设置于电池箱中的多个电池模块4。电池箱包括上箱体2和下箱体3,上箱体2能够盖设于下箱体3,并形成用于容纳电池模块4的封闭空间。多个电池模块4可以按照任意的方式排布于电池箱中。6 and 7 show the battery pack 1 as an example. Referring to FIGS. 6 and 7 , the battery pack 1 may include a battery box and a plurality of battery modules 4 disposed in the battery box. The battery box includes an upper box body 2 and a lower box body 3 , the upper box body 2 can cover the lower box body 3 and form a closed space for accommodating the battery module 4 . Multiple battery modules 4 can be arranged in the battery box in any manner.

另外,本申请还提供一种用电装置,所述用电装置包括本申请提供的二次电池、电池模块、或电池包中的至少一种。所述二次电池、电池模块、或电池包可以用作所述用电装置的电源,也可以用作所述用电装置的能量存储单元。所述用电装置可以包括移动设备(例如手机、笔记本电脑等)、电动车辆(例如纯电动车、混合动力电动车、插电式混合动力电动车、电动自行车、电动踏板车、电动高尔夫球车、电动卡车等)、电气列车、船舶及卫星、储能系统等,但不限于此。In addition, the present application also provides an electric device, which includes at least one of the secondary battery, battery module, or battery pack provided in the present application. The secondary battery, battery module, or battery pack can be used as a power source of the electric device, and can also be used as an energy storage unit of the electric device. The electric devices may include mobile devices (such as mobile phones, notebook computers, etc.), electric vehicles (such as pure electric vehicles, hybrid electric vehicles, plug-in hybrid electric vehicles, electric bicycles, electric scooters, electric golf carts, etc.) , electric trucks, etc.), electric trains, ships and satellites, energy storage systems, etc., but not limited thereto.

作为所述用电装置,可以根据其使用需求来选择二次电池、电池模块或电池包。As the electric device, a secondary battery, a battery module or a battery pack can be selected according to its use requirements.

图8是作为一个示例的用电装置。该用电装置为纯电动车、混合动力电动车、或插电式混合动力电动车等。为了满足该用电装置对二次电池的高功率和高能量密度的需求,可以采用电池包或电池模块。FIG. 8 is an example of an electrical device. The electric device is a pure electric vehicle, a hybrid electric vehicle, or a plug-in hybrid electric vehicle. In order to meet the high power and high energy density requirements of the electric device for the secondary battery, a battery pack or a battery module may be used.

作为另一个示例的装置可以是手机、平板电脑、笔记本电脑等。该装置通常要求轻薄化,可以采用二次电池作为电源。As another example, a device may be a cell phone, tablet, laptop, or the like. The device is generally required to be light and thin, and a secondary battery can be used as a power source.

实施例Example

以下,说明本申请的实施例。下面描述的实施例是示例性的,仅用于解释本申请,而不能理解为对本申请的限制。实施例中未注明具体技术或条件的,按照本领域内的文献所描述的技术或条件或者按照产品说明书进行。所用试剂或仪器未注明生产厂商者,均为本领域通常使用的可以通过市购获得的常规产品。本申请实施例中各成分的含量,如果没有特别说明,均以不含结晶水的质量计。Hereinafter, examples of the present application will be described. The embodiments described below are exemplary and are only used for explaining the present application, and should not be construed as limiting the present application. If no specific technique or condition is indicated in the examples, it shall be carried out according to the technique or condition described in the literature in this field or according to the product specification. The reagents or instruments used, those whose manufacturers are not indicated, are conventional products commonly used in this field and available commercially. The content of each component in the examples of the present application is based on the mass without water of crystallization, unless otherwise specified.

以下描述用语:“实施例A1的负极极片”是指实施例A1的锂离子电池制备过程中的所用的负极极片;“实施例A1的正极极片”是指实施例A1的锂离子电池制备过程中的所用的正极极片;“实施例A1的电解液”是指实施例A1的锂离子电池制备过程中的所用的电解液;“实施例A1的隔离膜”是指实施例A1的锂离子电池制备过程中的所用的隔离膜;“实施例A1的锂离子电池”是指由实施例A1的正极、隔离膜、负极、电解液制备而成的锂离子电池。The following descriptive terms: "the negative electrode sheet of embodiment A1" refers to the negative electrode sheet used in the lithium ion battery preparation process of embodiment A1; "the positive electrode sheet of embodiment A1" refers to the lithium ion battery of embodiment A1 The positive electrode sheet used in the preparation process; "the electrolyte of embodiment A1" refers to the electrolyte used in the lithium ion battery preparation process of embodiment A1; "the separator of embodiment A1" refers to the electrolyte of embodiment A1 The separator used in the preparation process of the lithium-ion battery; "the lithium-ion battery of Example A1" refers to the lithium-ion battery prepared from the positive electrode, separator, negative electrode, and electrolyte of Example A1.

在本申请中,涂布重量均为干重。In this application, coat weights are all dry weights.

本申请实施例涉及的原材料来源如下:The sources of raw materials involved in the embodiments of the present application are as follows:

镍钴锰三元材料(LiMO2,M为Ni-Co-Mn固溶体,其具体比例详见各实施例)Nickel-cobalt-manganese ternary material (LiMO 2 , M is a Ni-Co-Mn solid solution, see the specific ratios in each embodiment)

人造石墨a(广东凯金新能源科技股份有限公司,DV50=22μm);Artificial graphite a (Guangdong Kaijin New Energy Technology Co., Ltd., DV50=22μm);

人造石墨b(广东凯金新能源科技股份有限公司,DV50=12μm);Artificial graphite b (Guangdong Kaijin New Energy Technology Co., Ltd., DV50=12 μm);

N-甲基吡咯烷酮(NMP,CAS:872-50-4,上海麦克林生物科技有限公司)N-Methylpyrrolidone (NMP, CAS: 872-50-4, Shanghai McLean Biotechnology Co., Ltd.)

聚偏氟乙烯(CAS:24937-79-9,上海麦克林生物科技有限公司)Polyvinylidene fluoride (CAS: 24937-79-9, Shanghai McLean Biotechnology Co., Ltd.)

乙炔黑(广东凯金新能源科技股份有限公司)Acetylene black (Guangdong Kaijin New Energy Technology Co., Ltd.)

丙烯酸酯(CAS:25067-02-1,上海麦克林生物科技有限公司)Acrylate (CAS: 25067-02-1, Shanghai McLean Biotechnology Co., Ltd.)

碳酸二甲酯(DMC,CAS:616-38-6,上海麦克林生物科技有限公司)Dimethyl carbonate (DMC, CAS: 616-38-6, Shanghai McLean Biotechnology Co., Ltd.)

碳微米管按照以下方法制备:Carbon microtubes were prepared as follows:

将含有15%(质量百分比)的聚苯乙烯的纳米纤维丝前驱液(N甲基吡咯烷酮作为溶剂)进行静电纺丝(电压20Kv、流速50mL/min),得到纳米纤维丝;将纳米纤维丝均匀分散到含有15%(质量百分比)吡咯的1M盐酸溶液中,吡咯和纳米纤维丝的质量比为1:1;然后加入过硫酸铵进行聚合反应,过硫酸铵的质量为纳米纤维丝的1.2倍,得到表面包覆聚合物的纳米纤维丝,再向上述表面包覆的聚合物纳米纤维丝中加入四氢呋喃,四氢呋喃的质量为纳米纤维丝的16倍;在25℃下,充分搅拌6h,溶解聚苯乙烯,即得到中空的聚合物管,经过300℃预烧结2h和1200℃炭化4h,冷却后就得到微米级碳管;Carry out electrospinning (voltage 20Kv, flow velocity 50mL/min) with the nanofiber silk precursor solution (N methylpyrrolidone as solvent) that contains the polystyrene of 15% (mass percentage), obtain nanofiber silk; Disperse in 1M hydrochloric acid solution containing 15% (mass percentage) pyrrole, the mass ratio of pyrrole and nanofiber silk is 1:1; then add ammonium persulfate to carry out polymerization reaction, the quality of ammonium persulfate is 1.2 times of nanofiber silk , to obtain nanofibers coated with polymers on the surface, and then add tetrahydrofuran to the above-mentioned polymer nanofibers coated on the surface, the quality of tetrahydrofuran is 16 times that of nanofibers; at 25 ° C, fully stir for 6 hours, dissolve the polymer Styrene, that is, to obtain hollow polymer tubes, after pre-sintering at 300°C for 2 hours and carbonization at 1200°C for 4 hours, micron-sized carbon tubes are obtained after cooling;

由此得到的碳微米管,内径为2.5μm,壁厚为0.05μm,长度为15μm。The carbon microtubes thus obtained had an inner diameter of 2.5 μm, a wall thickness of 0.05 μm, and a length of 15 μm.

重复上述实施过程,改变四氢呋喃与纳米纤维丝的质量比分别为20、19、17、14、13、12、10,得到内径分别为0.2、1、2、4、6、10、12μm的碳微米管。Repeat the above implementation process, change the mass ratio of tetrahydrofuran to nanofibers to 20, 19, 17, 14, 13, 12, and 10, respectively, and obtain carbon micrometers with inner diameters of 0.2, 1, 2, 4, 6, 10, and 12 μm, respectively. Tube.

实施例A1Example A1

【负极浆料的制备】【Preparation of Negative Electrode Slurry】

将原料的各组分:负极活性物质人造石墨b(中值粒径DV50=12μm)、粘结剂丁苯橡胶、分散剂羧甲基纤维素钠CMC、导电剂sp、碳微米管按照质量分数95%:1.8%:1.2%:0.2%:1.8%(基于原料的总重量计)混合,加入去离子水,在真空搅拌机作用下获得固体组分质量分数为50%的负极浆料;所用的碳微米管的内径为2.5μm,壁厚为0.05μm,长度为15μm。Each component of raw material: Negative electrode active material artificial graphite b (median particle diameter DV50=12 μ m), binder styrene-butadiene rubber, dispersant sodium carboxymethyl cellulose CMC, conductive agent sp, carbon microtube according to mass fraction 95%: 1.8%: 1.2%: 0.2%: 1.8% (based on the total weight of the raw material) mixes, adds deionized water, and obtains a negative electrode slurry whose solid component mass fraction is 50% under the action of a vacuum mixer; used The inner diameter of the carbon microtube is 2.5 μm, the wall thickness is 0.05 μm, and the length is 15 μm.

【负极极片的制备】[Preparation of negative electrode sheet]

将上述制备的负极浆料以9mg/cm2(干重)的涂布重量均匀涂覆在厚度为8μm的负极集流体铜箔上;然后将铜箔在室温晾干后转移至120℃烘箱干燥1h,然后经过冷压、分切得到负极极片。The negative electrode slurry prepared above was uniformly coated on the negative electrode current collector copper foil with a thickness of 8 μm at a coating weight of 9 mg/cm 2 (dry weight); then the copper foil was dried at room temperature and then transferred to a 120 ° C oven for drying 1h, and then cold-pressed and cut to obtain the negative electrode sheet.

【正极极片的制备】【Preparation of Positive Electrode】

将正极活性材料镍钴锰三元材料(LiNi0.8Co0.1Mn0.1O2)、粘结剂聚偏氟乙烯、导电剂乙炔黑按照质量比8:1:1进行混合,加入溶剂NMP,在真空搅拌机作用下获得正极浆料;将正极浆料按照一定的涂布重量(按照N/P=1.05,N/P是指单位面积的负极面容量与单位面积正极面容量的比值)均匀涂敷在厚度为13μm的正极集流体铝箔上;将铝箔在室温晾干后转移至120℃烘箱干燥1h,然后经过冷压、分切得到正极极片。Mix the positive electrode active material nickel-cobalt-manganese ternary material (LiNi 0.8 Co 0.1 Mn 0.1 O 2 ), the binder polyvinylidene fluoride, and the conductive agent acetylene black according to the mass ratio of 8:1:1, add the solvent NMP, and vacuum The positive electrode slurry is obtained under the action of the mixer; the positive electrode slurry is evenly coated on the On a positive electrode current collector aluminum foil with a thickness of 13 μm; after drying the aluminum foil at room temperature, transfer it to an oven at 120°C for 1 hour, and then cold press and cut to obtain the positive electrode sheet.

【电解液的制备】【Preparation of Electrolyte】

在含水量<10ppm的氩气气氛手套箱中,于烧杯中,将EC和EMC按照3:7的质量比混合,加入LiPF6形成电解液,在所述电解液中,LiPF6质量含量为12.5%。In an argon atmosphere glove box with a water content <10ppm, in a beaker, mix EC and EMC at a mass ratio of 3:7, add LiPF 6 to form an electrolyte, and in the electrolyte, the mass content of LiPF 6 is 12.5 %.

【隔离膜】【Isolation film】

隔离膜采购自Cellgard企业,型号为cellgard2400。The isolation film was purchased from Cellgard, and the model was cellgard2400.

【锂离子电池的制备】【Preparation of lithium ion battery】

将正极极片、隔离膜、负极极片按顺序叠好,使隔离膜处于正、负极极片之间起到隔离的作用,然后卷绕得到裸电芯;将容量为4.3Ah的裸电芯置于外包装箔中,将上述制备好的8.6g电解液注入到干燥后的电池中,经过真空封装、静置、化成、整形等工序,获得锂离子电池。外包装为33mm(宽度)×220mm(长度)×97mm(高度),壳体的厚度为0.6mm;电池群裕度为90%。Stack the positive electrode, separator, and negative electrode in order, so that the separator is between the positive and negative electrodes for isolation, and then wind the bare cell; the bare cell with a capacity of 4.3Ah Put it in the outer packaging foil, inject 8.6g of the above-mentioned prepared electrolyte into the dried battery, and go through processes such as vacuum packaging, standing, forming, and shaping to obtain a lithium-ion battery. The outer package is 33mm (width)×220mm (length)×97mm (height), the thickness of the casing is 0.6mm; the margin of the battery group is 90%.

实施例A2-A5和A15-A16Examples A2-A5 and A15-A16

锂离子电池的制备过程整体上参照实施例A1,区别在于,在负极浆料的制备中,改变碳微米管的内径,具体数值如表1所示。The preparation process of the lithium-ion battery is generally referred to in Example A1, the difference is that in the preparation of the negative electrode slurry, the inner diameter of the carbon microtubes is changed, and the specific values are shown in Table 1.

实施例A6-A12Examples A6-A12

锂离子电池的制备过程整体上参照实施例A1,区别在于,在负极浆料的制备中,改变原料中导电剂sp和碳微米管的质量分数,如表1所示。The preparation process of the lithium-ion battery is generally referred to in Example A1, the difference is that in the preparation of the negative electrode slurry, the mass fractions of the conductive agent sp and carbon microtubes in the raw materials are changed, as shown in Table 1.

对比例1Comparative example 1

锂离子电池的制备过程整体上参照实施例A1,区别在于,在负极浆料的制备中,改变原料中碳微米管和导电剂sp的质量分数分别为1.8%和2%,如表1所示。The preparation process of the lithium-ion battery refers to Example A1 as a whole. The difference is that in the preparation of the negative electrode slurry, the mass fractions of carbon microtubes and conductive agent sp in the raw materials are changed to 1.8% and 2%, respectively, as shown in Table 1. .

对比例2Comparative example 2

锂离子电池的制备过程整体上参照实施例A1,区别在于,在负极浆料的制备中,不加入导电剂,碳微米管的质量分数为6%,如表1所示。The preparation process of the lithium-ion battery is generally referred to in Example A1, the difference is that no conductive agent is added in the preparation of the negative electrode slurry, and the mass fraction of carbon microtubes is 6%, as shown in Table 1.

对比例3Comparative example 3

锂离子电池的制备过程整体上参照实施例A1,区别在于,负极极片的制备中,不加入碳微米管,如表1所示。The preparation process of the lithium-ion battery is generally referred to in Example A1, the difference is that no carbon microtubes are added in the preparation of the negative electrode sheet, as shown in Table 1.

在实施例A2-A16和对比例1-3中,制备浆料所用的碳微米管和导电剂在原料中的质量分数,即为表1示出的负极膜层中碳微米管和导电剂的质量分数;对于制备浆料所用的其余组分,负极活性物质人造石墨、粘结剂丁苯橡胶、分散剂羧甲基纤维素钠按照质量比为95:1.8:1.2加入。In embodiment A2-A16 and comparative example 1-3, the massfraction of carbon microtube and conductive agent used in preparing slurry in the raw material is the carbon microtube and conductive agent in the negative film layer shown in table 1. Mass fraction; for the remaining components used in the preparation of the slurry, the negative electrode active material artificial graphite, the binder styrene-butadiene rubber, and the dispersant sodium carboxymethyl cellulose are added in a mass ratio of 95:1.8:1.2.

实施例B1Example B1

锂离子电池的制备过程整体上参照实施例A1,区别在于负极的制备过程:The preparation process of the lithium-ion battery refers to Example A1 as a whole, the difference lies in the preparation process of the negative electrode:

【第一膜层的浆料的制备】[Preparation of slurry for the first film layer]

将原料组分:第一负极活性物质人造石墨a(中值粒径Dv50=22)、导电剂sp、粘结剂丁苯橡胶、分散剂羧甲基纤维素钠按照质量分数96%:1%:1.8%:1.2%(基于原料的总重量计)混合,加入去离子水,在真空搅拌机作用下获得固体组分质量分数为50%的负极浆料;用于制备负极膜层的下层,即靠近集流体的一层。Raw material components: the first negative electrode active material artificial graphite a (median particle diameter Dv50=22), conductive agent sp, binder styrene-butadiene rubber, dispersant sodium carboxymethyl cellulose according to mass fraction 96%: 1% : 1.8%: 1.2% (based on the total weight of the raw material) mixes, adds deionized water, and obtains the negative electrode slurry that the solid component mass fraction is 50% under the effect of vacuum mixer; It is used to prepare the lower layer of the negative electrode film layer, namely The layer next to the current collector.

【第二膜层的浆料的制备】[Preparation of slurry for the second film layer]

将原料组分:第二负极活性物质人造石墨b(中值粒径Dv50=12)、粘结剂丁苯橡胶、分散剂羧甲基纤维素钠CMC、碳微米管按照质量分数94%:1.8%:1.2%:3%(基于原料的总重量计)混合,加入去离子水,在真空搅拌机作用下获得固体组分质量分数为50%的负极浆料;用于制备负极膜层的上层,即远离集流体的一层,其中不包含碳微米管。Raw material components: second negative electrode active material artificial graphite b (median particle diameter Dv50=12), binder styrene-butadiene rubber, dispersant sodium carboxymethyl cellulose CMC, carbon microtube according to mass fraction 94%: 1.8 %: 1.2%: 3% (based on the total weight of the raw materials) mixed, adding deionized water, under the action of a vacuum mixer to obtain a negative electrode slurry with a solid component mass fraction of 50%; for preparing the upper layer of the negative electrode film layer, That is, the layer away from the current collector, which does not contain carbon microtubes.

【负极极片的制备】[Preparation of negative electrode sheet]

在将上述制备的第一膜层的浆料以7mg/cm2(干重)的涂布重量均匀涂覆在厚度为8μm的负极集流体铜箔上,烘干,获得本实施例用的第一膜层(即负极膜层的下层);在第一膜层上以7mg/cm2(干重)的涂布重量均匀涂覆上述制备的第二膜层的浆料;然后将铜箔在室温晾干后转移至120℃烘箱干燥1h,然后经过冷压、分切得到负极极片。The slurry of the first film layer prepared above was evenly coated on the negative electrode current collector copper foil with a thickness of 8 μm at a coating weight of 7 mg/cm 2 (dry weight), and dried to obtain the first film used in this embodiment. A film layer (i.e. the lower layer of the negative electrode film layer); on the first film layer, the slurry of the second film layer prepared above is evenly coated with a coating weight of 7mg/cm 2 (dry weight); then the copper foil is placed on the After drying at room temperature, it was transferred to an oven at 120° C. for 1 hour, and then subjected to cold pressing and slitting to obtain negative electrode sheets.

其中,所用的碳微米管的内径为2.5μm,壁厚为0.05μm,长度为15μm。第一膜层与第二膜层的涂布重量比为1:1,即为第一膜层与第二膜层的重量比。Wherein, the inner diameter of the carbon microtubes used is 2.5 μm, the wall thickness is 0.05 μm, and the length is 15 μm. The coating weight ratio of the first film layer to the second film layer is 1:1, which is the weight ratio of the first film layer to the second film layer.

实施例B2-B5和B15-B16Examples B2-B5 and B15-B16

锂离子电池的制备过程整体上参照实施例B1,区别在于,在第一和第二膜层的浆料制备中,改变碳微米管的内径,具体数值如表2所示。The preparation process of the lithium-ion battery is generally referred to in Example B1, the difference is that in the slurry preparation of the first and second film layers, the inner diameter of the carbon microtubes is changed, and the specific values are shown in Table 2.

实施例B6和B17-B18Examples B6 and B17-B18

锂离子电池的制备过程整体上参照实施例B1,区别在于,在第一膜层的浆料制备中,原料的导电剂sp的质量分数分别如表2所示,其余组分第一负极活性物质人造石墨a(中值粒径Dv50=22)、粘结剂丁苯橡胶、分散剂羧甲基纤维素钠按照质量比96:1.8:1.2加入;The preparation process of the lithium-ion battery refers to Example B1 as a whole, the difference is that in the slurry preparation of the first film layer, the mass fraction of the conductive agent sp of the raw material is shown in Table 2, and the remaining components are the first negative active material Artificial graphite a (median particle diameter Dv50=22), binder styrene-butadiene rubber, dispersant sodium carboxymethyl cellulose add according to mass ratio 96:1.8:1.2;

在第二膜层的浆料制备中,原料还包含导电剂sp,原料中碳微米管和导电剂sp的质量分数分别如表2所示,其余组分第二负极活性物质人造石墨b(中值粒径Dv50=12)、粘结剂丁苯橡胶、分散剂羧甲基纤维素钠按照质量比94:1.8:1.2加入。In the slurry preparation of the second film layer, the raw material also includes conductive agent sp, the mass fractions of carbon microtubes and conductive agent sp in the raw material are shown in Table 2 respectively, and the second negative electrode active material artificial graphite b (middle) of the remaining components Value particle size Dv50=12), binder styrene-butadiene rubber, dispersant sodium carboxymethyl cellulose are added according to the mass ratio of 94:1.8:1.2.

实施例B7-B12Examples B7-B12

锂离子电池的制备过程整体上参照实施例B1,区别在于,在第一膜层的浆料制备中,原料的导电剂sp的质量分数分别如表2所示,其余组分第一负极活性物质人造石墨a(中值粒径Dv50=22)、粘结剂丁苯橡胶、分散剂羧甲基纤维素钠按照质量比96:1.8:1.2加入;The preparation process of the lithium-ion battery refers to Example B1 as a whole, the difference is that in the slurry preparation of the first film layer, the mass fraction of the conductive agent sp of the raw material is shown in Table 2, and the remaining components are the first negative active material Artificial graphite a (median particle diameter Dv50=22), binder styrene-butadiene rubber, dispersant sodium carboxymethyl cellulose add according to mass ratio 96:1.8:1.2;

在第二膜层的浆料制备中,改变原料中碳微米管的质量分数分别如表2所示;其余组分第二负极活性物质人造石墨b(中值粒径Dv50=12)、粘结剂丁苯橡胶、分散剂羧甲基纤维素钠按照质量比94:1.8:1.2加入。In the slurry preparation of the second film layer, change the mass fraction of carbon microtubes in the raw material as shown in Table 2 respectively; The second negative electrode active material artificial graphite b (median particle diameter Dv50=12) of the remaining components, bonding The agent styrene-butadiene rubber and the dispersant sodium carboxymethylcellulose are added according to the mass ratio of 94:1.8:1.2.

实施例B13-B14Examples B13-B14

锂离子电池的制备过程整体上参照实施例B1,区别在于,在第一膜层的浆料制备中,原料的导电剂sp的质量分数分别如表2所示,其余组分第一负极活性物质人造石墨a(中值粒径Dv50=22)、粘结剂丁苯橡胶、分散剂羧甲基纤维素钠按照质量比96:1.8:1.2加入;The preparation process of the lithium-ion battery refers to Example B1 as a whole, the difference is that in the slurry preparation of the first film layer, the mass fraction of the conductive agent sp of the raw material is shown in Table 2, and the remaining components are the first negative active material Artificial graphite a (median particle diameter Dv50=22), binder styrene-butadiene rubber, dispersant sodium carboxymethyl cellulose add according to mass ratio 96:1.8:1.2;

在负极极片的制备中,改变第一膜层与第二膜层的涂布比,如表2所示。In the preparation of the negative electrode sheet, the coating ratio of the first film layer and the second film layer was changed, as shown in Table 2.

实施例B19-B20Examples B19-B20

锂离子电池的制备过程整体上参照实施例B1,区别在于,在第一膜层的浆料制备中,原料的导电剂sp的质量分数分别如表2所示,其余组分第一负极活性物质人造石墨a(中值粒径Dv50=22)、粘结剂丁苯橡胶、分散剂羧甲基纤维素钠按照质量比96:1.8:1.2加入;The preparation process of the lithium-ion battery refers to Example B1 as a whole, the difference is that in the slurry preparation of the first film layer, the mass fraction of the conductive agent sp of the raw material is shown in Table 2, and the remaining components are the first negative active material Artificial graphite a (median particle diameter Dv50=22), binder styrene-butadiene rubber, dispersant sodium carboxymethyl cellulose add according to mass ratio 96:1.8:1.2;

在第二膜层的浆料制备中,实施例B20的原料还包含导电剂sp,原料中碳微米管和导电剂sp的质量分数分别如表2所示,其余组分第二负极活性物质人造石墨b(中值粒径Dv50=12)、粘结剂丁苯橡胶、分散剂羧甲基纤维素钠按照质量比94:1.8:1.2加入。In the slurry preparation of the second film layer, the raw material of Example B20 also contains conductive agent sp, the mass fractions of carbon microtubes and conductive agent sp in the raw material are shown in Table 2, and the remaining components of the second negative electrode active material are artificial Graphite b (median particle size Dv50=12), binder styrene-butadiene rubber, and dispersant sodium carboxymethylcellulose are added in a mass ratio of 94:1.8:1.2.

在负极极片的制备中,改变第一膜层与第二膜层的重量比,如表2所示。In the preparation of the negative electrode sheet, the weight ratio of the first film layer to the second film layer was changed, as shown in Table 2.

对比例4Comparative example 4

锂离子电池的制备过程整体上参照实施例B1,区别在于,第二膜层的制备中,第二膜层的浆料中不包含碳微米管,但是包含导电剂,其质量分数为3%,如表2所示。The preparation process of the lithium-ion battery refers to Example B1 as a whole, the difference is that in the preparation of the second film layer, the slurry of the second film layer does not contain carbon microtubes, but contains a conductive agent with a mass fraction of 3%, As shown in table 2.

实施例C1Example C1

锂离子电池的制备过程整体上参照实施例A1,区别在于以下制备过程:The preparation process of the lithium-ion battery refers to Example A1 as a whole, the difference lies in the following preparation process:

【第一膜层的浆料的制备】[Preparation of slurry for the first film layer]

将原料组分:第一负极活性物质人造石墨a(中值粒径Dv50=22)、导电剂sp、粘结剂丁苯橡胶、分散剂羧甲基纤维素钠、碳微米管按照质量分数为95.3%:0.8%:1.5%:1.2%:1.2%(基于原料的总重量计)混合,加入去离子水,在真空搅拌机作用下获得固体组分质量分数为50%的负极浆料;用于制备负极膜层的下层,即靠近集流体的一层。Raw material components: the first negative electrode active material artificial graphite a (median particle diameter Dv50=22), conductive agent sp, binding agent styrene-butadiene rubber, dispersant sodium carboxymethyl cellulose, carbon microtubes according to the mass fraction of 95.3%: 0.8%: 1.5%: 1.2%: 1.2% (based on the total weight of raw materials) mixed, adding deionized water, under the action of a vacuum mixer to obtain a negative electrode slurry with a solid component mass fraction of 50%; for Prepare the lower layer of the negative electrode film layer, that is, the layer close to the current collector.

【第二膜层的浆料的制备】:[Preparation of slurry for the second film layer]:

将原料组分:第二负极活性物质人造石墨b(中值粒径Dv50=12)、粘结剂丁苯橡胶、分散剂羧甲基纤维素钠、碳微米管按照质量分数为93.3%:1.5%:1.2%:4%(基于原料的总重量计)混合,加入去离子水,在真空搅拌机作用下获得固体组分质量分数为50%的负极浆料;用于制备负极膜层的上层,即远离集流体的一层。The raw material components: the second negative electrode active material artificial graphite b (median particle diameter Dv50=12), binder styrene-butadiene rubber, dispersant sodium carboxymethyl cellulose, carbon microtubes are 93.3% according to the mass fraction: 1.5 %: 1.2%: 4% (based on the total weight of the raw materials) mixed, adding deionized water, under the action of a vacuum mixer to obtain a negative electrode slurry with a solid component mass fraction of 50%; for preparing the upper layer of the negative electrode film layer, That is, the layer away from the current collector.

【负极极片的制备】[Preparation of negative electrode sheet]

在将上述制备的第一膜层的浆料以6mg/cm2(干重)的涂布重量均匀涂覆在厚度为8μm的负极集流体铜箔上,烘干,获得本实施例用的第一膜层(即负极膜层的下层);在第一膜层上以6mg/cm2(干重)的涂布重量均匀涂覆上述制备的第二膜层的浆料;然后将铜箔在室温晾干后转移至120℃烘箱干燥1h,然后经过冷压、分切得到负极极片。The slurry of the first film layer prepared above was evenly coated on the negative electrode current collector copper foil with a thickness of 8 μm at a coating weight of 6 mg/cm 2 (dry weight), and dried to obtain the first film used in this embodiment. One film layer (i.e. the lower layer of the negative electrode film layer); on the first film layer, the slurry of the second film layer prepared above is evenly coated with a coating weight of 6mg/cm 2 (dry weight); then the copper foil is placed on the After drying at room temperature, it was transferred to an oven at 120° C. for 1 hour, and then subjected to cold pressing and slitting to obtain negative electrode sheets.

其中,所用的碳微米管的内径为2.5μm,壁厚为0.05μm,长度为15μm。第一膜层与第二膜层的涂布重量比为1:1,即为第一膜层与第二膜层的重量比。Wherein, the inner diameter of the carbon microtubes used is 2.5 μm, the wall thickness is 0.05 μm, and the length is 15 μm. The coating weight ratio of the first film layer to the second film layer is 1:1, which is the weight ratio of the first film layer to the second film layer.

实施例C2-C5和C15-C16Examples C2-C5 and C15-C16

锂离子电池的制备过程整体上参照实施例C1,区别在于,在第一和第二膜层的浆料制备中,改变碳微米管的内径,具体数值如表3所示。The preparation process of the lithium-ion battery is generally referred to in Example C1, the difference is that in the slurry preparation of the first and second film layers, the inner diameter of the carbon microtubes is changed, and the specific values are shown in Table 3.

实施例C6-C12和C17-C18Examples C6-C12 and C17-C18

锂离子电池的制备过程整体上参照实施例C1,区别在于:The preparation process of the lithium-ion battery refers to Example C1 as a whole, the difference is:

在第一膜层的浆料制备中,原料中任选地包含导电剂sp,原料中碳微米管和导电剂sp的质量分数分别如表3所示,其余组分第一负极活性物质人造石墨a(中值粒径Dv50=22)、粘结剂丁苯橡胶、分散剂羧甲基纤维素钠按照质量比95.3:1.5:1.2加入;In the slurry preparation of the first film layer, the conductive agent sp is optionally included in the raw material, and the mass fractions of the carbon microtubes and the conductive agent sp in the raw material are shown in Table 3, and the remaining components are the first negative electrode active material artificial graphite a (median particle size Dv50=22), binder styrene-butadiene rubber, and dispersant sodium carboxymethylcellulose are added according to the mass ratio of 95.3:1.5:1.2;

在第二膜层的浆料制备中,原料任选地包含导电剂sp,原料中碳微米管和导电剂sp的质量分数分别如表3所示,其余组分第二负极活性物质人造石墨b(中值粒径Dv50=12)、粘结剂丁苯橡胶、分散剂羧甲基纤维素钠按照质量比93.3:1.5:1.2加入。In the slurry preparation of the second film layer, the raw material optionally includes a conductive agent sp, the mass fractions of the carbon microtubes and the conductive agent sp in the raw material are shown in Table 3, and the remaining components are the second negative active material artificial graphite b (median particle size Dv50=12), binder styrene-butadiene rubber, and dispersant sodium carboxymethyl cellulose are added in a mass ratio of 93.3:1.5:1.2.

C13-C14和C19-C20C13-C14 and C19-C20

锂离子电池的制备过程整体上参照实施例C1,区别在于:The preparation process of the lithium-ion battery refers to Example C1 as a whole, the difference is:

在第一膜层的浆料制备中,原料中碳微米管和导电剂sp的质量分数分别如表3所示,其余组分第一负极活性物质人造石墨a(中值粒径Dv50=22)、粘结剂丁苯橡胶、分散剂羧甲基纤维素钠按照质量比95.3:1.5:1.2加入;In the slurry preparation of the first membrane layer, the massfraction of carbon microtubes and conductive agent sp in the raw material is shown in table 3 respectively, and the first negative electrode active material artificial graphite a (median particle diameter Dv50=22) of all the other components , Binder styrene-butadiene rubber, dispersant sodium carboxymethyl cellulose are added according to the mass ratio of 95.3:1.5:1.2;

在第二膜层的浆料制备中,原料还包含导电剂sp,原料中碳微米管和导电剂sp的质量分数分别如表3所示,其余组分第二负极活性物质人造石墨b(中值粒径Dv50=12)、粘结剂丁苯橡胶、分散剂羧甲基纤维素钠按照质量比93.3:1.5:1.2加入;In the slurry preparation of the second film layer, the raw material also includes conductive agent sp, the mass fractions of carbon microtubes and conductive agent sp in the raw material are shown in Table 3 respectively, and the second negative electrode active material artificial graphite b (middle) of the remaining components Value particle size Dv50=12), binder styrene-butadiene rubber, dispersant sodium carboxymethylcellulose are added according to the mass ratio of 93.3:1.5:1.2;

在负极极片的制备中,改变第一膜层与第二膜层的重量比,如表3所示。In the preparation of the negative electrode sheet, the weight ratio of the first film layer to the second film layer was changed, as shown in Table 3.

对比例5Comparative example 5

锂离子电池的制备过程整体上参照实施例C1,区别在于,负极极片的制备中,第一和第二膜层的浆料中都不包含碳微米管,原料中的导电剂的质量分数都为1%,如表3所示;The preparation process of the lithium-ion battery refers to Example C1 as a whole. The difference is that in the preparation of the negative electrode sheet, the slurry of the first and second film layers does not contain carbon microtubes, and the mass fraction of the conductive agent in the raw materials is the same. is 1%, as shown in Table 3;

第一膜层制备的浆料中的其余组分第一负极活性物质人造石墨a(中值粒径Dv50=22)、粘结剂丁苯橡胶、分散剂羧甲基纤维素钠按照质量比96.3:1.5:1.2加入;第二膜层制备的浆料中的其余组分第一负极活性物质人造石墨b(中值粒径Dv50=12)、粘结剂丁苯橡胶、分散剂羧甲基纤维素钠按照质量比96.3:1.5:1.2加入。The remaining components in the slurry prepared by the first film layer are the first negative electrode active material artificial graphite a (median particle diameter Dv50=22), binding agent styrene-butadiene rubber, dispersant sodium carboxymethyl cellulose according to mass ratio 96.3 : 1.5: 1.2 added; the remaining components in the slurry prepared by the second film layer, the first negative electrode active material artificial graphite b (median particle size Dv50=12), binder styrene-butadiene rubber, dispersant carboxymethyl fiber Vegetarian sodium is added according to the mass ratio of 96.3:1.5:1.2.

【相关参数及电池性能测试】【Related parameters and battery performance test】

1.碳微米管的测定方法1. Determination of carbon microtubes

在本申请中,碳微米管的长度、内径和壁厚可以通过使用扫描电子显微镜(ZEISSSigma 300)进行测试。样品制备如下:将极片裁成8mm×3mm尺寸的样品,放置到样品台上,通过扫描电子显微镜(ZEISS Sigma 300)在放大10K倍数下进行测试,可以观察到碳微米管,并进行碳微米管的长度、内径和壁厚的测量。In this application, the length, inner diameter and wall thickness of carbon microtubes can be tested by using a scanning electron microscope (ZEISSSigma 300). The sample preparation is as follows: Cut the pole piece into a sample with a size of 8mm×3mm, place it on the sample stage, and test it at a magnification of 10K through a scanning electron microscope (ZEISS Sigma 300). Measurement of tube length, inside diameter and wall thickness.

2.负极膜层的结构的测定方法2. Determination of the structure of the negative electrode film layer

在本申请中,负极膜层的结构可以通过使用扫描电子显微镜(ZEISS Sigma 300),在放大10K倍数下进行测试。样品制备如下:首先将负极极片裁成2cm×2cm尺寸的待测样品,通过石蜡将负极极片固定在样品台上。然后将样品台装进样品架上锁好固定,将氩离子截面抛光仪(IB-19500CP)电源打开、抽真空(10-4Pa),同时设置氩气流量(0.15MPa)和电压(8KV)以及抛光时间(2小时),调整样品台为摇摆模式开始抛光。样品测试参考JY/T010-1996进行。In this application, the structure of the negative electrode film layer can be tested under a magnification of 10K by using a scanning electron microscope (ZEISS Sigma 300). The sample preparation is as follows: firstly, the negative pole piece is cut into a sample to be tested with a size of 2cm×2cm, and the negative pole piece is fixed on the sample stage by paraffin. Then put the sample stage into the sample rack and lock it, turn on the power of the argon ion cross-section polisher (IB-19500CP), vacuumize (10 -4 Pa), and set the argon gas flow (0.15MPa) and voltage (8KV) at the same time As well as the polishing time (2 hours), adjust the sample stage to swing mode and start polishing. The sample test is carried out with reference to JY/T010-1996.

3.电池的快速充电能力测试3. Battery fast charging capability test

25℃下,将上述各实施例和对比例的电池以1C(即1h内完全放掉理论容量的电流值)的电流进行第一次充电和放电,具体包括:将电池以1C倍率恒流充电至电压4.25V,之后恒压充电至电流≤0.05C,静置5min,再以0.33C倍率恒流放电至电压2.8V,记录其实际容量为C0。At 25°C, the batteries of the above-mentioned examples and comparative examples were charged and discharged for the first time with a current of 1C (that is, the current value at which the theoretical capacity is completely released within 1h), specifically including: charging the battery with a constant current at a rate of 1C to a voltage of 4.25V, then charged at a constant voltage to a current of ≤0.05C, let it stand for 5 minutes, and then discharged at a rate of 0.33C to a voltage of 2.8V, and recorded its actual capacity as C0.

然后将电池依次以1.0C0、1.3C0、1.5C0、1.8C0、2.0C0、2.3C0、2.5C0、3.0C0、恒流充电至全电池充电截止电压4.25V或者0V负极截止电位(以先达到者为准),每次充电完成后需以1C0放电至全电池放电截止电压2.8V,记录不同充电倍率下充电至10%、20%、30%、……、80%SOC(State of Charge,荷电状态)时所对应的负极电位,绘制出不同SOC态下的充电倍率-负极电位曲线,线性拟合后得出不同SOC态下负极电位为0V时所对应的充电倍率,该充电倍率即为该SOC态下的充电窗口,分别记为C10%SOC、C20%SOC、C30%SOC、C40%SOC、C50%SOC、C60%SOC、C70%SOC、C80%SOC,根据公式(60/C20%SOC+60/C30%SOC+60/C40%SOC+60/C50%SOC+60/C60%SOC+60/C70%SOC+60/C80%SOC)×10%计算得到该电池从10%SOC充电至80%SOC的充电时间T,单位为min。该时间越短,则电池的快速充电性能越优秀。初始放电DCR(直流电阻,Directive Current Resistance)测试Then charge the battery at 1.0C0, 1.3C0, 1.5C0, 1.8C0, 2.0C0, 2.3C0, 2.5C0, 3.0C0, constant current to the full battery charge cut-off voltage of 4.25V or 0V negative cut-off potential (whichever comes first) After each charge, it needs to be discharged at 1C0 to the full battery discharge cut-off voltage of 2.8V, and recorded at different charge rates to 10%, 20%, 30%, ..., 80% Electric state) corresponding to the negative electrode potential, draw the charge rate-negative electrode potential curves under different SOC states, and after linear fitting, the corresponding charge rate when the negative electrode potential is 0V under different SOC states is obtained, the charge rate is The charging window under the SOC state is recorded as C10%SOC, C20%SOC, C30%SOC, C40%SOC, C50%SOC, C60%SOC, C70%SOC, C80%SOC, according to the formula (60/C20% SOC+60/C30%SOC+60/C40%SOC+60/C50%SOC+60/C60%SOC+60/C70%SOC+60/C80%SOC)×10% Calculate the battery is charged from 10%SOC Charging time T to 80% SOC, unit is min. The shorter the time, the better the fast charging performance of the battery. Initial discharge DCR (DC resistance, Directive Current Resistance) test

按照上述过程分别测试实施例和对比例的锂离子电池,具体数值参见表1~表3。According to the above process, the lithium-ion batteries of the embodiment and the comparative example were respectively tested, and the specific values are shown in Table 1-Table 3.

表1:制备单层涂布的负极极片的相关参数对电池性能的影响Table 1: Effects of parameters related to the preparation of single-layer coated negative electrode sheets on battery performance

Figure BDA0003649272590000301
Figure BDA0003649272590000301

Figure BDA0003649272590000311
Figure BDA0003649272590000311

Figure BDA0003649272590000321
Figure BDA0003649272590000321

Figure BDA0003649272590000331
Figure BDA0003649272590000331

Figure BDA0003649272590000341
Figure BDA0003649272590000341

本申请的实施例与对比例相比,由表1可见,碳微米管与导电剂在单层涂布的负极膜层中的质量分数满足特定的关系式时,能够显著提升电池的快充能力;由表2-3可见,双层涂布的负极极片在包含碳微米管时,电池的充电能力得以明显改善。Compared with the comparative examples in the examples of the present application, it can be seen from Table 1 that when the mass fraction of the carbon microtubes and the conductive agent in the negative electrode film layer coated with a single layer satisfies a specific relational expression, the fast charging capacity of the battery can be significantly improved ; As can be seen from Table 2-3, when the double-coated negative pole sheet contains carbon microtubes, the charging capacity of the battery is significantly improved.

需要说明的是,本申请不限定于上述实施方式。上述实施方式仅为示例,在本申请的技术方案范围内具有与技术思想实质相同的构成、发挥相同作用效果的实施方式均包含在本申请的技术范围内。此外,在不脱离本申请主旨的范围内,对实施方式施加本领域技术人员能够想到的各种变形、将实施方式中的一部分构成要素加以组合而构筑的其它方式也包含在本申请的范围内。It should be noted that the present application is not limited to the above-mentioned embodiments. The above-mentioned embodiments are merely examples, and within the scope of the technical solutions of the present application, embodiments that have substantially the same configuration as the technical idea and exert the same effects are included in the technical scope of the present application. In addition, without departing from the scope of the present application, various modifications conceivable by those skilled in the art are added to the embodiments, and other forms constructed by combining some components in the embodiments are also included in the scope of the present application. .

Claims (21)

1. A single-layer coated negative pole piece is characterized in that,
the single-layer coated negative electrode sheet comprises a current collector and a negative electrode film layer arranged on at least one surface of the current collector, wherein the negative electrode film layer comprises a negative electrode active material and a carbon micron tube, and optionally comprises a conductive agent;
the mass fraction W1 of the carbon micron tube on the negative electrode film layer and the mass fraction W2 of the conductive agent on the negative electrode film layer meet the following requirements: when W1 is more than or equal to 0.2% and less than or equal to 2%, then W1+ W2 is less than or equal to 2%; when W1 is more than 2%, then 0. Ltoreq. W2. Ltoreq.0.5%, based on the total weight of the negative electrode film layer.
2. The single-layer coated negative electrode sheet according to claim 1, wherein the mass fraction W1 of the carbon nanotube in the negative electrode film layer is 0.2% to 5%.
3. The single coated negative electrode sheet of claim 1 or 2, wherein the carbon nanotubes have an internal diameter of 0.2 to 12 μ ι η, optionally 2 to 10 μ ι η; alternatively, the aspect ratio is from 2 to 20; further optionally, the carbon nanotube has a tube wall thickness of 0.01 μm to 1 μm.
4. The single-layer coated negative electrode sheet according to any one of claims 1 to 3, wherein the negative active material comprises at least one of artificial graphite, natural graphite, and silicon-based material; optionally, the conductive agent comprises at least one of conductive agents sp, KS-6, conductive graphite, carbon nanotubes, graphene, carbon fibers VGCF.
5. A double-layer coated negative pole piece is characterized in that,
the double-layer coated negative pole piece comprises a current collector, a first film layer and a second film layer, wherein the first film layer is arranged on at least one surface of the current collector, and the second film layer is arranged on the outer surface of the first film layer; the first membrane layer is positioned between the current collector and the second membrane layer;
wherein the first film layer comprises a first negative electrode active material; the second film layer includes a second negative active material; at least one of the first and second membrane layers comprises carbon nanotubes; the first film layer and the second film layer are different from each other at least in one of a negative electrode active material and whether or not the negative electrode active material includes a carbon nanotube.
6. The double-coated negative electrode sheet of claim 5, wherein the first film layer does not comprise carbon nanotubes and the second film layer comprises carbon nanotubes.
7. The double-coated negative electrode sheet of claim 5, wherein the first and second film layers each comprise carbon nanotubes.
8. The double-coated negative electrode sheet according to any one of claims 5 to 7, wherein the total mass fraction W3 of the carbon nanotubes in the first and second film layers is 0.2 to 5% based on the total weight of the first and second film layers.
9. The double-coated negative electrode sheet according to any one of claims 5 to 8, wherein in the first and second film layers, optionally further comprising a conductive agent, the total mass fraction W3 of the carbon nanotubes and the total mass fraction W4 of the conductive agent satisfy: when W3 is more than or equal to 0.2% and less than or equal to 2%, then W3+ W4 is less than or equal to 2%; when W3 is greater than 2%, then 0. Ltoreq. W4. Ltoreq.0.5%, based on the total mass of the first and second film layers.
10. The double-coated negative electrode sheet according to any one of claims 5 to 9, wherein the mass of the carbon nanotubes in the second film layer is 50 to 100% with respect to the total mass of the carbon nanotubes.
11. The double-coated negative electrode sheet according to any of claims 5 to 10, wherein the carbon nanotubes have an internal diameter of 0.2 to 12 μm, optionally 2 to 10 μm; alternatively, the aspect ratio is from 2 to 20; further optionally, the carbon nanotube has a tube wall thickness of 0.01 μm to 1 μm.
12. The double-coated negative electrode sheet according to claim 6, wherein in the first and second film layers, a conductive agent is optionally further contained; the mass fraction of the carbon nanotubes in the second film layer is from 0.4% to 10%, and the mass fraction of the conductive agent is from 0% to 4%, optionally from 0% to 1.6%, based on the weight of the second film layer; the mass fraction of the conductive agent in the first film layer is 0% to 4%, optionally 0% to 2%, based on the weight of the first film layer.
13. The double-coated negative electrode sheet according to claim 7, wherein in the first and second film layers, a conductive agent is optionally further contained; when the first and second film layers each contain the carbon nanotube, the mass fraction of the carbon nanotube in each film layer is 0.2% to 5%, and the mass fraction of the conductive agent in each film layer is 0% to 2%, based on the weight of each film layer.
14. The double-coated negative electrode sheet according to claim 13, wherein the mass fraction ratio of the carbon nanotube in the second film layer to the first film layer is 10 to 1.
15. The double-coated negative electrode sheet according to any one of claims 5 to 14, wherein the weight ratio of the second film layer to the first film layer is 1.
16. The double-coated negative electrode tab according to any one of claims 5 to 15, wherein the first and second negative active materials may be the same or different and comprise at least one of artificial graphite, natural graphite, silicon-based materials.
17. The bilayer coated negative electrode sheet of any one of claims 9 to 16, wherein the conductive agent may be the same or different in the first and second film layers, including at least one of conductive agents sp, KS-6, conductive graphite, carbon nanotubes, graphene, carbon fibres VGCF.
18. A secondary battery comprising the single-layer coated negative electrode sheet of any one of claims 1 to 4, or the double-layer coated negative electrode sheet of any one of claims 5 to 17.
19. A battery module characterized by comprising the secondary battery according to claim 18.
20. A battery pack comprising the battery module according to claim 19.
21. An electric device comprising at least one selected from the secondary battery according to claim 18, the battery module according to claim 19, and the battery pack according to claim 20.
CN202210538481.6A 2022-05-18 Negative electrode sheet and secondary battery, battery module, battery pack and power-consuming device containing the same Active CN115832212B (en)

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Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS60227357A (en) * 1984-04-24 1985-11-12 Shin Kobe Electric Mach Co Ltd Manufacture of plate for lead storage battery
CN112909220A (en) * 2019-12-04 2021-06-04 宁德时代新能源科技股份有限公司 Secondary battery and device containing the same
CN113875051A (en) * 2020-04-30 2021-12-31 宁德时代新能源科技股份有限公司 Secondary battery, method for producing the same, and device containing the same

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS60227357A (en) * 1984-04-24 1985-11-12 Shin Kobe Electric Mach Co Ltd Manufacture of plate for lead storage battery
CN112909220A (en) * 2019-12-04 2021-06-04 宁德时代新能源科技股份有限公司 Secondary battery and device containing the same
CN113875051A (en) * 2020-04-30 2021-12-31 宁德时代新能源科技股份有限公司 Secondary battery, method for producing the same, and device containing the same

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