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WO2026000399A1 - Battery and electrical apparatus - Google Patents

Battery and electrical apparatus

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Publication number
WO2026000399A1
WO2026000399A1 PCT/CN2024/102665 CN2024102665W WO2026000399A1 WO 2026000399 A1 WO2026000399 A1 WO 2026000399A1 CN 2024102665 W CN2024102665 W CN 2024102665W WO 2026000399 A1 WO2026000399 A1 WO 2026000399A1
Authority
WO
WIPO (PCT)
Prior art keywords
busbar
negative electrode
battery
battery cell
layer
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
PCT/CN2024/102665
Other languages
French (fr)
Chinese (zh)
Inventor
杨周飞
廖柏翔
牛从酥
李晓伟
裴振兴
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Contemporary Amperex Technology Co Ltd
Original Assignee
Contemporary Amperex Technology Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Contemporary Amperex Technology Co Ltd filed Critical Contemporary Amperex Technology Co Ltd
Priority to PCT/CN2024/102665 priority Critical patent/WO2026000399A1/en
Priority to CN202510600830.6A priority patent/CN120127293B/en
Publication of WO2026000399A1 publication Critical patent/WO2026000399A1/en
Pending legal-status Critical Current
Anticipated expiration legal-status Critical

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Classifications

    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M50/00Constructional details or processes of manufacture of the non-active parts of electrochemical cells other than fuel cells, e.g. hybrid cells
    • H01M50/10Primary casings; Jackets or wrappings
    • H01M50/102Primary casings; Jackets or wrappings characterised by their shape or physical structure
    • H01M50/103Primary casings; Jackets or wrappings characterised by their shape or physical structure prismatic or rectangular
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M10/00Secondary cells; Manufacture thereof
    • H01M10/05Accumulators with non-aqueous electrolyte
    • H01M10/052Li-accumulators
    • H01M10/0525Rocking-chair batteries, i.e. batteries with lithium insertion or intercalation in both electrodes; Lithium-ion batteries
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/02Electrodes composed of, or comprising, active material
    • H01M4/13Electrodes for accumulators with non-aqueous electrolyte, e.g. for lithium-accumulators; Processes of manufacture thereof
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/02Electrodes composed of, or comprising, active material
    • H01M4/36Selection of substances as active materials, active masses, active liquids
    • H01M4/38Selection of substances as active materials, active masses, active liquids of elements or alloys
    • H01M4/386Silicon or alloys based on silicon
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/02Electrodes composed of, or comprising, active material
    • H01M4/36Selection of substances as active materials, active masses, active liquids
    • H01M4/48Selection of substances as active materials, active masses, active liquids of inorganic oxides or hydroxides
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M50/00Constructional details or processes of manufacture of the non-active parts of electrochemical cells other than fuel cells, e.g. hybrid cells
    • H01M50/50Current conducting connections for cells or batteries
    • H01M50/502Interconnectors for connecting terminals of adjacent batteries; Interconnectors for connecting cells outside a battery casing
    • H01M50/507Interconnectors for connecting terminals of adjacent batteries; Interconnectors for connecting cells outside a battery casing comprising an arrangement of two or more busbars within a container structure, e.g. busbar modules
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/10Energy storage using batteries

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

Abstract

A battery (2) and an electrical apparatus. The battery (2) comprises a plurality of battery cells (10) and a first busbar component (30a). The plurality of battery cells (10) are arranged along the thickness direction of each battery cell (10), and the battery cells (10) each comprise a housing (12) and an electrode assembly (11) accommodated in the housing. The expansion pressure of each battery cell (10) in the thickness direction is 0.5 MPa to 2.4 MPa. The first busbar component (30a) is electrically connected to at least two battery cells (10) arranged in the thickness direction, and the first busbar component (30a) is of a multi-layer structure. The electrode assembly comprises a positive electrode plate (111), a negative electrode plate (112), and a separator (113) located between the positive electrode plate (111) and the negative electrode plate (112). The positive electrode plate (111) comprises a positive electrode current collector (1111) and a positive electrode film layer (1112) provided on at least one side of the positive electrode current collector (1111). The positive electrode film layer (1112) comprises a positive electrode active material. The positive electrode active material comprises a lithium-containing phosphate having an olivine structure. The negative electrode plate (112) comprises a negative electrode current collector (1121) and a negative electrode film layer (1122) provided on at least one side of the negative electrode current collector (1121). The negative electrode film layer (1122) comprises a negative electrode active material. The negative electrode active material comprises a carbon-based material.

Description

电池和用电装置Batteries and electrical devices 技术领域Technical Field

本申请涉及电池技术领域,并且更具体地,涉及一种电池和用电装置。This application relates to the field of battery technology, and more specifically, to a battery and an electrical device.

背景技术Background Technology

电池广泛用于电子设备,例如手机、笔记本电脑、电瓶车、电动汽车、电动飞机、电动轮船、电动玩具汽车、电动玩具轮船、电动玩具飞机和电动工具等等。Batteries are widely used in electronic devices such as mobile phones, laptops, electric vehicles, electric cars, electric airplanes, electric ships, electric toy cars, electric toy ships, electric toy airplanes, and power tools, etc.

在电池技术的发展中,如何提高电池的可靠性,是电池技术中的一个研究方向。In the development of battery technology, improving battery reliability is one of the research directions.

发明内容Summary of the Invention

本申请提供了一种电池和用电装置,其能提高电池的可靠性。This application provides a battery and an electrical device that can improve the reliability of the battery.

第一方面,本申请实施例提供了一种电池,其包括多个电池单体和第一汇流部件。多个电池单体沿电池单体的厚度方向排列,电池单体包括外壳和容纳于外壳内的电极组件。电池单体在厚度方向上的膨胀压强为0.5MPa-2.4MPa。第一汇流部件电连接至少两个沿厚度方向排列设置的电池单体,第一汇流部件为多层结构。电极组件包括正极片、负极片以及位于正极片和负极片之间的隔离膜,正极片包括正极集流体和设置于正极集流体至少一侧的正极膜层,正极膜层中包括正极活性材料,正极活性材料包括橄榄石结构的含锂磷酸盐,负极片包括负极集流体和设置于负极集流体至少一侧的负极膜层,负极膜层包括负极活性材料,负极活性材料包括碳基材料。In a first aspect, embodiments of this application provide a battery comprising a plurality of battery cells and a first busbar. The plurality of battery cells are arranged along the thickness direction of the battery cells, and each battery cell includes a casing and an electrode assembly housed within the casing. The expansion pressure of the battery cells in the thickness direction is 0.5 MPa-2.4 MPa. The first busbar electrically connects at least two battery cells arranged along the thickness direction, and the first busbar has a multilayer structure. The electrode assembly includes a positive electrode sheet, a negative electrode sheet, and a separator between the positive and negative electrode sheets. The positive electrode sheet includes a positive current collector and a positive electrode film layer disposed on at least one side of the positive current collector. The positive electrode film layer includes a positive active material, which includes a lithium phosphate with an olivine structure. The negative electrode sheet includes a negative current collector and a negative electrode film layer disposed on at least one side of the negative current collector. The negative electrode film layer includes a negative active material, which includes a carbon-based material.

电池单体的膨胀压强与电极组件的密实程度相关,本申请实施例可以允许电池单体在厚度方向上具有大于或等于0.5MPa的膨胀压强,从而提升电极组件的密实程度,提高电池单体的能量密度。电池单体在厚度方向上的膨胀压强小于或等于2.4MPa,可限制电极组件在循环过程中的变形,降低电极组件的隔离件褶皱变形的风险以及正极片和负极片在局部间距增大的风险,减少极化,改善电池单体的循环性能。第一汇流部件具有多层结构,且第一汇流部件的每一层结构均可传输电流,这样可以使第一汇流部件具有较高的过流面积,进而减少第一汇流部件的产热,提升电池的快速充电能力和可靠性。The expansion pressure of a single battery cell is related to the density of the electrode assembly. Embodiments of this application allow the battery cell to have an expansion pressure greater than or equal to 0.5 MPa in the thickness direction, thereby improving the density of the electrode assembly and increasing the energy density of the battery cell. An expansion pressure of less than or equal to 2.4 MPa in the thickness direction can limit the deformation of the electrode assembly during cycling, reducing the risk of wrinkling and deformation of the separator and the risk of increased local spacing between the positive and negative electrodes, thus reducing polarization and improving the cycle performance of the battery cell. The first busbar has a multi-layer structure, and each layer of the first busbar can transmit current. This allows the first busbar to have a high current-carrying area, thereby reducing heat generation in the first busbar and improving the battery's fast-charging capability and reliability.

在过流面积满足要求的前提下,将第一汇流部件设置为多层结构,可以减小第一汇流部件的每一层结构的厚度。电池单体在循环过程中会出现膨胀,从而拉伸第一汇流部件的与电池单体相连的一层结构,第一汇流部件的一层结构具有较小的厚度,其易于变形以适应电池单体的膨胀变形,从而在电池单体10的膨胀压强为0.5MPa-2.4Mpa时,降低电池单体与第一汇流部件的连接处被拉裂的风险,提升电池的可靠性。Provided the flow area meets the requirements, setting the first busbar component as a multi-layer structure can reduce the thickness of each layer. During cycling, the battery cell expands, stretching the layer of the first busbar component connected to the battery cell. The first layer of the first busbar component has a small thickness, making it easily deformable to accommodate the expansion and deformation of the battery cell. This reduces the risk of the connection between the battery cell and the first busbar component cracking when the expansion pressure of the battery cell 10 is 0.5MPa-2.4MPa, thus improving battery reliability.

采用具有多层结构的第一汇流部件,可适应电池单体的膨胀,并兼顾第一汇流部 件的过流能力和可变形能力,从而提升电池的可靠性和快速充电能力。The first busbar component, with its multi-layer structure, can accommodate the expansion of individual battery cells while also providing a complete first busbar. The current carrying capacity and deformability of the components are improved, thereby enhancing the reliability and fast charging capability of the battery.

在一些实施例中,第一汇流部件包括层叠并连接的第一汇流层和第二汇流层,第一汇流层连接至少两个沿厚度方向排列的电池单体。In some embodiments, the first busbar component includes a first busbar layer and a second busbar layer stacked and connected, wherein the first busbar layer connects at least two battery cells arranged along the thickness direction.

第一汇流层和第二汇流层均可传输电流,这样可以使第一汇流部件具有较高的过流面积,进而减少第一汇流部件的产热,提升电池的快速充电能力和可靠性。在过流面积满足要求的前提下,将第一汇流部件设置为双层结构,可以减小对第一汇流层的厚度的要求。电池单体在循环过程中会出现膨胀,从而拉伸第一汇流层,第一汇流层具有较小的厚度,其易于变形以适应电池单体的变形,降低电池单体与第一汇流层的连接处被拉裂的风险,提升电池的可靠性。Both the first and second busbars can transmit current, allowing the first busbar component to have a larger current-carrying area. This reduces heat generation in the first busbar component and improves the battery's fast-charging capability and reliability. Provided the current-carrying area requirement is met, designing the first busbar component as a double-layer structure reduces the thickness requirement for the first busbar layer. During cycling, individual battery cells expand, stretching the first busbar layer. The first busbar layer, with its smaller thickness, is easily deformable to accommodate the deformation of the battery cells, reducing the risk of tearing at the connection between the battery cells and the first busbar layer, thus improving battery reliability.

在一些实施例中,电池单体包括设置于外壳的电极端子,电极端子电连接于电极组件。第一汇流层的不与第二汇流层重叠的部分连接于电极端子。第二汇流层可以避开第一汇流层与电极端子连接处,从而在池单体膨胀时减小第二汇流层对第一汇流层与电极端子连接处的影响,降低与电极端子与第一汇流层的连接处被拉裂的风险,提升电池的可靠性。In some embodiments, the battery cell includes electrode terminals disposed on the housing, the electrode terminals being electrically connected to an electrode assembly. A portion of the first busbar that does not overlap with the second busbar is connected to the electrode terminals. The second busbar can bypass the connection point between the first busbar and the electrode terminals, thereby reducing the impact of the second busbar on the connection point when the battery cell expands, lowering the risk of the connection point being torn, and improving battery reliability.

在一些实施例中,第一汇流层焊接于电极端子,且第一汇流层与电极端子的焊接面积大于或等于60mm2。第一汇流层与电极端子之间具有较大的过流面积,从而减少焊接处的产热,降低第一汇流层在快速充电时的温升,提升电池的快速充电能力。In some embodiments, the first busbar is welded to the electrode terminal, and the welding area between the first busbar and the electrode terminal is greater than or equal to 60 mm² . The large current-carrying area between the first busbar and the electrode terminal reduces heat generation at the welding point, lowers the temperature rise of the first busbar during fast charging, and improves the battery's fast charging capability.

在一些实施例中,第一汇流部件包括至少一个弯折部,弯折部连接第一汇流层和第二汇流层。弯折部可以连接第一汇流层和第二汇流层,并在第一汇流层和第二汇流层之间传输电流,从而提升第一汇流部件的过流能力。In some embodiments, the first bus component includes at least one bend connecting a first bus layer and a second bus layer. The bend can connect the first bus layer and the second bus layer and transmit current between the first bus layer and the second bus layer, thereby improving the current carrying capacity of the first bus component.

在一些实施例中,第一汇流层包括第一汇流部、第二汇流部以及第一缓冲部,第一汇流部和第二汇流部沿厚度方向设置并连接于不同的电池单体,第一缓冲部连接第一汇流部和第二汇流部。第一汇流部和第二汇流部中的至少一者连接于弯折部。在电池单体的循环过程中,电池单体膨胀并对第一汇流层施加拉力;第一缓冲部可以通过变形释放应力,从而减小第一汇流部与电池单体的连接处的受力以及第二汇流部与电池单体的连接处的受力,降低第一汇流层与电池单体连接失效的风险。In some embodiments, the first busbar includes a first busbar portion, a second busbar portion, and a first buffer portion. The first busbar portion and the second busbar portion are disposed along the thickness direction and connected to different battery cells. The first buffer portion connects the first busbar portion and the second busbar portion. At least one of the first busbar portion and the second busbar portion is connected to a bending portion. During the cycling process of the battery cells, the battery cells expand and exert tensile force on the first busbar layer; the first buffer portion can release stress through deformation, thereby reducing the stress at the connection between the first busbar portion and the battery cell, as well as the stress at the connection between the second busbar portion and the battery cell, reducing the risk of connection failure between the first busbar layer and the battery cell.

在一些实施例中,弯折部与第一缓冲部避开设置。弯折部不与第一缓冲部直接连接,从而减小弯折部对第一缓冲部的变形的影响,降低第一缓冲部变形的难度。In some embodiments, the bent portion is disposed away from the first buffer portion. The bent portion is not directly connected to the first buffer portion, thereby reducing the impact of the bent portion on the deformation of the first buffer portion and reducing the difficulty of deforming the first buffer portion.

在一些实施例中,第二汇流层包括第一层叠部、第二层叠部和第二缓冲部,第一层叠部与第一汇流部层叠并通过至少一个弯折部连接,第二层叠部与第二汇流部层叠并通过至少一个弯折部连接。第二缓冲部连接第一层叠部和第二层叠部。在第一汇流层与第二汇流层的层叠方向上,第二缓冲部与第一缓冲部至少部分的重叠。In some embodiments, the second bus layer includes a first stacked portion, a second stacked portion, and a second buffer portion. The first stacked portion is stacked with the first bus layer and connected by at least one bend. The second stacked portion is stacked with the second bus layer and connected by at least one bend. The second buffer portion connects the first stacked portion and the second stacked portion. In the stacking direction of the first bus layer and the second bus layer, the second buffer portion at least partially overlaps with the first buffer portion.

在电池单体的循环过程中,电池单体膨胀并对第一汇流层施加拉力;第一缓冲部和第二缓冲部均可以通过变形释放应力,从而降低第一汇流层与电池单体连接失效的风险。第二缓冲部与第一缓冲部至少部分的重叠,这样可以使第一缓冲部与第二缓冲部的变形区域接近,从而降低第一缓冲部与第二缓冲部在变形时与其它部分干涉的风险。During the cycling process of a single battery cell, the cell expands and exerts tension on the first busbar layer. Both the first and second buffer sections can release stress through deformation, thereby reducing the risk of connection failure between the first busbar layer and the battery cell. The second buffer section at least partially overlaps with the first buffer section, which brings their deformation areas closer together, thereby reducing the risk of interference between the first and second buffer sections and other parts during deformation.

在一些实施例中,第二缓冲部和第一缓冲部贴合设置,可以节省空间,提升过流 能力。In some embodiments, the second buffer portion and the first buffer portion are fitted together, which can save space and improve overcurrent. ability.

在一些实施例中,电池还包括至少一个第二汇流部件,第二汇流部件为单层结构并连接至少两个电池单体,第二汇流部件的厚度大于第一汇流层的厚度,且第二汇流部件的厚度大于第二汇流层的厚度。在电池中,不同位置的电池单体的膨胀量可能会存在差异。对于膨胀量较小的电池单体,可以采用具有单层结构的第二汇流部件;相较于第一汇流部件,第二汇流部件结构简单,易于制造,可节省成本。第二汇流部件的厚度大于第一汇流层的厚度和第二汇流层的厚度,其过流能力可满足要求。In some embodiments, the battery further includes at least one second busbar component, which is a single-layer structure connecting at least two battery cells. The thickness of the second busbar component is greater than the thickness of the first busbar layer, and the thickness of the second busbar component is greater than the thickness of the second busbar layer. In the battery, the expansion amount of battery cells at different locations may vary. For battery cells with smaller expansion amounts, a second busbar component with a single-layer structure can be used; compared to the first busbar component, the second busbar component has a simpler structure, is easier to manufacture, and can save costs. The thickness of the second busbar component, being greater than the thickness of both the first and second busbar layers, ensures that its current-carrying capacity meets requirements.

在一些实施例中,第一汇流层的厚度与第二汇流层的厚度之和等于第二汇流部件的厚度,可减小第一汇流部件与第二汇流部件的过流能力的差异,改善电流一致性。In some embodiments, the sum of the thickness of the first bus layer and the thickness of the second bus layer is equal to the thickness of the second bus component, which can reduce the difference in overcurrent capacity between the first bus component and the second bus component and improve current consistency.

在一些实施例中,在多个电池单体中,沿厚度方向位于最外侧电池单体连接于第一汇流部件。在充电过程中,多个电池单体的膨胀可能会在厚度方向上叠加,这造成在厚度方向上位于最外侧的电池单体出现的位移较大;采用具有多层结构的第一汇流部件来连接最外侧电池单体,可以降低第一汇流部件与电池单体连接失效的风险。In some embodiments, among a plurality of battery cells, the outermost battery cell located along the thickness direction is connected to the first busbar. During charging, the expansion of the multiple battery cells may be superimposed in the thickness direction, which causes a larger displacement of the outermost battery cell in the thickness direction; using a first busbar with a multi-layer structure to connect the outermost battery cell can reduce the risk of connection failure between the first busbar and the battery cell.

在一些实施例中,第一汇流层的厚度为1mm-2.5mm,可选为1.2mm-1.8mm。本申请实施例根据电池单体的膨胀压强选择第一汇流层的厚度,可以在一定程度上兼顾第一汇流层的过流能力和第一汇流层的可变形能力,从而提升电池的快速充电能力和可靠性。In some embodiments, the thickness of the first busbar is 1mm-2.5mm, and can be selected as 1.2mm-1.8mm. The embodiments of this application select the thickness of the first busbar based on the expansion pressure of the battery cell, which can, to a certain extent, balance the current-carrying capacity and deformability of the first busbar, thereby improving the battery's fast-charging capability and reliability.

在一些实施例中,第二汇流层的厚度为1mm-2.5mm,可选为1.2mm-1.8mm。In some embodiments, the thickness of the second busbar is 1mm-2.5mm, optionally 1.2mm-1.8mm.

在一些实施例中,电池单体的体积能量密度为390Wh/L-450Wh/L,第一汇流层的厚度小于或等于2.5mm;或者,电池单体的体积能量密度为450Wh/L-480Wh/L,第一汇流层的厚度小于或等于2.2mm。In some embodiments, the volumetric energy density of the battery cell is 390Wh/L-450Wh/L, and the thickness of the first busbar is less than or equal to 2.5mm; or, the volumetric energy density of the battery cell is 450Wh/L-480Wh/L, and the thickness of the first busbar is less than or equal to 2.2mm.

电池单体的膨胀与其体积能量密度相关,本申请根据电池单体的体积能量密度设计第一汇流层的厚度,从而在一定程度上兼顾第一汇流层的过流能力和第一汇流层的可变形能力,从而提升电池的快速充电能力和可靠性。The expansion of a single battery cell is related to its volumetric energy density. This application designs the thickness of the first busbar layer based on the volumetric energy density of the battery cell, thereby balancing the current carrying capacity and deformability of the first busbar layer to a certain extent, thus improving the battery's fast charging capability and reliability.

在一些实施例中,负极活性材料中还包括硅基材料。硅基材料中硅元素在负极活性材料中的质量含量为1%-6%;第一汇流层的厚度为1.2mm-2.2mm,第二汇流层的厚度为1.2mm-2.2mm。In some embodiments, the negative electrode active material further includes a silicon-based material. The silicon content in the negative electrode active material is 1%-6% by mass; the thickness of the first busbar layer is 1.2mm-2.2mm, and the thickness of the second busbar layer is 1.2mm-2.2mm.

通过引入硅基材料,可以提升负极片的容量,提高电池单体的能量密度。引入硅基材料,还会增大负极片在循环过程中的膨胀,结合硅元素的含量设计第一汇流层的厚度和第二汇流层的厚度,可以降低因引入硅基材料而引发第一汇流层与电池单体连接失效的风险,并满足对第一汇流部件对过流能力的要求。By introducing silicon-based materials, the capacity of the negative electrode can be increased, thereby improving the energy density of the battery cell. Introducing silicon-based materials also increases the expansion of the negative electrode during cycling. By designing the thickness of the first and second busbars in conjunction with the silicon content, the risk of connection failure between the first busbar and the battery cell due to the introduction of silicon-based materials can be reduced, while still meeting the current-carrying capacity requirements of the first busbar component.

在一些实施例中,第一汇流层包括第一汇流部、第二汇流部以及连接第一汇流部和第二汇流部的第一缓冲部,第一汇流部和第二汇流部沿厚度方向设置并连接于不同的电池单体。在第一汇流层和第二汇流层的层叠方向上,第一缓冲部凸出于第一汇流部和第二汇流部。第一汇流层在与第一缓冲部对应的位置设有凹部。通过设置凹部,可减小第一缓冲部的强度,便于第一缓冲部在电池单体膨胀时的变形。In some embodiments, the first busbar layer includes a first busbar portion, a second busbar portion, and a first buffer portion connecting the first busbar portion and the second busbar portion. The first busbar portion and the second busbar portion are disposed along the thickness direction and connected to different battery cells. In the stacking direction of the first busbar layer and the second busbar layer, the first buffer portion protrudes from the first busbar portion and the second busbar portion. The first busbar layer has a recess at a position corresponding to the first buffer portion. By providing the recess, the strength of the first buffer portion can be reduced, facilitating the deformation of the first buffer portion when the battery cell expands.

在一些实施例中,电池单体的体积能量密度为390Wh/L-450Wh/L,凹部的深度为1.2mm-2.5mm;或者,电池单体的体积能量密度为450Wh/L-480Wh/L,凹部的深度为 1mm-2.2mm。In some embodiments, the volumetric energy density of the battery cell is 390Wh/L-450Wh/L, and the depth of the recess is 1.2mm-2.5mm; or, the volumetric energy density of the battery cell is 450Wh/L-480Wh/L, and the depth of the recess is... 1mm-2.2mm.

电池单体的膨胀与其体积能量密度相关,本申请根据电池单体的体积能量密度设计凹部的深度,从而在一定程度上兼顾第一缓冲部的过流能力和第一缓冲部的可变形能力,从而提升电池的快速充电能力和可靠性。The expansion of a battery cell is related to its volumetric energy density. This application designs the depth of the recess based on the volumetric energy density of the battery cell, thereby taking into account the overcurrent capacity and deformability of the first buffer section to a certain extent, thereby improving the battery's fast charging capability and reliability.

在一些实施例中,电极组件包括两个第一表面和两个第二表面,两个第一表面沿厚度方向相对设置,两个第二表面沿与厚度方向垂直的方向相对设置,第二表面连接两个第一表面。第一表面的面积大于第二表面的面积。In some embodiments, the electrode assembly includes two first surfaces and two second surfaces, the two first surfaces being disposed opposite each other along the thickness direction, and the two second surfaces being disposed opposite each other along a direction perpendicular to the thickness direction, the second surfaces connecting the two first surfaces. The area of the first surfaces is larger than the area of the second surfaces.

在一些实施例中,电池单体在厚度方向上的膨胀压强为1.5MPa-2.0MPa。将电池单体在厚度方向上的膨胀压强限定在上述范围,可以在电池单体的循环过程中减小电池单体对第一汇流部件的拉力,降低电池单体与第一汇流部件连接失效的风险,提高电池的可靠性。In some embodiments, the expansion pressure of the battery cell in the thickness direction is 1.5 MPa-2.0 MPa. Limiting the expansion pressure of the battery cell in the thickness direction within the above range can reduce the pulling force of the battery cell on the first busbar component during battery cell cycling, reduce the risk of connection failure between the battery cell and the first busbar component, and improve battery reliability.

在一些实施例中,负极膜层的单面涂布重量为90mg/1540mm2至170mg/1540mm2,可选为110mg/1540mm2至150mg/1540mm2。负极膜层的单面涂布重量与负极膜层的膨胀相关,将负极膜层的单面涂布重量限定在上述范围,能够在一定程度上兼顾电池单体的能量密度和膨胀压强,减小电池单体的变形,降低电池单体与第一汇流部件连接失效的风险。In some embodiments, the single-sided coating weight of the negative electrode film is from 90 mg/1540 mm² to 170 mg/1540 mm² , and optionally from 110 mg/1540 mm² to 150 mg/1540 mm² . The single-sided coating weight of the negative electrode film is related to the expansion of the negative electrode film. Limiting the single-sided coating weight of the negative electrode film to the above range can, to a certain extent, balance the energy density and expansion pressure of the battery cell, reduce the deformation of the battery cell, and reduce the risk of connection failure between the battery cell and the first busbar component.

在一些实施例中,负极膜层于电池单体100%SOC下的压实密度为1.15g/cm3至1.36g/cm3,可选为1.25g/cm3至1.36g/cm3。负极膜层的压实密度与电池单体于100%荷电状态的膨胀相关,将负极膜层的压实密度限定在1.15g/cm3至1.36g/cm3,能够在一定程度上兼顾电池单体的能量密度和膨胀压强,减小电池单体的变形,降低电池单体与第一汇流部件连接失效的风险。In some embodiments, the compaction density of the negative electrode film at 100% SOC of the battery cell is 1.15 g/ cm³ to 1.36 g/ cm³ , optionally 1.25 g/ cm³ to 1.36 g/ cm³ . The compaction density of the negative electrode film is related to the expansion of the battery cell at 100% SOC. Limiting the compaction density of the negative electrode film to 1.15 g/ cm³ to 1.36 g/ cm³ can, to a certain extent, balance the energy density and expansion pressure of the battery cell, reduce battery cell deformation, and lower the risk of connection failure between the battery cell and the first busbar component.

负极膜层的压实密度在上述范围时,有利于提升电池单体的能量密度;且由于负极膜层中的负极活性材料堆积较为紧密,颗粒与颗粒间接触电阻较小,能够降低负极片的电阻,从而降低产热。When the compaction density of the negative electrode film is within the above range, it is beneficial to improve the energy density of the battery cell; and because the negative electrode active material in the negative electrode film is packed more tightly, the contact resistance between particles is smaller, which can reduce the resistance of the negative electrode sheet, thereby reducing heat generation.

负极膜层的压实密度在上述范围时,可提升电池单体的快速充电能力。负极膜层的压实密度较小,可增大负极片的孔隙率,减缓负极片的膨胀,减小电池单体的膨胀压强。When the compaction density of the negative electrode film is within the above range, the fast charging capability of the battery cell can be improved. A lower compaction density of the negative electrode film can increase the porosity of the negative electrode sheet, slow down the expansion of the negative electrode sheet, and reduce the expansion pressure of the battery cell.

在一些实施例中,负极片的孔隙率为27%-40%。负极片的孔隙率大于或等于27%,可为负极片因发生副反应所产生的杂质提供空间,减缓负极片的膨胀,减小电池单体的膨胀压强,降低电池单体的变形,改善电池单体的循环性能,降低电池单体与第一汇流部件连接失效的风险。负极片的孔隙率小于或等于40%,可兼顾电池单体的能量密度。In some embodiments, the porosity of the negative electrode is 27%-40%. A porosity greater than or equal to 27% provides space for impurities generated by side reactions, slows down the expansion of the negative electrode, reduces the expansion pressure of the battery cell, decreases the deformation of the battery cell, improves the cycle performance of the battery cell, and reduces the risk of connection failure between the battery cell and the first busbar component. A porosity less than or equal to 40% can balance the energy density of the battery cell.

在一些实施例中,碳基材料包括人造石墨和天然石墨中的至少一种。人造石墨和天然石墨的导电性能好,可减少负极片在充电时的产热,提升电池单体的快速充电性能。In some embodiments, the carbon-based material includes at least one of artificial graphite and natural graphite. Artificial and natural graphite have good electrical conductivity, which can reduce heat generation of the negative electrode during charging and improve the fast-charging performance of the battery cell.

在一些实施例中,负极活性材料中还包括硅基材料,硅基材料中硅元素在负极活性材料中的质量含量为0.3%至10%,可选为1%至6%。In some embodiments, the negative electrode active material further includes a silicon-based material, wherein the silicon element in the silicon-based material has a mass content of 0.3% to 10%, optionally 1% to 6%.

在负极片中引入硅基材料,既可以提升容量,还会增大负极片的膨胀。因此,将 硅元素在负极活性材料中的质量含量限定在上述范围,可以在一定程度上兼顾电池单体的能量密度和膨胀,减小电池单体的变形,改善电池单体的循环性能,降低电池单体与第一汇流部件连接失效的风险。Introducing silicon-based materials into the negative electrode can both increase capacity and increase the expansion of the negative electrode. Therefore, [the following is a possible interpretation:] Limiting the mass content of silicon in the negative electrode active material to the above range can, to a certain extent, balance the energy density and expansion of the battery cell, reduce the deformation of the battery cell, improve the cycle performance of the battery cell, and reduce the risk of failure of the connection between the battery cell and the first busbar component.

在一些实施例中,硅基材料包括硅氧化合物和硅碳复合物中的至少一种。In some embodiments, the silicon-based material includes at least one of silicon oxides and silicon-carbon composites.

在一些实施例中,负极膜层包括第一负极膜层和第二负极膜层,第二负极膜层设置于第一负极膜层和负极集流体之间。负极活性材料包括设置于第一负极膜层的第一负极活性材料和设置于第二负极膜层的第二负极活性材料,第一负极活性材料包括人造石墨,第二负极活性材料包括人造石墨、天然石墨和硅基材料的一种或多种。第一负极膜层和第二负极膜层可以进行差异化设置,从而在一定程度上兼顾负极膜层的膨胀和容量;双层涂布能够构造负极膜层的孔隙差异,降低离子传输曲折度,减少副反应,提升电池单体的快速充电性能。In some embodiments, the negative electrode film layer includes a first negative electrode film layer and a second negative electrode film layer, with the second negative electrode film layer disposed between the first negative electrode film layer and the negative electrode current collector. The negative electrode active material includes a first negative electrode active material disposed in the first negative electrode film layer and a second negative electrode active material disposed in the second negative electrode film layer. The first negative electrode active material includes artificial graphite, and the second negative electrode active material includes one or more of artificial graphite, natural graphite, and silicon-based materials. The first and second negative electrode film layers can be differentiated to balance the expansion and capacity of the negative electrode film layer to a certain extent. Double-layer coating can create porosity differences in the negative electrode film layer, reduce ion transport tortuosity, reduce side reactions, and improve the fast-charging performance of the battery cell.

在一些实施例中,第一负极膜层的厚度和第二负极膜层的厚度比值为3:7至7:3,可选为4:6至6:4。通过调整第一负极膜层和第二负极膜层的厚度占比,能够进一步增加上下层的梯度孔隙差异,降低锂离子传输曲折度,提升电池单体的快速充电能力In some embodiments, the thickness ratio of the first negative electrode film layer to the second negative electrode film layer is 3:7 to 7:3, and optionally 4:6 to 6:4. By adjusting the thickness ratio of the first negative electrode film layer to the second negative electrode film layer, the gradient porosity difference between the upper and lower layers can be further increased, the lithium-ion transport tortuosity can be reduced, and the fast charging capability of the battery cell can be improved.

在一些实施例中,第一负极膜层的厚度小于或等于第二负极膜层的厚度,可进一步提升电池单体的快速充电能力。In some embodiments, the thickness of the first negative electrode film is less than or equal to the thickness of the second negative electrode film, which can further improve the fast charging capability of the battery cell.

在一些实施例中,第一负极活性材料的体积平均粒径Dv50小于或等于第二负极活性材料的体积平均粒径Dv50。In some embodiments, the volume average particle size Dv50 of the first negative electrode active material is less than or equal to the volume average particle size Dv50 of the second negative electrode active material.

第一负极活性材料和第二负极活性材料的颗粒粒径存在差异,能够提升电池单体的快速充电性能;在快速充电过程中,第一负极膜层的过电势通常较高,快速充电的瓶颈主要在于第一负极膜层,而本申请实施方式中第一负极活性材料的颗粒粒径相对较小,能够缩短离子的固相传输路径,提升快速充电性能,并能够改善负极片表层离子析出问题。第二负极活性材料的颗粒粒径相对较大,可使第二负极膜层中形成较大的孔隙,在充电时,孔隙可以吸收膨胀,减小负极膜层的膨胀量,减小电池单体对第一汇流部件施加的力,降低电池单体与第一汇流部件连接失效的风险。The difference in particle size between the first and second negative electrode active materials can improve the fast charging performance of the battery cell. During fast charging, the overpotential of the first negative electrode film is usually high, and the bottleneck of fast charging mainly lies in the first negative electrode film. However, in the embodiments of this application, the particle size of the first negative electrode active material is relatively small, which can shorten the solid-phase transport path of ions, improve fast charging performance, and improve the problem of ion deposition on the surface of the negative electrode sheet. The particle size of the second negative electrode active material is relatively large, which can form larger pores in the second negative electrode film. During charging, the pores can absorb expansion, reduce the expansion of the negative electrode film, reduce the force exerted by the battery cell on the first busbar component, and reduce the risk of connection failure between the battery cell and the first busbar component.

在一些实施例中,第一负极活性材料的体积平均粒径Dv50为7.8μm-14.3μm,可选为7.8μm-11.3μm。In some embodiments, the volume average particle size Dv50 of the first negative electrode active material is 7.8 μm-14.3 μm, and optionally 7.8 μm-11.3 μm.

第一负极活性材料的体积平均粒径Dv50设置在上述范围,一方面能够缩短锂离子的固相传输路径,提升快速充电性能;另一方面,材料在制备过程中不易发生团聚,能够提升材料的稳定性;再一方面,上述体积平均粒径范围的第一负极活性材料能够与第二负极活性材料配合,有利于构建第一负极膜层和第二负极膜层的梯度孔隙差异,降低锂离子传输曲折度,提升电池单体的快速充电性能。The volume average particle size Dv50 of the first negative electrode active material is set within the above-mentioned range. On the one hand, this can shorten the solid-phase transport path of lithium ions and improve fast charging performance. On the other hand, the material is less prone to agglomeration during the preparation process, which can improve the stability of the material. Furthermore, the first negative electrode active material within the above-mentioned volume average particle size range can cooperate with the second negative electrode active material, which is conducive to constructing a gradient porosity difference between the first negative electrode film and the second negative electrode film, reducing the tortuosity of lithium ion transport, and improving the fast charging performance of the battery cell.

在一些实施例中,第二负极活性材料的体积平均粒径Dv50为Dv50为9.5μm-18.5μm,可选为9.5μm-14.6μm。第二负极活性材料的体积平均粒径Dv设置在上述范围,可以使第二负极膜层的孔隙更加丰富,有利于提升电池单体的快速充电能力,并减小负极膜层在充电过程中的膨胀。In some embodiments, the volume average particle size Dv50 of the second negative electrode active material is 9.5 μm-18.5 μm, optionally 9.5 μm-14.6 μm. Setting the volume average particle size Dv of the second negative electrode active material within the above range can enrich the porosity of the second negative electrode film, which is beneficial to improving the fast charging capability of the battery cell and reducing the expansion of the negative electrode film during charging.

在一些实施例中,负极活性材料的比表面积为0.5m2/g-3m2/g,可选为0.6m2/g-1.2m2/g。将负极活性材料的比表面积限定为大于或等于0.5m2/g,可以提升电池单体快 速充电的能力;将负极活性材料的比表面积限定为小于或等于3m2/g,可减少电池单体在存储过程中的副反应,减小膨胀压强。In some embodiments, the specific surface area of the negative electrode active material is 0.5 /g to 3 /g, optionally 0.6 /g to 1.2 m² /g. Limiting the specific surface area of the negative electrode active material to greater than or equal to 0.5 /g can improve the fast charging speed of individual battery cells. The ability to charge quickly; limiting the specific surface area of the negative electrode active material to less than or equal to 3 /g can reduce side reactions of battery cells during storage and reduce expansion pressure.

在一些实施例中,正极膜层的单面涂布重量为200mg/1540mm2-370mg/1540/mm2;可选为240mg/1540mm2至330mg/1540mm2。将正极膜层的单面涂布重量设置在上述范围时,可限制正极片单位面积内的产热量,且能够兼顾提升电池单体的能量密度和充电倍率性能。In some embodiments, the single-sided coating weight of the positive electrode film is 200 mg/1540 mm² - 370 mg/1540 mm² ; optionally, it is 240 mg/1540 mm² to 330 mg/1540 mm² . Setting the single-sided coating weight of the positive electrode film within the above range can limit the heat generation per unit area of the positive electrode sheet, while also improving the energy density and charging rate performance of the battery cell.

在一些实施例中,正极膜层于电池单体100%SOC下的压实密度为2.50g/cm3至2.80g/cm3;可选为2.55g/cm3-2.70g/cm3。正极膜层的压实密度在上述范围时,有利于提升电池单体的能量密度;且由于正极膜层中的正极活性材料堆积较为紧密,颗粒与颗粒间接触电阻较小,能够进一步降低正极片的电阻,从而降低快速充电下的产热。In some embodiments, the compaction density of the positive electrode film at 100% SOC of the battery cell is 2.50 g/ cm³ to 2.80 g/ cm³ ; optionally, it is 2.55 g/ cm³ to 2.70 g/ cm³ . A compaction density within this range is beneficial for increasing the energy density of the battery cell; and because the positive electrode active material in the positive electrode film is densely packed, the contact resistance between particles is low, which further reduces the resistance of the positive electrode sheet, thereby reducing heat generation during fast charging.

在一些实施例中,正极片的孔隙率为25%-32%。正极片的孔隙率大于或等于25%,可为正极片因发生副反应所产生的杂质提供空间,减小电池单体的膨胀压强,降低电池单体的变形,改善电池单体的循环性能,降低电池单体与汇流部件连接失效的风险。正极片的孔隙率小于或等于32%,可在一定程度上兼顾电池单体的能量密度。In some embodiments, the porosity of the positive electrode is 25%-32%. A porosity greater than or equal to 25% provides space for impurities generated by side reactions, reducing the expansion pressure of the battery cell, decreasing cell deformation, improving cycle performance, and lowering the risk of connection failure between the battery cell and the busbar. A porosity less than or equal to 32% can, to some extent, maintain the energy density of the battery cell.

在一些实施例中,正极片的厚度为0.13mm-0.2mm。采用具有较小厚度的正极片,可以缩短离子迁移路径,提升离子迁移速率,减少电池单体的产热,提升电池单体的快速充电性能。In some embodiments, the thickness of the positive electrode sheet is 0.13 mm to 0.2 mm. Using a positive electrode sheet with a smaller thickness can shorten the ion migration path, increase the ion migration rate, reduce the heat generation of the battery cell, and improve the fast charging performance of the battery cell.

在一些实施例中,正极集流体的厚度与正极膜层的厚度之比为0.05-0.3。将正极集流体的厚度与正极膜层的厚度之比限定为大于或等于0.05,可以提升正极集流体的过流能力,减少正极片的温升,提升电池单体的快速充电性能;将正极集流体的厚度与正极膜层的厚度之比限定为小于或等于0.3,可降低正极片的容量的损失。本申请实施例将正极集流体的厚度与正极膜层的厚度之比限定在上述范围,可以在一定程度上兼顾电池单体的快速充电能力和能量密度。In some embodiments, the ratio of the thickness of the positive current collector to the thickness of the positive electrode film is 0.05-0.3. Limiting the ratio of the positive current collector thickness to the positive electrode film thickness to greater than or equal to 0.05 can improve the current-carrying capacity of the positive current collector, reduce the temperature rise of the positive electrode sheet, and improve the fast-charging performance of the battery cell. Limiting the ratio of the positive current collector thickness to the positive electrode film thickness to less than or equal to 0.3 can reduce the capacity loss of the positive electrode sheet. The embodiments of this application limit the ratio of the positive current collector thickness to the positive electrode film thickness within the above range, which can, to a certain extent, balance the fast-charging capability and energy density of the battery cell.

在一些实施例中,正极活性材料的体积平均粒径满足1μm≤Dv50≤2μm,0.4μm≤Dv10≤0.7μm。正极活性材料的粒径相对较小,锂离子在正极活性材料中的脱嵌锂路径较短,产热量较少;而且上述正极活性材料的粒径不会过小,可在加工制备过程中减少团聚,使得正极活性材料的性能稳定。In some embodiments, the volume average particle size of the positive electrode active material satisfies 1 μm ≤ Dv50 ≤ 2 μm and 0.4 μm ≤ Dv10 ≤ 0.7 μm. The relatively small particle size of the positive electrode active material results in a shorter lithium ion insertion/extraction pathway and less heat generation. Furthermore, the particle size of the aforementioned positive electrode active material is not too small, which reduces agglomeration during processing and preparation, thus ensuring stable performance of the positive electrode active material.

在一些实施例中,电池单体包括容纳于外壳内的电解液。In some embodiments, a battery cell includes an electrolyte contained within a housing.

在一些实施例中,电解液于室温下的电导率为15mS/cm至20mS/cm。电解液的电导率在上述范围时,离子在该电解液中的迁移速率较高,从而进一步降低电池单体的内阻,减少产热,并能够提升电池单体的快速充电性能。In some embodiments, the electrolyte has a conductivity of 15 mS/cm to 20 mS/cm at room temperature. When the conductivity of the electrolyte is within this range, the ion migration rate in the electrolyte is high, thereby further reducing the internal resistance of the battery cell, reducing heat generation, and improving the fast charging performance of the battery cell.

在一些实施例中,电解液包括有机溶剂,有机溶剂包括碳酸酯类溶剂和羧酸酯类溶剂中的一种或多种。有机溶剂搭配可提高电解液电导率、降低粘度,从而提高电池快速充电性能。In some embodiments, the electrolyte includes an organic solvent, which may include one or more of carbonate solvents and carboxylic acid ester solvents. The use of organic solvents can improve the electrolyte conductivity and reduce viscosity, thereby improving the battery's fast-charging performance.

在一些实施例中,碳酸酯类溶剂包括碳酸乙烯酯、碳酸丙烯酯、碳酸二甲酯、碳酸二乙酯和碳酸甲乙酯中的一种或多种。In some embodiments, carbonate solvents include one or more of ethylene carbonate, propylene carbonate, dimethyl carbonate, diethyl carbonate, and ethyl methyl carbonate.

在一些实施例中,羧酸酯包括R1-COO-R2,R1和R2分别独立地包括碳原子数为1-5的烷基或碳原子数为1-5的卤代烷基。上述链状羧酸酯类溶剂的电导率较高,有利于 提升电池单体的快速充电能力。In some embodiments, the carboxylic acid ester comprises R1 -COO- R2 , where R1 and R2 each independently comprise an alkyl group having 1-5 carbon atoms or a haloalkyl group having 1-5 carbon atoms. The above-mentioned chain-like carboxylic acid ester solvents have high conductivity, which is advantageous. Improve the fast charging capability of individual battery cells.

在一些实施例中,电解液包括锂盐,锂盐包括双氟磺酰亚胺锂LiFSI和六氟磷酸锂LiPF6,双氟磺酰亚胺锂LiFSI的摩尔浓度为0.2mol/L至0.5mol/L,六氟磷酸锂LiPF6的摩尔浓度为0.5mol/L至1.0mol/L。In some embodiments, the electrolyte comprises a lithium salt, including lithium bis(fluorosulfonyl)imide (LiFSI) and lithium hexafluorophosphate (LiPF6 ) , wherein the molar concentration of lithium bis(fluorosulfonyl)imide (LiFSI) is from 0.2 mol/L to 0.5 mol/L, and the molar concentration of lithium hexafluorophosphate (LiPF6 ) is from 0.5 mol/L to 1.0 mol/L.

在一些实施例中,电解液于室温下的密度ρ满足:1.05g/mL≤ρ≤1.35g/mL。电解液的密度ρ在上述范围时,锂离子在电解液中的迁移速率较高,能够进一步降低电池单体的内阻,从而降低产热,并能够提升电池单体的快速充电性能。In some embodiments, the electrolyte density ρ at room temperature satisfies: 1.05 g/mL ≤ ρ ≤ 1.35 g/mL. When the electrolyte density ρ is within the above range, the migration rate of lithium ions in the electrolyte is higher, which can further reduce the internal resistance of the battery cell, thereby reducing heat generation and improving the fast charging performance of the battery cell.

在一些实施例中,电极组件沿厚度方向上的尺寸为T,单层负极片的厚度为T1,负极片在厚度方向上层叠的层数为N;In some embodiments, the dimension of the electrode assembly along the thickness direction is T, the thickness of the single-layer negative electrode sheet is T1, and the number of layers of the negative electrode sheet stacked in the thickness direction is N.

T、T1以及N满足:0.3≤(N×T1)/T≤0.5。T, T1, and N satisfy: 0.3≤(N×T1)/T≤0.5.

在电池单体的循环过程中,负极片由于不可逆的副反应会出现厚度增大,从而使电池单体膨胀;将(N×T1)/T限定在上述范围,可以减小的电池单体的膨胀,降低电池单体与汇流部件连接失效的风险。During the cycling process of a battery cell, the negative electrode sheet will increase in thickness due to irreversible side reactions, thus causing the battery cell to expand. Limiting (N×T1)/T within the above range can reduce the expansion of the battery cell and reduce the risk of failure of the connection between the battery cell and the busbar component.

在一些实施例中,电池单体从10%SOC充电至80%SOC的充电时间为5分钟至10.5分钟。In some embodiments, the charging time for a single battery cell from 10% SOC to 80% SOC is 5 to 10.5 minutes.

第二方面,本申请实施例提供了一种用电装置,其包括第一方面任一实施例提供的电池,电池用于提供电能。Secondly, embodiments of this application provide an electrical device that includes a battery provided in any of the embodiments of the first aspect, the battery being used to provide electrical energy.

附图说明Attached Figure Description

为了更清楚地说明本申请实施例的技术方案,下面将对本申请实施例中所需要使用的附图作简单地介绍,显而易见地,下面所描述的附图仅仅是本申请的一些实施例,对于本领域普通技术人员来讲,在不付出创造性劳动的前提下,还可以根据附图获得其他的附图。To more clearly illustrate the technical solutions of the embodiments of this application, the drawings used in the embodiments of this application will be briefly introduced below. Obviously, the drawings described below are only some embodiments of this application. For those skilled in the art, other drawings can be obtained based on the drawings without creative effort.

图1为本申请一些实施例提供的车辆的结构示意图;Figure 1 is a schematic diagram of the vehicle structure provided in some embodiments of this application;

图2为本申请一些实施例提供的电池的示意图;Figure 2 is a schematic diagram of a battery provided in some embodiments of this application;

图3为本申请一些实施例提供的电池单体的爆炸示意图;Figure 3 is an exploded schematic diagram of a battery cell provided in some embodiments of this application;

图4为本申请一些实施例提供的电池的示意图;Figure 4 is a schematic diagram of a battery provided in some embodiments of this application;

图5为图4在圆框处的放大示意图;Figure 5 is an enlarged view of Figure 4 at the circular frame;

图6为图5所示的第一汇流部件的结构示意图;Figure 6 is a structural schematic diagram of the first busbar component shown in Figure 5;

图7为本申请一些实施例提供的电池单体和第一汇流部件的连接示意图;Figure 7 is a schematic diagram showing the connection between a battery cell and a first busbar according to some embodiments of this application;

图8为图3所述的电极组件的示意图;Figure 8 is a schematic diagram of the electrode assembly described in Figure 3;

图9为图8所示的电极组件的剖视示意图;Figure 9 is a cross-sectional schematic diagram of the electrode assembly shown in Figure 8;

图10为本申请一些实施例提供的电池单体的负极片的一剖视示意图;Figure 10 is a cross-sectional schematic diagram of the negative electrode sheet of a battery cell provided in some embodiments of this application;

图11为本申请一些实施例提供的电池单体的正极片的一剖视示意图;Figure 11 is a cross-sectional schematic diagram of the positive electrode sheet of a battery cell provided in some embodiments of this application;

图12为本申请另一些实施例提供的电池单体的负极片的一剖视示意图;Figure 12 is a cross-sectional schematic diagram of the negative electrode sheet of a battery cell provided in some other embodiments of this application;

图13为本申请另一些实施例提供的电池的俯视示意图;Figure 13 is a top view of a battery provided in some other embodiments of this application;

图14为图13在方框处的放大示意图; Figure 14 is an enlarged view of Figure 13 at the boxed area;

图15为图14中的第二汇流部件的结构示意图。Figure 15 is a schematic diagram of the structure of the second busbar component in Figure 14.

附图标记说明如下The reference numerals in the attached figures are explained as follows:

1、车辆;2、电池;3、控制器;4、马达;1. Vehicle; 2. Battery; 3. Controller; 4. Motor;

10、电池单体;100、电池单体列;10a、大面;10b、窄面;10. Battery cell; 100. Battery cell array; 10a. Large surface; 10b. Narrow surface;

11、电极组件;111、正极片;1111、正极集流体;1112、正极膜层;112、负极片;1121、负极集流体;1122、负极膜层;11221、第一负极膜层;11222、第二负极膜层;112a、平直层;113、隔离膜;11a、主体部;11b、正极耳;11c、负极耳;11d、第一表面;11e、第二表面;11f、第三表面;11. Electrode assembly; 111. Positive electrode sheet; 1111. Positive current collector; 1112. Positive electrode film; 112. Negative electrode sheet; 1121. Negative current collector; 1122. Negative electrode film; 11221. First negative electrode film; 11222. Second negative electrode film; 112a. Flat layer; 113. Separator; 11a. Main body; 11b. Positive electrode tab; 11c. Negative electrode tab; 11d. First surface; 11e. Second surface; 11f. Third surface;

12、外壳;121、壳体;122、端盖;13、电极端子;12. Outer shell; 121. Housing; 122. End cap; 13. Electrode terminal;

20、箱体;21、限位梁;22、框体;23、支撑梁;24、承载板;20. Box body; 21. Limiting beam; 22. Frame; 23. Support beam; 24. Load-bearing plate;

30、汇流部件;30a、第一汇流部件;30b、第二汇流部件;30c、第三汇流部件;31、第一汇流层;311、第一汇流部;312、第二汇流部;313、第一缓冲部;314、凹部;32、第二汇流层;321、第一层叠部;322、第二层叠部;323、第二缓冲部;33、弯折部;30. Busbar component; 30a. First busbar component; 30b. Second busbar component; 30c. Third busbar component; 31. First busbar layer; 311. First busbar section; 312. Second busbar section; 313. First buffer section; 314. Recess; 32. Second busbar layer; 321. First stacked section; 322. Second stacked section; 323. Second buffer section; 33. Bending section;

X、厚度方向;Y、宽度方向;Z、高度方向。X: Thickness direction; Y: Width direction; Z: Height direction.

具体实施方式Detailed Implementation

为使本申请实施例的目的、技术方案和优点更加清楚,下面将结合本申请实施例中的附图,对本申请实施例中的技术方案进行清楚地描述,显然,所描述的实施例是本申请一部分实施例,而不是全部的实施例。基于本申请中的实施例,本领域普通技术人员在没有作出创造性劳动前提下所获得的所有其他实施例,都属于本申请保护的范围。To make the objectives, technical solutions, and advantages of the embodiments of this application clearer, the technical solutions of the embodiments of this application will be clearly described below with reference to the accompanying drawings. Obviously, the described embodiments are only some embodiments of this application, not all embodiments. Based on the embodiments of this application, all other embodiments obtained by those skilled in the art without creative effort are within the scope of protection of this application.

除非另有定义,本申请所使用的所有的技术和科学术语与属于本申请的技术领域的技术人员通常理解的含义相同;本申请中在申请的说明书中所使用的术语只是为了描述具体的实施例的目的,不是旨在于限制本申请;本申请的说明书和权利要求书及上述附图说明中的术语“包括”和“具有”以及它们的任何变形,意图在于覆盖不排他的包含。本申请的说明书和权利要求书或上述附图中的术语“第一”、“第二”等是用于区别不同对象,而不是用于描述特定顺序或主次关系。Unless otherwise defined, all technical and scientific terms used in this application have the same meaning as commonly understood by one of ordinary skill in the art to which this application pertains; the terminology used in the description of this application is for the purpose of describing particular embodiments only and is not intended to limit the application; the terms "comprising" and "having," and any variations thereof, in the description, claims, and accompanying drawings of this application are intended to cover non-exclusive inclusion. The terms "first," "second," etc., in the description, claims, or accompanying drawings of this application are used to distinguish different objects, not to describe a specific order or hierarchy.

在本申请中提及“实施例”意味着,结合实施例描述的特定特征、结构或特性可以包含在本申请的至少一个实施例中。在说明书中的各个位置出现该短语并不一定均是指相同的实施例,也不是与其它实施例互斥的独立的或备选的实施例。In this application, the reference to "embodiment" means that a particular feature, structure, or characteristic described in connection with an embodiment may be included in at least one embodiment of this application. The appearance of this phrase in various places in the specification does not necessarily refer to the same embodiment, nor is it a separate or alternative embodiment that is mutually exclusive with other embodiments.

在本申请的描述中,需要说明的是,除非另有明确的规定和限定,术语“安装”、“相连”、“连接”、“附接”应做广义理解,例如,可以是固定连接,也可以是可拆卸连接,或一体地连接;可以是直接相连,也可以通过中间媒介间接相连,可以是两个元件内部的连通。对于本领域的普通技术人员而言,可以根据具体情况理解上述术语在本申请中的具体含义。In the description of this application, it should be noted that, unless otherwise expressly specified and limited, the terms "installation," "connection," "linking," and "attachment" should be interpreted broadly. For example, they can refer to a fixed connection, a detachable connection, or an integral connection; they can refer to a direct connection or an indirect connection through an intermediate medium; and they can refer to the internal communication between two components. Those skilled in the art can understand the specific meaning of the above terms in this application according to the specific circumstances.

本申请中术语“和/或”,仅仅是一种描述关联对象的关联关系,表示可以存在三 种关系,例如,A和/或B,可以表示:单独存在A,同时存在A和B,单独存在B这三种情况。另外,本申请中字符“/”,一般表示前后关联对象是一种“或”的关系。In this application, the term "and/or" is merely a description of the relationship between related objects, indicating that three or more relationships can exist. Such a relationship, for example, A and/or B, can represent three cases: A existing alone, A and B existing simultaneously, and B existing alone. Additionally, the character "/" in this application generally indicates that the preceding and following objects have an "or" relationship.

在本申请的实施例中,相同的附图标记表示相同的部件,并且为了简洁,在不同实施例中,省略对相同部件的详细说明。应理解,附图示出的本申请实施例中的各种部件的厚度、长宽等尺寸,以及集成装置的整体厚度、长宽等尺寸仅为示例性说明,而不应对本申请构成任何限定。In the embodiments of this application, the same reference numerals denote the same components, and for the sake of brevity, detailed descriptions of the same components are omitted in different embodiments. It should be understood that the thickness, length, width, and other dimensions of various components in the embodiments of this application shown in the accompanying drawings, as well as the overall thickness, length, width, and other dimensions of the integrated device, are merely illustrative and should not constitute any limitation on this application.

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至120和80至110的范围,理解为60至110和80至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至3、1至4、1至5、2至3、2至4和2至5。在本申请中,除非有其他说明,数值范围“a至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至5”表示本文中已经全部列出了“0至5”之间的全部实数,“0至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。The "range" disclosed in this application is defined by a lower limit and an upper limit. A given range is defined by selecting a lower limit and an upper limit, which define the boundaries of the particular range. Ranges defined in this way can include or exclude endpoints and can be arbitrarily combined; that is, any lower limit can be combined with any upper limit to form a range. For example, if ranges of 60 to 120 and 80 to 110 are listed for a specific parameter, it is also expected that ranges of 60 to 110 and 80 to 120 are also included. Furthermore, if minimum range values of 1 and 2 are listed, and if maximum range values of 3, 4, and 5 are listed, then the following ranges are all expected: 1 to 3, 1 to 4, 1 to 5, 2 to 3, 2 to 4, and 2 to 5. In this application, unless otherwise stated, the numerical range "a to b" represents a shortened representation of any combination of real numbers between a and b, where a and b are real numbers. For example, the numerical range "0 to 5" means that all real numbers between "0 and 5" have been listed in this article; "0 to 5" is just a shortened representation of these numerical combinations. In addition, when a parameter is stated as an integer ≥ 2, it is equivalent to disclosing that the parameter is, for example, an integer 2, 3, 4, 5, 6, 7, 8, 9, 10, 11, 12, etc.

本申请中出现的“多个”指的是两个以上(包括两个)。In this application, "multiple" means two or more (including two).

“平行”不仅包括绝对平行的情况,也包括了工程上常规认知的大致平行的情况。“垂直”不仅包括绝对垂直的情况,也包括了工程上常规认知的大致垂直的情况。"Parallelism" includes not only absolutely parallel cases, but also roughly parallel cases as commonly understood in engineering. "Perpendicularity" includes not only absolutely perpendicular cases, but also roughly perpendicular cases as commonly understood in engineering.

目前,从市场形势的发展来看,电池的应用越加广泛。电池不仅被应用于水力、火力、风力和太阳能电站等储能电源系统,而且还被广泛应用于电动自行车、电动摩托车、电动汽车等电动交通工具,以及航空航天等多个领域。随着电池应用领域的不断扩大,其市场的需求量也在不断地扩增。Currently, judging from market trends, battery applications are becoming increasingly widespread. Batteries are not only used in energy storage systems such as hydropower, thermal power, wind power, and solar power plants, but also extensively in electric vehicles such as electric bicycles, electric motorcycles, and electric cars, as well as in aerospace and other fields. With the continuous expansion of battery applications, market demand is also constantly increasing.

电池通常是指包括多个电池单体以提供更高的电压和容量的单一的物理模块。电池单体是组成电池的最小单元,多个电池单体通常通过汇流部件电连接。电池单体在循环过程中,内部发生电化学反应,使得电池单体发生膨胀。电池单体的膨胀会对汇流部件施加拉力,引发电池单体与汇流部件连接失效的风险,影响可靠性。为了降低电池单体与汇流部件连接失效的风险,可以减小汇流部件的厚度,以使汇流部件在电池单体膨胀时能够通过变形释放应力,减小电池单体与汇流部件连接失效的风险。然而,减小汇流部件的厚度会降低汇流部件的过流面积,即会造成汇流部件温升高、电阻大,影响电池的快速充电能力。A battery typically refers to a single physical module comprising multiple individual cells to provide higher voltage and capacity. The individual cell is the smallest unit that makes up a battery, and multiple cells are usually electrically connected via a busbar. During cycling, electrochemical reactions occur inside the individual cells, causing them to expand. This expansion puts tension on the busbar, increasing the risk of connection failure between the individual cells and the busbar, thus affecting reliability. To reduce this risk, the thickness of the busbar can be reduced, allowing it to release stress through deformation when the individual cells expand, thus minimizing the risk of connection failure. However, reducing the thickness of the busbar reduces its current-carrying area, leading to increased temperature and resistance, which affects the battery's fast-charging capability.

鉴于此,本申请实施例提供了一种电池,其通过对电池单体和汇流部件进行合理化设计,以降低电池单体与汇流部件连接失效的风险,增大汇流部件的过流面积,提升电池的快速充电能力。In view of this, embodiments of this application provide a battery that, through rational design of the battery cells and the busbar components, reduces the risk of connection failure between the battery cells and the busbar components, increases the current-carrying area of the busbar components, and improves the battery's fast charging capability.

本申请实施例描述的电池适用于使用电池的用电装置。用电装置可以是使用电池作为电源的设备或者电池作为储能元件的各种储能系统。用电装置可以为但不限于手机、平板、笔记本电脑、电动玩具、电动工具、电瓶车、电动汽车、轮船、航天器等 等。其中,电动玩具可以包括固定式或移动式的电动玩具,例如,游戏机、电动汽车玩具、电动轮船玩具和电动飞机玩具等等,航天器可以包括飞机、火箭、航天飞机和宇宙飞船等等。The battery described in this application is applicable to electrical devices that use batteries. The electrical device can be a device that uses a battery as a power source or various energy storage systems that use a battery as an energy storage element. The electrical device can be, but is not limited to, mobile phones, tablets, laptops, electric toys, power tools, electric vehicles, electric cars, ships, spacecraft, etc. Etc. Among them, electric toys can include stationary or mobile electric toys, such as game consoles, electric car toys, electric ship toys, and electric airplane toys, etc. Spacecraft can include airplanes, rockets, space shuttles, and spacecraft, etc.

以下实施例为了方便说明,以用电装置为车辆为例进行说明。For ease of explanation, the following embodiments will use a vehicle as an example of an electrical device.

图1为本申请一些实施例提供的车辆的结构示意图。Figure 1 is a schematic diagram of the vehicle structure provided in some embodiments of this application.

如图1所示,车辆1的内部设置有电池2,电池2可以设置在车辆1的底部或头部或尾部。电池2可以用于车辆1的供电,例如,电池2可以作为车辆1的操作电源。As shown in Figure 1, a battery 2 is installed inside the vehicle 1. The battery 2 can be located at the bottom, front, or rear of the vehicle 1. The battery 2 can be used to power the vehicle 1; for example, the battery 2 can serve as the operating power source for the vehicle 1.

车辆1还可以包括控制器3和马达4,控制器3用来控制电池2为马达4供电,例如,用于车辆1的启动、导航和行驶时的工作用电需求。Vehicle 1 may also include controller 3 and motor 4. Controller 3 is used to control battery 2 to supply power to motor 4, for example, for the power needs of vehicle 1 during start-up, navigation and driving.

在本申请一些实施例中,电池2不仅仅可以作为车辆1的操作电源,还可以作为车辆1的驱动电源,代替或部分地代替燃油或天然气为车辆1提供驱动动力。In some embodiments of this application, the battery 2 can not only serve as the operating power source for the vehicle 1, but also as the driving power source for the vehicle 1, replacing or partially replacing fuel or natural gas to provide driving power for the vehicle 1.

图2为本申请一些实施例提供的电池的示意图。Figure 2 is a schematic diagram of a battery provided in some embodiments of this application.

参照图2,在一些实施例中,电池2包括箱体20和容纳于箱体20内的多个电池单体10。Referring to FIG2, in some embodiments, the battery 2 includes a housing 20 and a plurality of battery cells 10 housed within the housing 20.

电池单体10可以为二次电池,二次电池是指在电池单体放电后可通过充电的方式使活性材料激活而继续使用的电池单体。The battery cell 10 can be a secondary battery. A secondary battery is a battery cell that can be recharged to activate the active materials and continue to be used after the battery cell has been discharged.

示例性地,电池单体10可以为锂离子电池单体、钠离子电池单体、钠锂离子电池单体、锂金属电池单体、钠金属电池单体、锂硫电池单体、镁离子电池单体、镍氢电池单体、镍镉电池单体、铅蓄电池单体等。For example, the battery cell 10 can be a lithium-ion battery cell, a sodium-ion battery cell, a sodium-lithium-ion battery cell, a lithium metal battery cell, a sodium metal battery cell, a lithium-sulfur battery cell, a magnesium-ion battery cell, a nickel-metal hydride battery cell, a nickel-cadmium battery cell, a lead-acid battery cell, etc.

作为示例,电池单体10可以为圆柱形电池单体、棱柱电池单体、软包电池单体或其它形状的电池单体,棱柱电池单体包括方壳电池单体、刀片形电池单体、多棱柱电池,多棱柱电池例如为六棱柱电池等。As an example, the battery cell 10 can be a cylindrical battery cell, a prismatic battery cell, a pouch battery cell, or a battery cell of other shapes. Prismatic battery cells include prismatic battery cells, blade-shaped battery cells, and multi-prismatic batteries, such as hexagonal prismatic batteries.

多个电池单体10之间可串联或并联或混联,混联是指多个电池单体10中既有串联又有并联。多个电池单体10之间可直接串联或并联或混联在一起,再将多个电池单体10构成的整体容纳于箱体20内;当然,也可以是多个电池单体10先串联或并联或混联组成电池模块,多个电池模块再串联或并联或混联形成一个整体,并容纳于箱体20内。Multiple battery cells 10 can be connected in series, parallel, or in a mixed manner. A mixed connection means that multiple battery cells 10 are connected in both series and parallel. Multiple battery cells 10 can be directly connected in series, parallel, or in a mixed manner, and then the whole assembly of multiple battery cells 10 is housed in the housing 20. Alternatively, multiple battery cells 10 can first be connected in series, parallel, or in a mixed manner to form a battery module, and then multiple battery modules can be connected in series, parallel, or in a mixed manner to form a whole assembly, which is then housed in the housing 20.

在一些实施例中,电池2包括多个汇流部件,多个汇流部将多个电池单体10电连接。In some embodiments, the battery 2 includes a plurality of busbars that electrically connect a plurality of battery cells 10.

在一些实施例中,箱体20可以作为车辆的底盘结构的一部分。例如,箱体20的部分可以成为车辆的地板的至少一部分,或者,箱体20的部分可以成为车辆的横梁和纵梁的至少一部分。In some embodiments, the housing 20 may be part of the vehicle's chassis structure. For example, a portion of the housing 20 may be at least a portion of the vehicle's floor, or a portion of the housing 20 may be at least a portion of the vehicle's crossbeams and longitudinal beams.

图3为本申请一些实施例提供的电池单体的爆炸示意图。Figure 3 is an exploded schematic diagram of a battery cell provided in some embodiments of this application.

参照图3,在一些实施例中,电池单体10包括外壳12和容纳于外壳12内的电极组件11。Referring to FIG3, in some embodiments, the battery cell 10 includes a housing 12 and an electrode assembly 11 housed within the housing 12.

外壳12为空心结构,其内部形成用于容纳电极组件11和电解质的容纳空间。外壳12的形状可根据电极组件11的具体形状来确定。比如,若电极组件11为长方体结构,则可选用长方体外壳。 The outer shell 12 is a hollow structure, forming an internal space for accommodating the electrode assembly 11 and the electrolyte. The shape of the outer shell 12 can be determined according to the specific shape of the electrode assembly 11. For example, if the electrode assembly 11 has a cuboid structure, a cuboid outer shell can be used.

作为示例,外壳12包括壳体121和端盖122,壳体121具有开口,端盖122用于盖合开口。As an example, the housing 12 includes a housing 121 and an end cap 122, the housing 121 having an opening and the end cap 122 for closing the opening.

壳体121是用于配合端盖122以形成电池单体10的内部空腔的部件,形成的内部空腔可以用于容纳电极组件11、电解质以及其他部件。The housing 121 is a component used to cooperate with the end cap 122 to form an internal cavity of the battery cell 10, which can be used to accommodate the electrode assembly 11, electrolyte and other components.

壳体121和端盖122可以是独立的部件。示例性的,可以于壳体121上设置开口,通过在开口处使端盖122盖合开口,以形成电池单体10的内部空腔。The housing 121 and the end cap 122 can be separate components. For example, an opening can be provided on the housing 121, and the end cap 122 can be used to close the opening to form an internal cavity for the battery cell 10.

壳体121可以是多种形状和多种尺寸的,例如长方体形、圆柱体形、六棱柱形等。具体地,壳体121的形状可以根据电极组件11的具体形状和尺寸大小来确定。壳体121的材质可以是多种,比如,铜、铁、铝、不锈钢、铝合金等,本申请实施例对此不作特殊限制。The housing 121 can have various shapes and sizes, such as cuboid, cylindrical, hexagonal prism, etc. Specifically, the shape of the housing 121 can be determined according to the specific shape and size of the electrode assembly 11. The material of the housing 121 can be various, such as copper, iron, aluminum, stainless steel, aluminum alloy, etc., and this application embodiment does not impose any special limitations on this.

端盖122的形状可以与壳体121的形状相适应以配合壳体121。端盖122的材质与壳体121的材质可以相同,也可以不同。可选地,端盖122可以由具有一定硬度和强度的材质(比如,铜、铁、铝、不锈钢、铝合金、塑胶等)制成,这样,端盖122在受挤压碰撞时就不易发生形变,使电池单体10能够具备更高的结构强度,可靠性能也可以有所提高。The shape of the end cap 122 can be adapted to the shape of the housing 121 to fit the housing 121. The material of the end cap 122 can be the same as or different from the material of the housing 121. Optionally, the end cap 122 can be made of a material with a certain hardness and strength (such as copper, iron, aluminum, stainless steel, aluminum alloy, plastic, etc.), so that the end cap 122 is not easily deformed when subjected to compression and impact, so that the battery cell 10 can have higher structural strength and improve reliability.

端盖122通过焊接、粘接、卡接或其它方式连接于壳体121。The end cap 122 is connected to the housing 121 by welding, bonding, snap-fitting or other means.

壳体121可以一端开口,也可以两端开口。在一些示例中,壳体121可为一侧开口的结构,端盖122设置为一个并盖合于壳体121。在另一些示例中,壳体121也可为两侧开口的结构,端盖122设置为两个,两个端盖122分别盖合于壳体121的两个开口。The housing 121 may be open at one end or open at both ends. In some examples, the housing 121 may be a structure with an opening on one side, and an end cap 122 is provided and covers the housing 121. In other examples, the housing 121 may also be a structure with openings on both sides, and two end caps 122 are provided, with the two end caps 122 respectively covering the two openings of the housing 121.

电极组件11是电池单体10中发生电化学反应的部件。壳体121内可以包含一个或更多个电极组件11。Electrode assembly 11 is a component in the battery cell 10 where electrochemical reactions occur. The housing 121 may contain one or more electrode assemblies 11.

在一些实施例中,电极组件11包括正极片和负极片。在电池单体10充放电过程中,活性离子(例如锂离子)在正极片和负极片之间往返嵌入和脱出。In some embodiments, the electrode assembly 11 includes a positive electrode and a negative electrode. During the charging and discharging process of the battery cell 10, active ions (e.g., lithium ions) are inserted and extracted back and forth between the positive and negative electrode.

作为示例,正极片和负极片具有活性物质的部分构成电极组件11的主体部11a,正极片不具有活性物质的部分构成正极耳11b,负极片不具有活性物质的部分构成负极耳11c。正极耳11b和负极耳11c可以共同位于主体部11a的一端或是分别位于主体部11a的两端。As an example, the portions of the positive and negative electrodes containing active material constitute the main body 11a of the electrode assembly 11, the portion of the positive electrode without active material constitutes the positive tab 11b, and the portion of the negative electrode without active material constitutes the negative tab 11c. The positive tab 11b and the negative tab 11c may be located together at one end of the main body 11a or at both ends of the main body 11a respectively.

在一些实施例中,电极组件11还包括隔离膜,隔离膜设置在正极片和负极片之间,可以起到防止正负极短路的作用,同时可以使活性离子通过。In some embodiments, the electrode assembly 11 further includes a separator membrane disposed between the positive electrode and the negative electrode, which can prevent short circuit between the positive and negative electrodes, while allowing active ions to pass through.

在一些实施方式中,电极组件11为卷绕结构。正极片和负极片卷绕成卷绕结构。In some embodiments, the electrode assembly 11 is a wound structure. The positive and negative electrode sheets are wound into a wound structure.

在一些实施方式中,电极组件11为叠片结构。In some embodiments, the electrode assembly 11 has a stacked structure.

作为示例,正极片、负极片可分别设置多个,多个正极片和多个负极片交替层叠设置。As an example, multiple positive and negative electrodes can be set, and multiple positive and multiple negative electrodes can be stacked alternately.

作为示例,正极片可设置多个,负极片折叠形成多个层叠设置的折叠段,相邻的折叠段之间夹持一个正极片。As an example, multiple positive electrode plates can be provided, and negative electrode plates can be folded to form multiple stacked folded segments, with a positive electrode plate sandwiched between adjacent folded segments.

作为示例,正极片和负极片均折叠形成多个层叠设置的折叠段。As an example, both the positive and negative electrode plates are folded to form multiple stacked folded segments.

作为示例,隔离膜可设置多个,分别设置在任意相邻的正极片或负极片之间。As an example, multiple separators can be provided, each positioned between any adjacent positive or negative electrode plates.

作为示例,隔离膜可连续地设置,通过折叠或者卷绕方式设置在任意相邻的正极 片或负极片之间。As an example, the separator can be continuously installed, either by folding or rolling, between any two adjacent positive electrodes. Between the plate or the negative electrode plate.

在一些实施例中,电池单体10还包括设置于外壳12的电极端子13;电极端子13可用于与电极组件11电连接,以输入或输出电能。In some embodiments, the battery cell 10 further includes an electrode terminal 13 disposed on the housing 12; the electrode terminal 13 can be electrically connected to the electrode assembly 11 to input or output electrical energy.

在一些实施例中,电极端子13电连接于极耳。示例性地,电极端子13为两个,两个电极端子13分别电连接于正极耳11b和负极耳11c。In some embodiments, electrode terminals 13 are electrically connected to tabs. Exemplarily, there are two electrode terminals 13, which are electrically connected to the positive tab 11b and the negative tab 11c, respectively.

图4为本申请一些实施例提供的电池的示意图;图5为图4在圆框处的放大示意图;图6为图5所示的第一汇流部件的结构示意图;图7为本申请一些实施例提供的电池单体和第一汇流部件的连接示意图;图8为图3所述的电极组件的示意图;图9为图8所示的电极组件的剖视示意图;图10为本申请一些实施例提供的电池单体的负极片的一剖视示意图;图11为本申请一些实施例提供的电池单体的正极片的一剖视示意图;图12为本申请另一些实施例提供的电池单体的负极片的一剖视示意图。Figure 4 is a schematic diagram of a battery provided in some embodiments of this application; Figure 5 is an enlarged schematic diagram of Figure 4 at the circular frame; Figure 6 is a structural schematic diagram of the first busbar shown in Figure 5; Figure 7 is a schematic diagram of the connection between a battery cell and the first busbar provided in some embodiments of this application; Figure 8 is a schematic diagram of the electrode assembly described in Figure 3; Figure 9 is a cross-sectional schematic diagram of the electrode assembly shown in Figure 8; Figure 10 is a cross-sectional schematic diagram of the negative electrode of a battery cell provided in some embodiments of this application; Figure 11 is a cross-sectional schematic diagram of the positive electrode of a battery cell provided in some embodiments of this application; Figure 12 is a cross-sectional schematic diagram of the negative electrode of a battery cell provided in other embodiments of this application.

参照图4至图12,本申请实施例的提供了一种电池,其包括多个电池单体10和多个汇流部件30,多个汇流部件30将多个电池单体10电连接。Referring to Figures 4 to 12, an embodiment of this application provides a battery, which includes a plurality of battery cells 10 and a plurality of busbar components 30, wherein the plurality of busbar components 30 electrically connect the plurality of battery cells 10.

多个汇流部件30可以将多个电池单体10串联、并联或混联。Multiple busbar components 30 can connect multiple battery cells 10 in series, parallel, or mixed connections.

多个汇流部件30可以采用相同的结构,也可以采用不同的结构。Multiple busbar components 30 may adopt the same structure or different structures.

在一些实施例中,多个电池单体10沿电池单体10的厚度方向X排列。电池单体10包括外壳12和容纳于外壳12内的电极组件11。电池单体10在厚度方向X上的膨胀压强为0.5MPa-2.4MPa。In some embodiments, a plurality of battery cells 10 are arranged along the thickness direction X of the battery cells 10. Each battery cell 10 includes a housing 12 and an electrode assembly 11 housed within the housing 12. The expansion pressure of the battery cells 10 in the thickness direction X is 0.5 MPa to 2.4 MPa.

在一些实施例中,电池包括第一汇流部件30a,第一汇流部件30a电连接至少两个沿厚度方向X排列设置的电池单体10。第一汇流部件30a为多层结构。In some embodiments, the battery includes a first busbar 30a, which electrically connects at least two battery cells 10 arranged along the thickness direction X. The first busbar 30a has a multilayer structure.

电极组件11包括正极片111、负极片112以及位于正极片111和负极片112之间的隔离膜113。正极片111包括正极集流体1111和设置于正极集流体1111至少一侧的正极膜层1112,正极膜层1112中包括正极活性材料,正极活性材料包括橄榄石结构的含锂磷酸盐。负极片112包括负极集流体1121和设置于负极集流体1121至少一侧的负极膜层1122,负极膜层1122包括负极活性材料,负极活性材料包括碳基材料。The electrode assembly 11 includes a positive electrode 111, a negative electrode 112, and a separator 113 located between the positive electrode 111 and the negative electrode 112. The positive electrode 111 includes a positive current collector 1111 and a positive electrode film 1112 disposed on at least one side of the positive current collector 1111. The positive electrode film 1112 includes a positive active material, which may include a lithium phosphate with an olivine structure. The negative electrode 112 includes a negative current collector 1121 and a negative electrode film 1122 disposed on at least one side of the negative current collector 1121. The negative electrode film 1122 includes a negative active material, which may include a carbon-based material.

电池单体10可以排成一列,也可以排成多列。示例性地,一列电池单体10可构成一个电池单体列100,电池单体列100包括至少两个沿厚度方向X排列的电池单体10。The battery cells 10 can be arranged in one column or multiple columns. For example, a column of battery cells 10 can constitute a battery cell column 100, which includes at least two battery cells 10 arranged along the thickness direction X.

电池单体10可包括一个或多个电极组件11。可选地,电极组件11沿厚度方向X排列。The battery cell 10 may include one or more electrode assemblies 11. Optionally, the electrode assemblies 11 are arranged along the thickness direction X.

可选地,电池单体10在厚度方向X上的膨胀压强为0.5MPa、0.6MPa、0.7MPa、0.8MPa、0.9MPa、1.0MPa、1.1MPa、1.2MPa、1.3MPa、1.4MPa、1.5MPa、1.6MPa、1.7MPa、1.8MPa、1.9MPa、2.0MPa、2.1MPa、2.2MPa、2.3MPa或2.4MPa。Optionally, the expansion pressure of the battery cell 10 in the thickness direction X is 0.5MPa, 0.6MPa, 0.7MPa, 0.8MPa, 0.9MPa, 1.0MPa, 1.1MPa, 1.2MPa, 1.3MPa, 1.4MPa, 1.5MPa, 1.6MPa, 1.7MPa, 1.8MPa, 1.9MPa, 2.0MPa, 2.1MPa, 2.2MPa, 2.3MPa, or 2.4MPa.

作为示例,电池单体10的膨胀压强可按照下述方式测得:As an example, the expansion pressure of the battery cell 10 can be measured in the following manner:

于45℃的环境温度中,将电池单体10以1C的恒流放电倍率放电至2.0V;At an ambient temperature of 45℃, the battery cell 10 was discharged to 2.0V at a constant current discharge rate of 1C.

将电池单体10夹持于两个夹板之间,其中,两个夹板分别位于电池单体10沿厚度方向X的两侧,并覆盖大面10a(大面10a为电池单体10沿厚度方向X一侧的表面);The battery cell 10 is clamped between two clamping plates, which are located on both sides of the battery cell 10 along the thickness direction X and cover the large surface 10a (the large surface 10a is the surface of the battery cell 10 on one side along the thickness direction X).

于45℃的环境温度中,将电池单体以0.8C的恒流充电倍率充电至3.8V,检测并记录电池单体对夹板施加的压力; At an ambient temperature of 45°C, the battery cells were charged to 3.8V at a constant current charging rate of 0.8C, and the pressure exerted by the battery cells on the clamping plate was detected and recorded.

按照上述充电策略和充电策略对电池单体进行循环充放电,直至电池单体循环至70%SOH(即电池单体的容量保持率=电池单体的放电容量/电池单体的标称容量=70%),记录电池单体对夹板施加的最大压力;The battery cells were cyclically charged and discharged according to the above charging strategy until the battery cells reached 70% SOH (i.e., the capacity retention rate of the battery cell = the discharge capacity of the battery cell / the nominal capacity of the battery cell = 70%), and the maximum pressure exerted by the battery cell on the clamping plate was recorded.

计算电池单体在厚度方向上的膨胀压强Q为:最大压力/大面面积。The expansion pressure Q of a single battery cell in the thickness direction is calculated as: maximum pressure / large surface area.

在本申请实施例中,可以仅在负极集流体1121的一侧设置负极膜层1122,也可以在负极集流体1121的两侧均设置负极膜层1122。In this embodiment, the negative electrode film layer 1122 may be provided only on one side of the negative electrode current collector 1121, or the negative electrode film layer 1122 may be provided on both sides of the negative electrode current collector 1121.

可选地,负极集流体1121沿自身厚度方向相对的两个表面上均设有负极膜层1122。负极集流体1121两个表面上的负极膜层1122可以采用相同的负极活性材料,也可以采用不同的负极活性材料;负极集流体1121两个表面上的负极膜层1122的厚度可以相同,也可以不同。Optionally, a negative electrode film layer 1122 is provided on both opposite surfaces of the negative electrode current collector 1121 along its thickness direction. The negative electrode film layer 1122 on the two surfaces of the negative electrode current collector 1121 can be made of the same negative electrode active material or different negative electrode active materials; the thickness of the negative electrode film layer 1122 on the two surfaces of the negative electrode current collector 1121 can be the same or different.

示例性地,负极集流体1121可采用金属箔片或复合集流体。作为金属箔片的示例,可采用铜、铜合金、镍、镍合金、钛、钛合金、银和银合金中的至少一种箔片。复合集流体可包括高分子材料基层以及形成于高分子材料基层至少一个表面上的金属材料层。作为示例,金属材料层中金属材料可包括铜、铜合金、镍、镍合金、钛、钛合金、银和银合金中的至少一种。作为示例,高分子材料基层可包括聚丙烯(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)和聚乙烯(PE)中的至少一种。Exemplarily, the negative electrode current collector 1121 may be a metal foil or a composite current collector. Examples of metal foils include at least one foil selected from copper, copper alloys, nickel, nickel alloys, titanium, titanium alloys, silver, and silver alloys. The composite current collector may include a polymeric material substrate and a metal material layer formed on at least one surface of the polymeric material substrate. As an example, the metal material layer may include at least one of copper, copper alloys, nickel, nickel alloys, titanium, titanium alloys, silver, and silver alloys. As an example, the polymeric material substrate may include at least one of polypropylene (PP), polyethylene terephthalate (PET), polybutylene terephthalate (PBT), polystyrene (PS), and polyethylene (PE).

负极活性材料包括碳基材料。碳基材料的循环稳定性较高,能够提升电池单体的循环性能。Negative electrode active materials include carbon-based materials. Carbon-based materials have high cycle stability and can improve the cycle performance of individual battery cells.

正极集流体1111具有在自身厚度方向相对的两个表面,正极膜层1112设置在正极集流体1111的两个相对表面中的任意一者或两者上。The positive current collector 1111 has two surfaces opposite each other in its thickness direction, and the positive electrode film layer 1112 is disposed on either or both of the two opposite surfaces of the positive current collector 1111.

示例性地,正极集流体1111可采用金属箔片或复合集流体。作为金属箔片的示例,可采用铝、铝合金、镍、镍合金、钛、钛合金、银和银合金中的至少一种箔片。复合集流体可包括高分子材料基层以及形成于高分子材料基层至少一个表面上的金属材料层。作为示例,金属材料层的金属材料可包括铝、铝合金、镍、镍合金、钛、钛合金、银和银合金中的至少一种。作为示例,高分子材料基层可包括聚丙烯(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)和聚乙烯(PE)中的至少一种。Exemplarily, the positive current collector 1111 may be a metal foil or a composite current collector. Examples of metal foils include at least one foil selected from aluminum, aluminum alloys, nickel, nickel alloys, titanium, titanium alloys, silver, and silver alloys. The composite current collector may include a polymeric material substrate and a metal material layer formed on at least one surface of the polymeric material substrate. As an example, the metal material layer may include at least one selected from aluminum, aluminum alloys, nickel, nickel alloys, titanium, titanium alloys, silver, and silver alloys. As an example, the polymeric material substrate may include at least one selected from polypropylene (PP), polyethylene terephthalate (PET), polybutylene terephthalate (PBT), polystyrene (PS), and polyethylene (PE).

含锂的磷酸盐的循环稳定性较高,采用含锂的磷酸盐作为正极活性材料,可以改善电池单体10在快速充电过程中因温升过高导致的循环衰减。Lithium-containing phosphates have high cycle stability. Using lithium-containing phosphates as positive electrode active materials can improve the cycle degradation caused by excessive temperature rise during fast charging of battery cell 10.

多个汇流部件30可以全部均是第一汇流部件30a,也可以是部分为第一汇流部件30a。Multiple busbar components 30 may all be the first busbar component 30a, or some may be the first busbar component 30a.

电池单体10的膨胀压强与电极组件11的密实程度相关,本申请实施例可以允许电池单体10在厚度方向X上具有大于或等于0.5MPa的膨胀压强,从而提升电极组件11的密实程度,提高电池单体10的能量密度。电池单体10在厚度方向X上的膨胀压强小于或等于2.4MPa,可限制电极组件11在循环过程中的变形,降低电极组件11的隔离件褶皱变形的风险以及正极片和负极片在局部间距增大的风险,减少极化,改善电池单体10的循环性能。 The expansion pressure of the battery cell 10 is related to the density of the electrode assembly 11. In this embodiment, the battery cell 10 can have an expansion pressure greater than or equal to 0.5 MPa in the thickness direction X, thereby increasing the density of the electrode assembly 11 and improving the energy density of the battery cell 10. An expansion pressure of less than or equal to 2.4 MPa in the thickness direction X of the battery cell 10 can limit the deformation of the electrode assembly 11 during cycling, reducing the risk of wrinkling and deformation of the separator in the electrode assembly 11 and the risk of increased local spacing between the positive and negative electrode plates, thus reducing polarization and improving the cycle performance of the battery cell 10.

第一汇流部件30a具有多层结构,且第一汇流部件30a的的每一层结构均可传输电流,这样可以使第一汇流部件30a具有较高的过流面积,进而减少第一汇流部件30a的产热,提升电池2的快速充电能力。The first busbar 30a has a multi-layer structure, and each layer of the first busbar 30a can transmit current. This allows the first busbar 30a to have a higher current-carrying area, thereby reducing the heat generated by the first busbar 30a and improving the fast charging capability of the battery 2.

在过流面积满足要求的前提下,将第一汇流部件30a设置为多层结构,可以减小第一汇流部件30a的每一层结构的厚度。电池单体10在循环过程中会出现膨胀,从而拉伸第一汇流部件30a的与电池单体10相连的一层结构,第一汇流部件30a的一层结构具有较小的厚度,其易于变形以适应电池单体10的膨胀变形,从而在电池单体10的膨胀压强为0.5MPa-2.4Mpa时,降低电池单体10与第一汇流部件30a的连接处被拉裂的风险,提升电池2的可靠性。Provided the flow area meets the requirements, setting the first busbar component 30a as a multi-layer structure can reduce the thickness of each layer of the first busbar component 30a. During cycling, the battery cell 10 expands, stretching the layer of the first busbar component 30a connected to the battery cell 10. The first layer of the first busbar component 30a has a small thickness, making it easily deformable to accommodate the expansion deformation of the battery cell 10. This reduces the risk of the connection between the battery cell 10 and the first busbar component 30a cracking when the expansion pressure of the battery cell 10 is between 0.5 MPa and 2.4 MPa, thus improving the reliability of the battery 2.

本申请实施例采用具有多层结构的第一汇流部件,可适应电池单体的膨胀,并兼顾第一汇流部件的过流能力和可变形能力,从而提升电池的可靠性和快速充电能力。The embodiments of this application employ a first busbar component with a multi-layer structure, which can adapt to the expansion of the battery cell and take into account the current carrying capacity and deformability of the first busbar component, thereby improving the reliability and fast charging capability of the battery.

在一些实施例中,第一汇流部件30a包括层叠并连接的第一汇流层31和第二汇流层32,第一汇流层31连接至少两个沿厚度方向X排列的电池单体10。In some embodiments, the first busbar component 30a includes a first busbar layer 31 and a second busbar layer 32 that are stacked and connected together, wherein the first busbar layer 31 connects at least two battery cells 10 arranged along the thickness direction X.

第一汇流层31和第二汇流层32可以为一体成型结构。可替代地,第一汇流层31和第二汇流层32也可以独立成型并通过焊接或其它方式连接。The first bus layer 31 and the second bus layer 32 can be integrally formed. Alternatively, the first bus layer 31 and the second bus layer 32 can also be formed independently and connected by welding or other means.

第一汇流层31和第二汇流层32均可传输电流,这样可以使第一汇流部件30a具有较高的过流面积,进而减少第一汇流部件30a的产热,提升电池的快速充电能力和可靠性。在过流面积满足要求的前提下,将第一汇流部件30a设置为双层结构,可以减小对第一汇流层31的厚度的要求。电池单体10在循环过程中会出现膨胀,从而拉伸第一汇流层31,第一汇流层31具有较小的厚度,其易于变形以适应电池单体10的变形,降低电池单体10与第一汇流层31的连接处被拉裂的风险,提升电池2的可靠性。Both the first busbar 31 and the second busbar 32 can transmit current, which allows the first busbar component 30a to have a higher current-carrying area, thereby reducing heat generation in the first busbar component 30a and improving the battery's fast-charging capability and reliability. Provided the current-carrying area requirement is met, setting the first busbar component 30a as a double-layer structure can reduce the thickness requirement of the first busbar layer 31. During cycling, the battery cell 10 expands, stretching the first busbar layer 31. The first busbar layer 31 has a relatively small thickness and is easily deformable to accommodate the deformation of the battery cell 10, reducing the risk of tearing at the connection between the battery cell 10 and the first busbar layer 31, and improving the reliability of the battery 2.

在一些实施例中,电池单体10包括设置于外壳12的电极端子13,电极端子13电连接于电极组件11。第一汇流层31连接于电池单体10的电极端子13。In some embodiments, the battery cell 10 includes an electrode terminal 13 disposed on the housing 12, the electrode terminal 13 being electrically connected to the electrode assembly 11. A first bus layer 31 is connected to the electrode terminal 13 of the battery cell 10.

可选地,第一汇流层31焊接于电极端子13。Optionally, the first bus layer 31 is welded to the electrode terminal 13.

在一些实施例中,第一汇流层31的不与第二汇流层32重叠的部分连接于电极端子13。In some embodiments, a portion of the first busbar 31 that does not overlap with the second busbar 32 is connected to the electrode terminal 13.

第二汇流层32可以避开第一汇流层31与电极端子13连接处,从而在池单体膨胀时减小第二汇流层32对第一汇流层31与电极端子13连接处的影响,降低与电极端子13与第一汇流层31的连接处被拉裂的风险,提升电池2的可靠性。另外,在装配电池单体10和第一汇流部件30a时,第二汇流层32不会覆盖第一汇流层31的用于与电极端子13连接的区域,这样可以降低装配难度。The second busbar 32 can avoid the connection point between the first busbar 31 and the electrode terminal 13, thereby reducing the impact of the second busbar 32 on the connection point when the battery cell expands, reducing the risk of the connection point between the electrode terminal 13 and the first busbar 31 being torn, and improving the reliability of the battery 2. In addition, when assembling the battery cell 10 and the first busbar component 30a, the second busbar 32 will not cover the area of the first busbar 31 used for connection with the electrode terminal 13, which can reduce the assembly difficulty.

在一些实施例中,第一汇流层31焊接于电极端子13,且第一汇流层31与电极端子13的焊接面积大于或等于60mm2In some embodiments, the first bus layer 31 is welded to the electrode terminal 13, and the welding area between the first bus layer 31 and the electrode terminal 13 is greater than or equal to 60 mm² .

示例性地,第一汇流层31与电极端子13焊接并形成焊印;焊接面积可为焊印沿第一汇流层的厚度方向的投影的面积。可选地,焊印为圆环形,焊印的内半径和外半径分别为R1和R2,则焊接面积为π×(R2 2-R1 2)。For example, the first bus layer 31 is welded to the electrode terminal 13 to form a solder mark; the welding area can be the area of the solder mark projected along the thickness direction of the first bus layer. Optionally, the solder mark is annular, and the inner radius and outer radius of the solder mark are R1 and R2 respectively, then the welding area is π × ( R22 -R12 ) .

示例性地,第一汇流层31与电极端子13的焊接面积为60mm2、70mm2、80mm2、90mm2、100mm2、110mm2或120mm2For example, the welding area between the first bus layer 31 and the electrode terminal 13 is 60 mm² , 70 mm² , 80 mm² , 90 mm² , 100 mm² , 110 mm² or 120 mm² .

本申请实施例可使第一汇流层31与电极端子13之间具有较大的过流面积,从而减少焊接处的产热,降低第一汇流层31在快速充电时的温升,提升电池的快速充电能力。The embodiments of this application can provide a larger flow area between the first busbar 31 and the electrode terminal 13, thereby reducing heat generation at the welding point, lowering the temperature rise of the first busbar 31 during fast charging, and improving the fast charging capability of the battery.

在一些实施例中,第二汇流层32未覆盖焊印。In some embodiments, the second bus layer 32 is not covered with solder pads.

在一些实施例中,在第一汇流层31和第二汇流层32的层叠方向上,第二汇流层32与电极端子13部分地重叠,这样可以缩短第二汇流层32与电极端子13之间的导电路径,从而减小电阻,减少产热。In some embodiments, in the stacking direction of the first bus layer 31 and the second bus layer 32, the second bus layer 32 partially overlaps with the electrode terminal 13, which can shorten the conductive path between the second bus layer 32 and the electrode terminal 13, thereby reducing resistance and heat generation.

在一些实施例中,第一汇流层31和第二汇流层32沿电池单体10的高度方向Z层叠。换言之,第一汇流层31与第二汇流层32的层叠方向平行于高度方向Z。示例性地,高度方向Z垂直于厚度方向X。In some embodiments, the first busbar 31 and the second busbar 32 are stacked along the height direction Z of the battery cell 10. In other words, the stacking direction of the first busbar 31 and the second busbar 32 is parallel to the height direction Z. Exemplarily, the height direction Z is perpendicular to the thickness direction X.

在一些实施例中,第二汇流层32可以设置于第一汇流层31面向电池单体10的一侧,也可以设置于第一汇流层31背离电池单体10的一侧。In some embodiments, the second busbar 32 may be disposed on the side of the first busbar 31 facing the battery cell 10, or it may be disposed on the side of the first busbar 31 away from the battery cell 10.

在一些实施例中,第一汇流部件30a包括至少一个弯折部33,弯折部33连接第一汇流层31和第二汇流层32。In some embodiments, the first busbar component 30a includes at least one bend 33, which connects the first busbar layer 31 and the second busbar layer 32.

弯折部33可以为一个,也可以为多个。There can be one or more bends 33.

弯折部33可以连接第一汇流层31和第二汇流层32,并在第一汇流层31和第二汇流层32之间传输电流,从而提升第一汇流部件30a的过流能力。The bend 33 can connect the first bus layer 31 and the second bus layer 32 and transmit current between the first bus layer 31 and the second bus layer 32, thereby improving the current carrying capacity of the first bus component 30a.

在一些实施例中,第一汇流层31包括第一汇流部311、第二汇流部312以及第一缓冲部313,第一汇流部311和第二汇流部312沿厚度方向X设置并连接于不同的电池单体10,第一缓冲部313连接第一汇流部311和第二汇流部312。第一汇流部311和第二汇流部312中的至少一者连接于弯折部33。In some embodiments, the first busbar layer 31 includes a first busbar 311, a second busbar 312, and a first buffer 313. The first busbar 311 and the second busbar 312 are disposed along the thickness direction X and connected to different battery cells 10. The first buffer 313 connects the first busbar 311 and the second busbar 312. At least one of the first busbar 311 and the second busbar 312 is connected to the bending portion 33.

第一汇流部311可以连接于一个电池单体10的电极端子13,也可以同时连接于至少两个电池单体10的电极端子13。第二汇流部312可以连接于一个电池单体10的电极端子13,也可以同时连接于至少两个电池单体10的电极端子13。The first busbar 311 can be connected to the electrode terminal 13 of one battery cell 10, or it can be connected to the electrode terminals 13 of at least two battery cells 10 simultaneously. The second busbar 312 can be connected to the electrode terminal 13 of one battery cell 10, or it can be connected to the electrode terminals 13 of at least two battery cells 10 simultaneously.

在电池单体10的循环过程中,电池单体10膨胀并对第一汇流层31施加拉力;第一缓冲部313可以通过变形释放应力,从而减小第一汇流部311与电池单体10的连接处的受力以及第二汇流部312与电池单体10的连接处的受力,降低第一汇流层31与电池单体10连接失效的风险。During the cycling process of the battery cell 10, the battery cell 10 expands and applies tension to the first busbar 31; the first buffer 313 can release stress through deformation, thereby reducing the stress at the connection between the first busbar 311 and the battery cell 10 and the connection between the second busbar 312 and the battery cell 10, and reducing the risk of failure of the connection between the first busbar 31 and the battery cell 10.

在一些实施例中,弯折部33与第一缓冲部313避开设置。弯折部33不与第一缓冲部313直接连接,从而减小弯折部33对第一缓冲部313的变形的影响,降低第一缓冲部313变形的难度。In some embodiments, the bending portion 33 is disposed away from the first buffer portion 313. The bending portion 33 is not directly connected to the first buffer portion 313, thereby reducing the impact of the bending portion 33 on the deformation of the first buffer portion 313 and reducing the difficulty of deforming the first buffer portion 313.

在一些实施例中,第一汇流层31和第二汇流层32贴合设置。可选地,初弯折部33外,第一汇流层31和第二汇流层32之间无其它固定连接关系。可替代地,第一汇流层31和第二汇流层32之间可设有导电胶。In some embodiments, the first bus layer 31 and the second bus layer 32 are bonded together. Optionally, apart from the initial bend 33, there is no other fixed connection between the first bus layer 31 and the second bus layer 32. Alternatively, conductive adhesive may be provided between the first bus layer 31 and the second bus layer 32.

在一些实施例中,第一汇流部311位于电池单体10的电极端子13的上侧,第二汇流部312位于电池单体10的电极端子13的上侧。In some embodiments, the first busbar 311 is located above the electrode terminal 13 of the battery cell 10, and the second busbar 312 is located above the electrode terminal 13 of the battery cell 10.

在一些实施例中,第一缓冲部313包括拱形结构。In some embodiments, the first buffer portion 313 includes an arched structure.

在一些实施例中,第一汇流部311通过至少一个弯折部33连接于第二汇流层32,第二汇流部312通过至少一个弯折部33连接于第二汇流层32。 In some embodiments, the first busbar 311 is connected to the second busbar layer 32 via at least one bend 33, and the second busbar 312 is connected to the second busbar layer 32 via at least one bend 33.

在一些实施例中,第二汇流层32包括第一层叠部321、第二层叠部322和第二缓冲部323,第一层叠部321与第一汇流部311层叠并通过至少一个弯折部33连接,第二层叠部322与第二汇流部312层叠并通过至少一个弯折部33连接。第二缓冲部323连接第一层叠部321和第二层叠部322。在第一汇流层31与第二汇流层32的层叠方向上,第二缓冲部323与第一缓冲部313至少部分的重叠。In some embodiments, the second bus layer 32 includes a first stacked portion 321, a second stacked portion 322, and a second buffer portion 323. The first stacked portion 321 is stacked with the first bus layer 311 and connected by at least one bend 33. The second stacked portion 322 is stacked with the second bus layer 312 and connected by at least one bend 33. The second buffer portion 323 connects the first stacked portion 321 and the second stacked portion 322. In the stacking direction of the first bus layer 31 and the second bus layer 32, the second buffer portion 323 at least partially overlaps with the first buffer portion 313.

在电池单体10的循环过程中,电池单体10膨胀并对第一汇流层31施加拉力;第一缓冲部313和第二缓冲部323均可以通过变形释放应力,从而降低第一汇流层31与电池单体10连接失效的风险。第二缓冲部323与第一缓冲部313至少部分的重叠,这样可以使第一缓冲部313与第二缓冲部323的变形区域接近,从而降低第一缓冲部313与第二缓冲部323在变形时与其它部分干涉的风险。During the cycling process of the battery cell 10, the battery cell 10 expands and applies tension to the first busbar 31; both the first buffer portion 313 and the second buffer portion 323 can release stress through deformation, thereby reducing the risk of connection failure between the first busbar 31 and the battery cell 10. The second buffer portion 323 at least partially overlaps with the first buffer portion 313, so that the deformation areas of the first buffer portion 313 and the second buffer portion 323 are close, thereby reducing the risk of interference between the first buffer portion 313 and the second buffer portion 323 and other parts during deformation.

在一些实施例中,第二缓冲部323和第一缓冲部313贴合设置。本申请实施例可以节省空间,提升过流能力。In some embodiments, the second buffer portion 323 and the first buffer portion 313 are fitted together. This embodiment can save space and improve current carrying capacity.

在一些实施例中,电池单体10的外表面包括两个大面10a和两个窄面10b,两个大面10a沿厚度方向X相对设置,两个窄面10b沿电池单体的宽度方向Y相对设置,大面10a沿宽度方向Y的两端连接于两个窄面10b。大面10a的面积大于窄面10b的面积。In some embodiments, the outer surface of the battery cell 10 includes two large surfaces 10a and two narrow surfaces 10b. The two large surfaces 10a are arranged opposite each other along the thickness direction X, and the two narrow surfaces 10b are arranged opposite each other along the width direction Y of the battery cell. The two ends of the large surfaces 10a along the width direction Y are connected to the two narrow surfaces 10b. The area of the large surfaces 10a is larger than the area of the narrow surfaces 10b.

在一些实施例中,厚度方向X、宽度方向Y以及高度方向Z两两垂直。In some embodiments, the thickness direction X, the width direction Y, and the height direction Z are perpendicular to each other.

在一些实施例中,多个电池单体列100沿宽度方向Y布置。In some embodiments, multiple battery cell rows 100 are arranged along the width direction Y.

在一些实施例中,电池单体10在厚度方向X上的膨胀压强为1.5MPa-2.0MPa。In some embodiments, the expansion pressure of the battery cell 10 in the thickness direction X is 1.5 MPa-2.0 MPa.

本申请实施例将电池单体10在厚度方向X上的膨胀压强限定在1.5MPa-2.0MPa,以在电池单体的循环过程中减小电池单体对第一汇流部件的拉力,降低电池单体与第一汇流部件连接失效的风险,提高电池的可靠性。In this embodiment, the expansion pressure of the battery cell 10 in the thickness direction X is limited to 1.5MPa-2.0MPa, so as to reduce the pulling force of the battery cell on the first busbar component during the battery cell cycle, reduce the risk of connection failure between the battery cell and the first busbar component, and improve the reliability of the battery.

在一些实施例中,第一汇流层31的厚度为1mm-2.5mm,可选为1.2mm-1.8mm。In some embodiments, the thickness of the first busbar 31 is 1mm-2.5mm, and optionally 1.2mm-1.8mm.

作为示例,第一汇流层31的厚度为1mm、1.2mm、1.3mm、1.4mm、1.5mm、1.6mm、1.7mm、1.8mm、1.9mm、2mm、2.1mm、2.2mm、2.3mm、2.4mm或2.5mm。As an example, the thickness of the first busbar 31 is 1 mm, 1.2 mm, 1.3 mm, 1.4 mm, 1.5 mm, 1.6 mm, 1.7 mm, 1.8 mm, 1.9 mm, 2 mm, 2.1 mm, 2.2 mm, 2.3 mm, 2.4 mm or 2.5 mm.

本申请实施例根据电池单体10的膨胀压强选择第一汇流层31的厚度,可以在一定程度上兼顾第一汇流层31的过流能力和第一汇流层31的可变形能力,从而提升电池2的快速充电能力和可靠性。The thickness of the first busbar 31 is selected according to the expansion pressure of the battery cell 10 in this embodiment, which can balance the current carrying capacity and deformability of the first busbar 31 to a certain extent, thereby improving the fast charging capability and reliability of the battery 2.

在一些实施例中,第二汇流层32的厚度为1mm-2.5mm,可选为1.2mm-1.8mm。作为示例,第二汇流层32的厚度为1mm、1.2mm、1.3mm、1.4mm、1.5mm、1.6mm、1.7mm、1.8mm、1.9mm、2mm、2.1mm、2.2mm、2.3mm、2.4mm或2.5mm。In some embodiments, the thickness of the second bus layer 32 is 1mm-2.5mm, optionally 1.2mm-1.8mm. As an example, the thickness of the second bus layer 32 is 1mm, 1.2mm, 1.3mm, 1.4mm, 1.5mm, 1.6mm, 1.7mm, 1.8mm, 1.9mm, 2mm, 2.1mm, 2.2mm, 2.3mm, 2.4mm, or 2.5mm.

第二汇流层32的厚度可以根据第一汇流层31的厚度以及电池对第一汇流部件的过流能力进行选择。示例性地,在第一汇流层31厚度较小时,第二汇流层32可具有大于第一汇流层31的厚度,以提升第一汇流部件的过流能力。The thickness of the second busbar 32 can be selected based on the thickness of the first busbar 31 and the current carrying capacity of the battery to the first busbar component. For example, when the thickness of the first busbar 31 is small, the second busbar 32 may have a greater thickness than the first busbar 31 to improve the current carrying capacity of the first busbar component.

在一些实施例中,电池单体10的体积能量密度为390Wh/L-450Wh/L,第一汇流层31的厚度小于或等于2.5mm。In some embodiments, the volumetric energy density of the battery cell 10 is 390Wh/L-450Wh/L, and the thickness of the first busbar 31 is less than or equal to 2.5mm.

电池单体10的体积能量密度为本领域公知的含义,可以采用本领域公知的设备和方法进行检测。 The volumetric energy density of the battery cell 10 has a meaning known in the art and can be tested using equipment and methods known in the art.

电池单体10的膨胀与其体积能量密度相关,本申请根据电池单体10的体积能量密度设计第一汇流层31的厚度,从而在一定程度上兼顾第一汇流层31的过流能力和第一汇流层31的可变形能力,从而提升电池2的快速充电能力和可靠性。The expansion of the battery cell 10 is related to its volumetric energy density. This application designs the thickness of the first busbar 31 based on the volumetric energy density of the battery cell 10, thereby taking into account the current carrying capacity and deformability of the first busbar 31 to a certain extent, thereby improving the fast charging capability and reliability of the battery 2.

在一些实施例中,电池单体10的体积能量密度为450Wh/L-480Wh/L,第一汇流层31的厚度小于或等于2.2mm。In some embodiments, the volumetric energy density of the battery cell 10 is 450Wh/L-480Wh/L, and the thickness of the first busbar 31 is less than or equal to 2.2mm.

电池单体10的膨胀与其体积能量密度相关,对于采用高体积能量密度的电池单体10的电池2,需要减小第一汇流层31的厚度。本申请实施例根据电池单体10的体积能量密度设计第一汇流层31的厚度,从而在一定程度上兼顾第一汇流层31的过流能力和第一汇流层31的可变形能力,从而提升电池2的快速充电能力和可靠性。The expansion of the battery cell 10 is related to its volumetric energy density. For the battery 2 using battery cells 10 with high volumetric energy density, the thickness of the first busbar 31 needs to be reduced. In this embodiment, the thickness of the first busbar 31 is designed according to the volumetric energy density of the battery cell 10, thereby balancing the current carrying capacity and deformability of the first busbar 31 to a certain extent, thus improving the fast charging capability and reliability of the battery 2.

在一些实施例中,负极活性材料中还包括硅基材料。硅基材料中硅元素在负极活性材料中的质量含量为1%-6%;第一汇流层31的厚度为1.2mm-2.2mm,第二汇流层32的厚度为1.2mm-2.2mm。In some embodiments, the negative electrode active material further includes a silicon-based material. The silicon content in the negative electrode active material is 1%-6% by mass; the thickness of the first busbar 31 is 1.2mm-2.2mm, and the thickness of the second busbar 32 is 1.2mm-2.2mm.

作为示例,硅基材料中硅元素在负极活性材料中的质量含量为1%、2%、3%、4%、5%或6%。作为示例,第一汇流层31的厚度为1.2mm、1.3mm、1.4mm、1.5mm、1.6mm、1.7mm、1.8mm、1.9mm、2mm、2.1mm或2.2mm。作为示例,第二汇流层32的厚度为1.2mm、1.3mm、1.4mm、1.5mm、1.6mm、1.7mm、1.8mm、1.9mm、2mm、2.1mm或2.2mm。As an example, the mass content of silicon in the negative electrode active material of the silicon-based material is 1%, 2%, 3%, 4%, 5%, or 6%. As an example, the thickness of the first busbar 31 is 1.2 mm, 1.3 mm, 1.4 mm, 1.5 mm, 1.6 mm, 1.7 mm, 1.8 mm, 1.9 mm, 2 mm, 2.1 mm, or 2.2 mm. As an example, the thickness of the second busbar 32 is 1.2 mm, 1.3 mm, 1.4 mm, 1.5 mm, 1.6 mm, 1.7 mm, 1.8 mm, 1.9 mm, 2 mm, 2.1 mm, or 2.2 mm.

通过引入硅基材料,可以提升负极片112的容量,提高电池单体10的能量密度。引入硅基材料,还会增大负极片112在循环过程中的膨胀,结合硅元素的含量设计第一汇流层31的厚度和第二汇流层32的厚度,可以降低因引入硅基材料而引发第一汇流层31与电池单体10连接失效的风险,并满足对第一汇流部件30a对过流能力的要求。By introducing silicon-based materials, the capacity of the negative electrode 112 can be increased, thereby improving the energy density of the battery cell 10. Introducing silicon-based materials also increases the expansion of the negative electrode 112 during cycling. By designing the thickness of the first busbar 31 and the second busbar 32 in conjunction with the silicon content, the risk of connection failure between the first busbar 31 and the battery cell 10 due to the introduction of silicon-based materials can be reduced, while also meeting the overcurrent capacity requirements of the first busbar component 30a.

在一些实施例中,第一汇流层31包括第一汇流部311、第二汇流部312以及连接第一汇流部311和第二汇流部312的第一缓冲部313,第一汇流部311和第二汇流部312沿厚度方向X设置并连接于不同的电池单体10。在第一汇流层31和第二汇流层32的层叠方向上,第一缓冲部313凸出于第一汇流部311和第二汇流部312。第一汇流层31在与第一缓冲部313对应的位置设有凹部314。In some embodiments, the first busbar layer 31 includes a first busbar 311, a second busbar 312, and a first buffer portion 313 connecting the first busbar 311 and the second busbar 312. The first busbar 311 and the second busbar 312 are disposed along the thickness direction X and connected to different battery cells 10. In the stacking direction of the first busbar layer 31 and the second busbar layer 32, the first buffer portion 313 protrudes from the first busbar 311 and the second busbar 312. The first busbar layer 31 has a recess 314 at a position corresponding to the first buffer portion 313.

通过设置凹部314,可减小第一缓冲部313的强度,便于第一缓冲部313在电池单体10膨胀时的变形。By providing the recess 314, the strength of the first buffer portion 313 can be reduced, which facilitates the deformation of the first buffer portion 313 when the battery cell 10 expands.

在一些实施例中,电池单体10的体积能量密度为390Wh/L-450Wh/L,凹部314的深度H2为1.2mm-2.5mm。In some embodiments, the volumetric energy density of the battery cell 10 is 390Wh/L-450Wh/L, and the depth H2 of the recess 314 is 1.2mm-2.5mm.

电池单体10的膨胀与其体积能量密度相关,本申请根据电池单体10的体积能量密度设计凹部314的深度,从而在一定程度上兼顾第一缓冲部313的过流能力和第一缓冲部313的可变形能力,从而提升电池2的快速充电能力和可靠性。The expansion of the battery cell 10 is related to its volumetric energy density. This application designs the depth of the recess 314 based on the volumetric energy density of the battery cell 10, thereby taking into account the overcurrent capacity and deformability of the first buffer portion 313 to a certain extent, thereby improving the fast charging capability and reliability of the battery 2.

在一些实施例中,电池单体10的体积能量密度为450Wh/L-480Wh/L,凹部314的深度为1mm-2.2mm。In some embodiments, the volumetric energy density of the battery cell 10 is 450Wh/L-480Wh/L, and the depth of the recess 314 is 1mm-2.2mm.

电池单体10的膨胀与其体积能量密度相关,对于采用高体积能量密度的电池单体10的电池2,需要降低第一缓冲部313变形的难度。本申请实施例根据电池单体10的体积能量密度设计凹部314的深度,从而在一定程度上兼顾第一缓冲部313的过流能力 和第一缓冲部313的可变形能力,从而提升电池2的快速充电能力和可靠性。The expansion of the battery cell 10 is related to its volumetric energy density. For the battery 2 using battery cells 10 with high volumetric energy density, it is necessary to reduce the difficulty of deformation of the first buffer portion 313. In this embodiment, the depth of the recess 314 is designed according to the volumetric energy density of the battery cell 10, thereby taking into account the current carrying capacity of the first buffer portion 313 to a certain extent. The deformability of the first buffer section 313 enhances the fast charging capability and reliability of the battery 2.

在一些实施例中,电池2还包括箱体20。箱体20用于容纳多个电池单体10。箱体20包括至少两个限位梁21,相邻两个限位梁21沿厚度方向X布置,多个电池单体10布置于相邻的限位梁21之间。In some embodiments, the battery 2 further includes a housing 20. The housing 20 is used to accommodate a plurality of battery cells 10. The housing 20 includes at least two limiting beams 21, with adjacent limiting beams 21 arranged along the thickness direction X, and the plurality of battery cells 10 arranged between adjacent limiting beams 21.

作为示例,任意相邻的两个限位梁21之间设置有至少一个电池单体列100。As an example, at least one battery cell row 100 is provided between any two adjacent limiting beams 21.

限位梁21可用于限制电池单体10在厚度方向X上的膨胀变形。限位梁21可以在厚度方向X上与电池单体10直接相抵;可替代地,限位梁21与电池单体10之间也可设置其它部件,即限位梁21通过该部件限制电池单体10的膨胀。The limiting beam 21 can be used to limit the expansion and deformation of the battery cell 10 in the thickness direction X. The limiting beam 21 can directly abut against the battery cell 10 in the thickness direction X; alternatively, other components can also be provided between the limiting beam 21 and the battery cell 10, that is, the limiting beam 21 limits the expansion of the battery cell 10 through these components.

限位梁21可以在电池的循环过程中限制电池单体10的膨胀,从而减小电池单体10对第一汇流部件30a施加的拉力,降低电池单体10与第一汇流部件30a连接失效的风险,提高电池的可靠性。The limiting beam 21 can restrict the expansion of the battery cell 10 during battery cycling, thereby reducing the tensile force exerted by the battery cell 10 on the first busbar component 30a, reducing the risk of connection failure between the battery cell 10 and the first busbar component 30a, and improving the reliability of the battery.

在一些实施例中,电极组件11包括两个第一表面11d和两个第二表面11e,两个第一表面11d沿厚度方向X相对设置,两个第二表面11e沿与厚度方向X垂直的方向相对设置,第二表面11e连接两个第一表面11d。第一表面11d的面积大于第二表面11e的面积。In some embodiments, the electrode assembly 11 includes two first surfaces 11d and two second surfaces 11e. The two first surfaces 11d are disposed opposite each other along the thickness direction X, and the two second surfaces 11e are disposed opposite each other along a direction perpendicular to the thickness direction X. The second surfaces 11e connect the two first surfaces 11d. The area of the first surfaces 11d is larger than the area of the second surfaces 11e.

将面积较大的第一表面11d与限位梁21沿厚度方向X相对,可以在电极组件11膨胀时,增大限位梁21的受力面积,减小限位梁21的变形。By positioning the larger first surface 11d opposite the limiting beam 21 along the thickness direction X, the force-bearing area of the limiting beam 21 can be increased and the deformation of the limiting beam 21 can be reduced when the electrode assembly 11 expands.

在一些实施例中,限位梁21沿宽度方向Y延伸。In some embodiments, the limiting beam 21 extends along the width direction Y.

在一些实施例中,两个第二表面11e沿宽度方向Y相对设置。In some embodiments, the two second surfaces 11e are arranged opposite each other along the width direction Y.

在一些实施例中,主体部11a包括两个第一表面11d、两个第二表面11e和两个第三表面11f;两个第三表面11f位于电池单体10沿高度方向Z的两端,第三表面11f连接于两个第一表面11d和两个第二表面11e。In some embodiments, the main body 11a includes two first surfaces 11d, two second surfaces 11e, and two third surfaces 11f; the two third surfaces 11f are located at both ends of the battery cell 10 along the height direction Z, and the third surfaces 11f are connected to the two first surfaces 11d and the two second surfaces 11e.

正极耳11b和负极耳11c从同一个第三表面11f延伸出,或者,正极耳11b和负极耳11c分别从两个第三表面11f延伸出。The positive electrode tab 11b and the negative electrode tab 11c extend from the same third surface 11f, or the positive electrode tab 11b and the negative electrode tab 11c extend from two different third surfaces 11f.

在一些实施例中,第二表面11e的至少部分为弧形。可选地,电极组件11为卷绕结构,第二表面11e为弧面。In some embodiments, at least a portion of the second surface 11e is arc-shaped. Optionally, the electrode assembly 11 is a wound structure, and the second surface 11e is an arc surface.

在一些实施例中,大面10a与第一表面11d平行。In some embodiments, the large surface 10a is parallel to the first surface 11d.

在一些实施例中,电池单体10为方壳电池单体。可选地,窄面10b垂直于大面10a。In some embodiments, the battery cell 10 is a prismatic battery cell. Optionally, the narrow face 10b is perpendicular to the large face 10a.

在一些实施例中,负极集流体1121的一部分未被负极膜层1122覆盖;负极集流体1121的未被负极膜层1122覆盖的部分可用于形成负极耳11c。In some embodiments, a portion of the negative electrode current collector 1121 is not covered by the negative electrode film layer 1122; the portion of the negative electrode current collector 1121 not covered by the negative electrode film layer 1122 may be used to form a negative electrode tab 11c.

在一些实施例中,负极集流体1121的厚度为4μm至6μm。示例性地,负极集流体1121的厚度为4μm、4.5μm、5μm、5.5μm、6μm或是上述任意两个数值组成的范围。In some embodiments, the thickness of the negative electrode current collector 1121 is 4 μm to 6 μm. Exemplarily, the thickness of the negative electrode current collector 1121 is 4 μm, 4.5 μm, 5 μm, 5.5 μm, 6 μm, or any range of two of the above values.

在一些实施例中,负极膜层1122于电池单体100%SOC下的压实密度为1.15g/cm3至1.36g/cm3。示例性地,电池单体10于100%荷电状态下,负极膜层1122的压实密度为1.15g/cm3、1.18g/cm3、1.20g/cm3、1.22g/cm3、1.25g/cm3、1.28g/cm3、1.3g/cm3、1.32g/cm3、1.35g/cm3、1.36g/cm3或是上述任意两个数值组成的范围。In some embodiments, the compaction density of the negative electrode film layer 1122 at 100% SOC of the battery cell is 1.15 g/ cm³ to 1.36 g/ cm³ . Exemplarily, the compaction density of the negative electrode film layer 1122 at 100% SOC of the battery cell 10 is 1.15 g/ cm³ , 1.18 g/ cm³ , 1.20 g/ cm³ , 1.22 g/ cm³ , 1.25 g/ cm³ , 1.28 g/ cm³ , 1.3 g/ cm³ , 1.32 g/ cm³ , 1.35 g/ cm³ , 1.36 g/ cm³ , or a range consisting of any two of the above values.

示例性地,100%SOC(state of charge,荷电状态)和0%SOC按照如下方式定义:For example, 100% SOC (state of charge) and 0% SOC are defined as follows:

将电池单体以0.33C的恒流充电倍率充电至电池充电上限电压,再恒压充电至 0.05C,对应电池单体100%SOC的状态;将电池单体以0.33C的恒流放电倍率放电至截止电压,对应电池单体0%SOC的状态。示范性的,电池充电上限电压可以为3.8V;电池放电截止电压可以为2.0V。The battery cells are charged at a constant current rate of 0.33C to the upper limit of the battery charging voltage, and then charged at a constant voltage until... 0.05C corresponds to a 100% SOC state for a single battery cell; discharging a single battery cell at a constant current discharge rate of 0.33C to the cutoff voltage corresponds to a 0% SOC state for the single battery cell. For example, the upper limit voltage for battery charging can be 3.8V; the battery discharge cutoff voltage can be 2.0V.

示例性地,电池单体于100%荷电状态下负极膜层的压实密度为本领域公知的含义,也即对100%SOC下的电池单体拆解出负极片,测定负极膜层的压实密度;例如取单面涂布的负极片(若是双面涂布的负极片,可先擦拭掉其中一面的负极膜层),冲切成面积为S1的小圆片,称其重量,记录为M1,量取其厚度H1。然后将上述称重后的负极片的负极膜层擦拭掉,称量负极集流体的重量,记录为M0,量取其厚度H0。负极膜层的单面涂布重量=(负极片的重量M1-负极集流体的重量M0)/S1,负极膜层的厚度=负极片的厚度H1-负极集流体的厚度H0,负极膜层的压实密度=负极膜层的单面涂布重量/负极膜层的厚度。For example, the compaction density of the negative electrode film layer of a battery cell at 100% SOC is a well-known concept in the art, meaning that the negative electrode sheet is disassembled from the battery cell at 100% SOC, and the compaction density of the negative electrode film layer is measured. For example, a single-sided coated negative electrode sheet (if it is a double-sided coated negative electrode sheet, the negative electrode film layer on one side can be wiped off first) is cut into a small circular piece with an area of S1, its weight is weighed and recorded as M1, and its thickness H1 is measured. Then, the negative electrode film layer of the weighed negative electrode sheet is wiped off, the weight of the negative electrode current collector is weighed and recorded as M0, and its thickness H0 is measured. The single-sided coating weight of the negative electrode film layer = (weight of the negative electrode sheet M1 - weight of the negative electrode current collector M0) / S1, the thickness of the negative electrode film layer = thickness of the negative electrode sheet H1 - thickness of the negative electrode current collector H0, and the compaction density of the negative electrode film layer = single-sided coating weight of the negative electrode film layer / thickness of the negative electrode film layer.

负极膜层1122的压实密度与电池单体10于100%荷电状态的膨胀相关,将负极膜层1122的压实密度限定在1.15g/cm3至1.36g/cm3,能够在一定程度上兼顾电池单体10的能量密度和膨胀压强,减小电池单体10的变形,降低电池单体10与汇流部件连接失效的风险。The compaction density of the negative electrode film layer 1122 is related to the expansion of the battery cell 10 at 100% charge. Limiting the compaction density of the negative electrode film layer 1122 to 1.15 g/ cm3 to 1.36 g/ cm3 can, to a certain extent, balance the energy density and expansion pressure of the battery cell 10, reduce the deformation of the battery cell 10, and reduce the risk of failure of the connection between the battery cell 10 and the busbar component.

负极膜层1122的压实密度在上述范围时,有利于提升电池单体10的能量密度;且由于负极膜层1122中的负极活性材料堆积较为紧密,颗粒与颗粒间接触电阻较小,能够降低负极片112的电阻,从而降低产热。When the compaction density of the negative electrode film layer 1122 is within the above range, it is beneficial to improve the energy density of the battery cell 10; and since the negative electrode active material in the negative electrode film layer 1122 is packed more tightly, the contact resistance between particles is smaller, which can reduce the resistance of the negative electrode sheet 112, thereby reducing heat generation.

负极膜层1122的压实密度在上述范围时,可提升电池单体10的快速充电能力。负极膜层1122的压实密度较小,可增大负极片112的孔隙率,减缓负极片的膨胀,减小电池单体10的膨胀压强。When the compaction density of the negative electrode film layer 1122 is within the above range, the fast charging capability of the battery cell 10 can be improved. A lower compaction density of the negative electrode film layer 1122 can increase the porosity of the negative electrode sheet 112, slow down the expansion of the negative electrode sheet, and reduce the expansion pressure of the battery cell 10.

在一些实施例中,负极膜层1122于电池单体100%SOC下的压实密度为1.25g/cm3至1.36g/cm3,可提升电池单体10的能量密度。In some embodiments, the negative electrode film layer 1122 has a compaction density of 1.25 g/ cm³ to 1.36 g/ cm³ at 100% SOC of the battery cell, which can improve the energy density of the battery cell 10.

在一些实施例中,负极膜层1122的单面涂布重量为90mg/1540mm2至170mg/1540mm2。示例性地,负极膜层1122的单面涂布重量为90mg/1540.25mm2、92mg/1540.25mm2、95mg/1540.25mm2、96mg/1540.25mm2、100mg/1540.25mm2、102mg/1540.25mm2、104mg/1540.25mm2、105mg/1540.25mm2、108mg/1540.25mm2、110mg/1540.25mm2、112mg/1540.25mm2、114mg/1540.25mm2、115mg/1540.25mm2、116mg/1540.25mm2、118mg/1540.25mm2、120mg/1540.25mm2、122mg/1540.25mm2、125mg/1540.25mm2、128mg/1540.25mm2、130mg/1540.25mm2、132mg/1540.25mm2、135mg/1540.25mm2、137mg/1540.25mm2、140mg/1540.25mm2、142mg/1540.25mm2、145mg/1540.25mm2、148mg/1540.25mm2、150mg/1540.25mm2、152mg/1540.25mm2、155mg/1540.25mm2、160mg/1540.25mm2、165mg/1540.25mm2、167mg/1540.25mm2、170mg/1540.25mm2或是上述任意两个数值组成的范围。In some embodiments, the single-sided coating weight of the negative electrode film layer 1122 is 90 mg/1540 mm² to 170 mg/1540 mm² . For example, the single-sided coating weight of the negative electrode film layer 1122 is 90 mg/1540.25 mm² , 92 mg/1540.25 mm² , 95 mg/1540.25 mm² , 96 mg/1540.25 mm² , 100 mg/1540.25 mm² , 102 mg/1540.25 mm² , 104 mg/1540.25 mm² , 105 mg/1540.25 mm² , 108 mg/1540.25 mm² , 110 mg/1540.25 mm² , 112 mg/1540.25 mm² , 114 mg/1540.25 mm² , or 115 mg/1540.25 mm². , 116mg/1540.25mm 2 , 118mg/1540.25mm 2 , 120mg/1540.25mm 2 , 122mg/1540.25mm 2 , 125mg/1540.25mm 2 , 128mg/1540.25mm 2 , 130mg/1540.25mm 2 , 132mg/1540.25mm 2 , 135mg/1540.25mm 2 , 137mg/1540.25mm 2 , 140mg/1540.25mm 2 , 142mg/1540.25mm 2 , 145mg/1540.25mm 2 ,148mg/1540.25mm 2 150mg/1540.25mm² , 152mg/1540.25mm² , 155mg/1540.25mm² , 160mg/1540.25mm² , 165mg/1540.25mm² , 167mg/1540.25mm², 170mg /1540.25mm² , or a range consisting of any two of the above values.

负极膜层1122的单面涂布重量与负极膜层的膨胀相关,将负极膜层1122的单面涂布重量限定在90mg/1540mm2至170mg/1540mm2,能够在一定程度上兼顾电池单体10的能量密度和膨胀压强,减小电池单体10的变形,降低电池单体10与汇流部件连接失效的风险。 The single-sided coating weight of the negative electrode film layer 1122 is related to the expansion of the negative electrode film layer. Limiting the single-sided coating weight of the negative electrode film layer 1122 to 90mg/1540mm2 to 170mg/ 1540mm2 can, to a certain extent, balance the energy density and expansion pressure of the battery cell 10, reduce the deformation of the battery cell 10, and reduce the risk of connection failure between the battery cell 10 and the busbar component.

另外,将负极膜层1122的单面涂布重量限定在90mg/1540mm2至170mg/1540mm2,还能够限制单位面积的负极片112的产热量,降低电池单体10的温升,特别是在快速充电时的温升。In addition, limiting the single-sided coating weight of the negative electrode film 1122 to 90mg/ 1540mm² to 170mg/ 1540mm² can also limit the heat generation per unit area of the negative electrode sheet 112, reduce the temperature rise of the battery cell 10, especially during fast charging.

在一些实施例中,负极膜层1122的单面涂布重量为110mg/1540mm2至150mg/1540mm2,以进一步兼顾电池单体10的能量密度和膨胀压强。In some embodiments, the single-sided coating weight of the negative electrode film layer 1122 is 110 mg/1540 mm² to 150 mg/1540 mm² , in order to further balance the energy density and expansion pressure of the battery cell 10.

在一些实施例中,负极片112的孔隙率为27%-40%。作为示例,负极片112的孔隙率可为27%、28%、29%、30%、31%、32%、33%、34%、35%、36%、37%、38%、39%或40%。In some embodiments, the porosity of the negative electrode 112 is 27%-40%. As an example, the porosity of the negative electrode 112 may be 27%, 28%, 29%, 30%, 31%, 32%, 33%, 34%, 35%, 36%, 37%, 38%, 39%, or 40%.

负极片的孔隙率可为负极片内的孔体积占负极片总体积的百分率。示例性地,在电池单体处于0%荷电状态时,取双侧涂布的负极片;由真密度仪AccuPycⅡ1340按照国标GB/T 24586-2009执行以测得负极片的孔隙率。The porosity of the negative electrode sheet can be defined as the percentage of the pore volume within the negative electrode sheet to its total volume. For example, when the battery cell is at 0% state of charge, a negative electrode sheet with double-sided coating is taken; the porosity of the negative electrode sheet is measured using a true density meter AccuPycⅡ1340 according to national standard GB/T 24586-2009.

在本申请实施例中,负极片112的孔隙率大于或等于27%,可为负极片112因发生副反应所产生的杂质提供空间,减缓负极片112的膨胀,减小电池单体10的膨胀压强,降低电池单体10的变形,改善电池单体10的循环性能,降低电池单体与汇流部件连接失效的风险。负极片112的孔隙率小于或等于40%,可兼顾电池单体10的能量密度。In this embodiment, the porosity of the negative electrode 112 is greater than or equal to 27%, which provides space for impurities generated by side reactions in the negative electrode 112, slows down the expansion of the negative electrode 112, reduces the expansion pressure of the battery cell 10, reduces the deformation of the battery cell 10, improves the cycle performance of the battery cell 10, and reduces the risk of connection failure between the battery cell and the busbar component. The porosity of the negative electrode 112 is less than or equal to 40%, which can balance the energy density of the battery cell 10.

在一些实施例中,碳基材料包括石墨颗粒,石墨颗粒的石墨化度为92.0%至94.5%。示例性地,石墨颗粒的石墨化度为92.0%、92.5%、93%、93.5%、94%、94.5%或是上述任意两个数值组成的范围。In some embodiments, the carbon-based material includes graphite particles with a graphitization degree of 92.0% to 94.5%. Exemplarily, the graphitization degree of the graphite particles is 92.0%, 92.5%, 93%, 93.5%, 94%, 94.5%, or a range consisting of any two of the above values.

石墨颗粒的石墨化度在上述范围时,石墨颗粒的导电性能较为优异,能够降低负极片112的产热,降低电池单体10的产热;并且能够提升电池单体10的快速充电性能。When the degree of graphitization of the graphite particles is within the above range, the graphite particles have excellent electrical conductivity, which can reduce the heat generation of the negative electrode 112 and the heat generation of the battery cell 10; and can improve the fast charging performance of the battery cell 10.

在一些实施例中,碳基材料包括人造石墨和天然石墨中的至少一种。人造石墨和天然石墨的导电性能好,可减少负极片112在充电时的产热,提升电池单体10的快速充电性能。In some embodiments, the carbon-based material includes at least one of artificial graphite and natural graphite. Artificial and natural graphite have good electrical conductivity, which can reduce heat generation of the negative electrode 112 during charging and improve the fast-charging performance of the battery cell 10.

在一些实施例中,负极活性材料中还包括硅基材料。硅基材料的引入能够提升负极活性材料的容量,提高电池单体10的能量密度。In some embodiments, the negative electrode active material further includes a silicon-based material. The introduction of a silicon-based material can improve the capacity of the negative electrode active material and increase the energy density of the battery cell 10.

在一些实施例中,硅基材料中硅元素在负极活性材料中的质量含量为0.3%至10%,可选为1%至6%。示例性地,硅元素在负极活性材料中的质量含量为0.3%、0.5%、0.8%、1%、1.2%、1.5%、1.8%、2%、2.2%、2.5%、2.8%、3%、3.2%、3.5%、3.8%、4%、4.2%、4.5%、4.8%、5%、5.2%、5.5%、5.8%、6%、6.2%、6.5%、6.8%、7%、7.2%、7.5%、7.8%、8%、8.2%、8.5%、8.8%、9%、9.2%、9.5%、9.8%、10%或是上述任意两个数值组成的范围。In some embodiments, the mass content of silicon in the silicon-based material in the negative electrode active material is 0.3% to 10%, optionally 1% to 6%. Exemplarily, the mass content of silicon in the negative electrode active material is 0.3%, 0.5%, 0.8%, 1%, 1.2%, 1.5%, 1.8%, 2%, 2.2%, 2.5%, 2.8%, 3%, 3.2%, 3.5%, 3.8%, 4%, 4.2%, 4.5%, 4.8%, 5%, 5.2%, 5.5%, 5.8%, 6%, 6.2%, 6.5%, 6.8%, 7%, 7.2%, 7.5%, 7.8%, 8%, 8.2%, 8.5%, 8.8%, 9%, 9.2%, 9.5%, 9.8%, 10%, or a range consisting of any two of the above values.

在负极片112中引入硅基材料,既可以提升容量,还会增大负极片112的膨胀。因此,将硅元素在负极活性材料中的质量含量限定为0.3%至10%,可以在一定程度上兼顾电池单体10的能量密度和膨胀,减小电池单体10的变形,降低电池单体与汇流部件连接失效的风险,改善电池单体10的循环性能。Introducing silicon-based materials into the negative electrode 112 can increase capacity but also increase the expansion of the negative electrode 112. Therefore, limiting the mass content of silicon in the negative electrode active material to 0.3% to 10% can, to a certain extent, balance the energy density and expansion of the battery cell 10, reduce the deformation of the battery cell 10, reduce the risk of connection failure between the battery cell and the busbar component, and improve the cycle performance of the battery cell 10.

本申请中各物质或各元素的定性及其定量可以用本领域技术人员已知的合适的设备和方法进行检测,相关检测方法可以参考国内外检测标准、国内外企业标准等,并 且本领域技术人员也可以从检测准确性角度出发适应性改变某些检测步骤/仪器参数等,以获得更加准确的检测结果。可以使用一种检测方法定性或定量,也可以联合使用几种检测方法定性或定量测定。The qualitative and quantitative analysis of each substance or element in this application can be performed using suitable equipment and methods known to those skilled in the art. Relevant testing methods can be referenced from domestic and international testing standards, domestic and international enterprise standards, etc. Furthermore, those skilled in the art can adaptively modify certain testing steps/instrument parameters from the perspective of testing accuracy to obtain more accurate testing results. A single testing method can be used for qualitative or quantitative determination, or several testing methods can be used in combination for qualitative or quantitative determination.

例如,硅基材料可以结合JIS/K0131-1996X射线衍射分析法通则对负极片或负极活性材料进行X射线粉末衍射测试并定性分析。For example, silicon-based materials can be subjected to X-ray powder diffraction tests and qualitative analysis on negative electrode sheets or negative electrode active materials in accordance with the general rules of X-ray diffraction analysis in JIS/K0131-1996.

在一些实施例中,硅基材料可包括单质硅、硅氧化物、硅碳复合物、硅氮复合物和硅合金材料中的至少一种。In some embodiments, the silicon-based material may include at least one of elemental silicon, silicon oxide, silicon-carbon composite, silicon-nitrogen composite, and silicon alloy material.

在一些实施例中,硅基材料包括硅氧化合物和硅碳复合物中的至少一种。In some embodiments, the silicon-based material includes at least one of silicon oxides and silicon-carbon composites.

在一些实施方式中,负极活性材料除了包括碳基材料,可选的硅基材料外,还可以包括锡基材料和钛酸锂中的至少一种。锡基材料可包括单质锡、锡氧化物和锡合金材料中的至少一种。In some embodiments, the negative electrode active material may include, in addition to carbon-based materials and optionally silicon-based materials, at least one of tin-based materials and lithium titanate. Tin-based materials may include at least one of elemental tin, tin oxide, and tin alloy materials.

在一些实施方式中,本申请实施方式中负极膜层1122包括至少一层膜层,换言之,负极膜层1122可以采用单层膜层,也可以采用至少两层膜层。可选地,负极膜层1122包括至少两层膜层。In some embodiments, the negative electrode film layer 1122 in this application includes at least one film layer; in other words, the negative electrode film layer 1122 can be a single film layer or at least two film layers. Optionally, the negative electrode film layer 1122 includes at least two film layers.

在负极膜层1122采用单层膜层的情况下,负极膜层1122中负极活性材料包括碳基材料,可选地还包括硅基材料。在采用单层膜层的情况下,负极活性材料的体积平均粒径Dv50为8.2μm至13.5μm。示例性地,负极活性材料的体积平均粒径Dv50为8.2μm、8.5μm、8.8μm、9μm、9.2μm、9.5μm、9.8μm、10μm、10.2μm、10.5μm、10.8μm、11μm、11.2μm、11.5μm、11.8μm、12μm、12.2μm、12.5μm、12.8μm、13μm、13.2μm、13.5μm或是上述任意两个数值组成的范围。When the negative electrode film layer 1122 is a single layer, the negative electrode active material in the negative electrode film layer 1122 includes a carbon-based material, and optionally also includes a silicon-based material. When a single layer is used, the volume average particle size Dv50 of the negative electrode active material is from 8.2 μm to 13.5 μm. Exemplarily, the volume average particle size Dv50 of the negative electrode active material is 8.2 μm, 8.5 μm, 8.8 μm, 9 μm, 9.2 μm, 9.5 μm, 9.8 μm, 10 μm, 10.2 μm, 10.5 μm, 10.8 μm, 11 μm, 11.2 μm, 11.5 μm, 11.8 μm, 12 μm, 12.2 μm, 12.5 μm, 12.8 μm, 13 μm, 13.2 μm, 13.5 μm, or a range consisting of any two of the above values.

在负极膜层1122采用至少两层膜层的情况下,负极膜层1122中负极活性材料包括碳基材料,可选地还包括硅基材料,硅基材料可以位于至少两层膜层中的其中一层,也可以位于至少两层膜层中的至少两层中。负极膜层1122可以包括两层膜层、三层膜层、四层膜层,甚至更多层膜层。When the negative electrode film layer 1122 employs at least two film layers, the negative electrode active material in the negative electrode film layer 1122 includes a carbon-based material, and optionally also includes a silicon-based material. The silicon-based material may be located in one of the at least two film layers, or in at least two of the at least two film layers. The negative electrode film layer 1122 may include two film layers, three film layers, four film layers, or even more film layers.

在一些实施例中,负极膜层1122包括第一负极膜层11221和第二负极膜层11222,第二负极膜层11222设置于第一负极膜层11221和负极集流体1121之间。负极活性材料包括设置于第一负极膜层11221的第一负极活性材料和设置于第二负极膜层11222的第二负极活性材料,第一负极活性材料包括人造石墨,第二负极活性材料包括人造石墨、天然石墨和硅基材料的一种或多种。In some embodiments, the negative electrode film layer 1122 includes a first negative electrode film layer 11221 and a second negative electrode film layer 11222, wherein the second negative electrode film layer 11222 is disposed between the first negative electrode film layer 11221 and the negative electrode current collector 1121. The negative electrode active material includes a first negative electrode active material disposed in the first negative electrode film layer 11221 and a second negative electrode active material disposed in the second negative electrode film layer 11222. The first negative electrode active material includes artificial graphite, and the second negative electrode active material includes one or more of artificial graphite, natural graphite, and silicon-based materials.

第一负极膜层11221和第二负极膜层11222的界面规则,也可以不规则;可选地为不规则。The interface between the first negative electrode film layer 11221 and the second negative electrode film layer 11222 can be regular or irregular; optionally, it can be irregular.

第一负极膜层11221和第二负极膜层11222可以进行差异化设置,从而在一定程度上兼顾负极膜层1122的膨胀和容量;双层涂布能够构造负极膜层1122的孔隙差异,降低离子传输曲折度,减少副反应,提升电池单体10的快速充电性能。The first negative electrode film layer 11221 and the second negative electrode film layer 11222 can be configured differently, thereby taking into account the expansion and capacity of the negative electrode film layer 1122 to a certain extent; the double coating can create the porosity difference of the negative electrode film layer 1122, reduce the tortuosity of ion transport, reduce side reactions, and improve the fast charging performance of the battery cell 10.

人造石墨可以具有较小的体积平均粒径Dv50,一方面能够缩短锂离子的固相传输路径,提升快速充电性能;另一方面,材料在制备过程中不易发生团聚,能够提升材料的稳定性。Artificial graphite can have a small volume average particle size Dv50, which can shorten the solid-phase transport path of lithium ions and improve fast charging performance. On the other hand, the material is less prone to agglomeration during the preparation process, which can improve the stability of the material.

在一些实施例中,第一负极膜层11221的厚度和第二负极膜层11222的厚度比值为 3:7至7:3。作为示例,第一负极膜层11221的厚度和第二负极膜层11222的厚度比值为3:7、4:6、5:5、6:4或7:3。In some embodiments, the ratio of the thickness of the first negative electrode film 11221 to the thickness of the second negative electrode film 11222 is: 3:7 to 7:3. As an example, the thickness ratio of the first negative electrode film layer 11221 to the thickness ratio of the second negative electrode film layer 11222 is 3:7, 4:6, 5:5, 6:4 or 7:3.

可选地,第一负极膜层11221的厚度和第二负极膜层11222的厚度比值为4:6至6:4。Optionally, the thickness ratio of the first negative electrode film layer 11221 to the thickness ratio of the second negative electrode film layer 11222 is 4:6 to 6:4.

通过调整第一负极膜层11221和第二负极膜层11222的厚度占比,能够进一步增加上下层的梯度孔隙差异,降低锂离子传输曲折度,提升电池单体10的快速充电能力。By adjusting the thickness ratio of the first negative electrode film layer 11221 and the second negative electrode film layer 11222, the gradient porosity difference between the upper and lower layers can be further increased, the lithium-ion transport tortuosity can be reduced, and the fast charging capability of the battery cell 10 can be improved.

在一些实施例中,第一负极膜层11221的厚度小于或等于第二负极膜层11222的厚度,可进一步提升电池单体10的快速充电能力。In some embodiments, the thickness of the first negative electrode film layer 11221 is less than or equal to the thickness of the second negative electrode film layer 11222, which can further improve the fast charging capability of the battery cell 10.

在一些实施例中,第一负极活性材料为颗粒状,第二负极活性材料为颗粒状。In some embodiments, the first negative electrode active material is in particulate form, and the second negative electrode active material is in particulate form.

在一些实施例中,第一负极活性材料的体积平均粒径Dv50小于或等于第二负极活性材料的体积平均粒径Dv50。进一步可选地,第一负极活性材料的体积平均粒径Dv50小于第二负极活性材料的体积平均粒径Dv50。In some embodiments, the volume average particle size Dv50 of the first negative electrode active material is less than or equal to the volume average particle size Dv50 of the second negative electrode active material. Further optionally, the volume average particle size Dv50 of the first negative electrode active material is less than the volume average particle size Dv50 of the second negative electrode active material.

第一负极活性材料和第二负极活性材料的颗粒粒径存在差异,能够提升电池单体10的快速充电性能;在快速充电过程中,第一负极膜层11221的过电势通常较高,快速充电的瓶颈主要在于第一负极膜层11221,而本申请实施方式中第一负极活性材料的颗粒粒径相对较小,能够缩短离子的固相传输路径,提升快速充电性能,并能够改善负极片112表层离子析出问题。第二负极活性材料的颗粒粒径相对较大,可使第二负极膜层11222中形成较大的孔隙,在充电时,孔隙可以吸收膨胀,减小负极膜层1122的膨胀量,减小电池单体10对第一汇流部件30a施加的力,降低电池单体10与第一汇流部件30a连接失效的风险。The difference in particle size between the first and second negative electrode active materials improves the fast-charging performance of the battery cell 10. During fast charging, the overpotential of the first negative electrode film 11221 is typically high, and the bottleneck of fast charging mainly lies in the first negative electrode film 11221. However, in this embodiment, the particle size of the first negative electrode active material is relatively small, which can shorten the solid-phase transport path of ions, improve fast-charging performance, and alleviate the problem of ion deposition on the surface of the negative electrode sheet 112. The particle size of the second negative electrode active material is relatively large, which can form larger pores in the second negative electrode film 11222. During charging, the pores can absorb expansion, reducing the expansion of the negative electrode film 1122, reducing the force exerted by the battery cell 10 on the first busbar component 30a, and reducing the risk of connection failure between the battery cell 10 and the first busbar component 30a.

在一些实施例中,第一负极活性材料的体积平均粒径Dv50为7.8μm-14.3μm,可选为7.8μm-11.3μm。示例性地,第一负极活性材料的体积平均粒径Dv50为7.8μm、8.0μm、8.2μm、8.5μm、8.8μm、9μm、9.2μm、9.5μm、9.8μm、10μm、10.2μm、10.5μm、10.8μm、11μm、11.3μm、11.2μm、11.5μm、11.8μm、12μm、12.2μm、12.5μm、12.8μm、13μm、13.2μm、13.5μm、13.8μm、14μm、14.1μm、14.3μm或是上述任意两个数值组成的范围。In some embodiments, the volume average particle size Dv50 of the first negative electrode active material is 7.8 μm-14.3 μm, and optionally 7.8 μm-11.3 μm. For example, the volume average particle size Dv50 of the first negative electrode active material is 7.8 μm, 8.0 μm, 8.2 μm, 8.5 μm, 8.8 μm, 9 μm, 9.2 μm, 9.5 μm, 9.8 μm, 10 μm, 10.2 μm, 10.5 μm, 10.8 μm, 11 μm, 11.3 μm, 11.2 μm, 11.5 μm, 11.8 μm, 12 μm, 12.2 μm, 12.5 μm, 12.8 μm, 13 μm, 13.2 μm, 13.5 μm, 13.8 μm, 14 μm, 14.1 μm, 14.3 μm, or a range of any two of the above values.

第一负极活性材料的体积平均粒径Dv50设置为7.8μm-14.3μm,一方面能够缩短锂离子的固相传输路径,提升快速充电性能;另一方面,材料在制备过程中不易发生团聚,能够提升材料的稳定性;再一方面,上述体积平均粒径范围的第一负极活性材料能够与第二负极活性材料配合,有利于构建第一负极膜层11221和第二负极膜层11222的梯度孔隙差异,降低锂离子传输曲折度,提升电池单体10的快速充电性能。The volume average particle size Dv50 of the first negative electrode active material is set to 7.8μm-14.3μm. On the one hand, this can shorten the solid-phase transport path of lithium ions and improve fast charging performance. On the other hand, the material is less prone to agglomeration during preparation, which can improve the stability of the material. Furthermore, the first negative electrode active material in the above-mentioned volume average particle size range can cooperate with the second negative electrode active material, which is conducive to constructing the gradient porosity difference between the first negative electrode film layer 11221 and the second negative electrode film layer 11222, reducing the tortuosity of lithium ion transport, and improving the fast charging performance of the battery cell 10.

材料的体积平均粒度Dv50是指体积分布中50%所对应的粒度,材料的体积平均粒度Dv10是指体积分布中10%所对应的粒度,可以采用本领域公知的设备和方法进行检测,例如将负极活性材料作为样品,依据测试标准GB/T 19077-2016,通过Mastersizer2000E型激光粒度分析仪测试颗粒的Dv50和Dv10等。The volume average particle size Dv50 of a material refers to the particle size corresponding to 50% of the volume distribution, and the volume average particle size Dv10 of a material refers to the particle size corresponding to 10% of the volume distribution. They can be detected using equipment and methods known in the art. For example, using the negative electrode active material as a sample, the Dv50 and Dv10 of the particles can be tested using a Mastersizer2000E laser particle size analyzer according to the testing standard GB/T 19077-2016.

在一些实施例中,第二负极活性材料的体积平均粒径Dv50为9.5μm-18.5μm,可选为9.5-14.6μm。In some embodiments, the volume average particle size Dv50 of the second negative electrode active material is 9.5 μm-18.5 μm, and optionally 9.5-14.6 μm.

示例性地,第二负极活性材料的体积平均粒径Dv50为9.5μm、10μm、10.5μm、11μm、11.5μm、12μm、12.5μm、13μm、13.5μm、14μm、14.5μm、14.6μm、15μm、 15.5μm、16μm、16.5μm、17μm、17.5μm、18μm、18.5μm或是上述任意两个数值组成的范围。For example, the volume average particle size Dv50 of the second negative electrode active material is 9.5 μm, 10 μm, 10.5 μm, 11 μm, 11.5 μm, 12 μm, 12.5 μm, 13 μm, 13.5 μm, 14 μm, 14.5 μm, 14.6 μm, 15 μm, 15.5μm, 16μm, 16.5μm, 17μm, 17.5μm, 18μm, 18.5μm or any range of two of the above values.

第二负极活性材料的体积平均粒径Dv50在9.5μm-18.5μm,可以使第二负极膜层11222的孔隙更加丰富,有利于提升电池单体10的快速充电能力,并减小负极膜层1122在充电过程中的膨胀。The volume average particle size Dv50 of the second negative electrode active material is between 9.5 μm and 18.5 μm, which can make the pores of the second negative electrode film 11222 more abundant, which is beneficial to improving the fast charging capability of the battery cell 10 and reducing the expansion of the negative electrode film 1122 during the charging process.

在一些实施例中,第一负极活性材料包括石墨颗粒,第一负极膜层11221中石墨颗粒的体积平均粒径Dv50为7.8μm至14.3μm,可选为7.8μm至11.3μm。可选地,第一负极活性材料包括人造石墨。In some embodiments, the first negative electrode active material comprises graphite particles, wherein the volume average particle size Dv50 of the graphite particles in the first negative electrode film layer 11221 is 7.8 μm to 14.3 μm, optionally 7.8 μm to 11.3 μm. Optionally, the first negative electrode active material comprises artificial graphite.

第二负极活性材料包括石墨颗粒,石墨颗粒的体积平均粒径Dv50为9.5μm至18.5μm,可选为9.5μm至14.6μm。可选地,第二负极活性材料包括天然石墨。The second negative electrode active material includes graphite particles with a volume average particle size Dv50 of 9.5 μm to 18.5 μm, optionally from 9.5 μm to 14.6 μm. Optionally, the second negative electrode active material includes natural graphite.

在一些实施例中,负极活性材料的比表面积为0.5m2/g-3m2/g,可选为0.6m2/g-1.2m2/g。示例性地,负极活性材料的比表面积为0.5m2/g、0.6m2/g、0.7m2/g、0.8m2/g、0.9m2/g、1.0m2/g、1.1m2/g、1.2m2/g、1.3m2/g、1.4m2/g、1.5m2/g、1.6m2/g、1.7m2/g、1.8m2/g、1.9m2/g、2.0m2/g、2.1m2/g、2.2m2/g、2.3m2/g、2.4m2/g、2.5m2/g、2.6m2/g、2.7m2/g、2.8m2/g、2.9m2/g、3.0m2/g或是上述任意两个数值组成的范围。In some embodiments, the specific surface area of the negative electrode active material is 0.5 /g to 3 /g, and optionally 0.6 /g to 1.2 m² /g. For example, the specific surface area of the negative electrode active material is 0.5 m²/ g, 0.6 m² /g, 0.7 m²/g, 0.8 /g, 0.9 /g, 1.0 /g, 1.1 /g, 1.2 /g, 1.3 m² /g, 1.4 m² /g, 1.5 m² / g, 1.6 /g, 1.7 /g , 1.8 /g, 1.9 /g, 2.0 m²/g, 2.1 /g, 2.2 /g, 2.3 m²/g, 2.4 /g, 2.5 m²/g, 2.6 m²/g, 2.7 /g , 2.8 /g, 2.9 m²/g, and 3.0 /g . /g or a range consisting of any two of the above values.

材料的比表面积为本领域公知的含义,可以采用本领域公知的设备和方法进行检测,例如,依据测试标准GB/T 19587-2017进行检测,将负极活性材料作为样品,通过美国Micromeritics公司的Tri-Star 3020型比表面积孔径分析测试仪测试比表面积。The specific surface area of a material is a well-known concept in the art and can be tested using equipment and methods known in the art. For example, it can be tested according to the testing standard GB/T 19587-2017, using the negative electrode active material as a sample and testing the specific surface area using a Tri-Star 3020 specific surface area and pore size analyzer from Micromeritics, Inc.

本申请实施例将负极活性材料的比表面积限定为大于或等于0.5m2/g,可以提升电池单体10快速充电的能力;将负极活性材料的比表面积限定为小于或等于3m2/g,可减少电池单体10在存储过程中的副反应,减缓负极片的膨胀,减小膨胀压强。In this embodiment, the specific surface area of the negative electrode active material is limited to greater than or equal to 0.5 /g, which can improve the fast charging capability of the battery cell 10; the specific surface area of the negative electrode active material is limited to less than or equal to 3 /g, which can reduce the side reactions of the battery cell 10 during storage, slow down the expansion of the negative electrode sheet, and reduce the expansion pressure.

在一些实施例中,正极膜层1112于电池单体100%SOC下的压实密度为2.50g/cm3至2.80g/cm3;可选为2.55g/cm3-2.70g/cm3。示例性地,电池单体10于100%荷电状态SOC下,正极膜层1112的压实密度为2.50g/cm3、2.52g/cm3、2.55g/cm3、2.56g/cm3、2.57g/cm3、2.58g/cm3、2.60g/cm3、2.62g/cm3、2.65g/cm3、2.68g/cm3、2.30g/cm3、2.32g/cm3、2.75g/cm3、2.78g/cm3、2.80g/cm3或是上述任意两个数值组成的范围。In some embodiments, the compaction density of the positive electrode film layer 1112 at 100% SOC of the battery cell is 2.50 g/ cm³ to 2.80 g/ cm³ ; optionally, it is 2.55 g/ cm³ to 2.70 g/ cm³ . For example, when the battery cell 10 is at 100% state of charge (SOC), the compaction density of the positive electrode film layer 1112 is 2.50 g/ cm³ , 2.52 g/ cm³ , 2.55 g/ cm³ , 2.56 g/ cm³ , 2.57 g/ cm³ , 2.58 g/ cm³ , 2.60 g/ cm³ , 2.62 g/ cm³ , 2.65 g/ cm³ , 2.68 g/cm³, 2.30 g/ cm³ , 2.32 g/ cm³ , 2.75 g/ cm³ , 2.78 g/ cm³ , 2.80 g/ cm³ , or any two of the above values.

正极膜层1112的压实密度在上述范围时,有利于提升电池单体10的能量密度;且由于正极膜层1112中的正极活性材料堆积较为紧密,颗粒与颗粒间接触电阻较小,能够进一步降低正极片111的电阻,从而降低快速充电下的产热。When the compaction density of the positive electrode film layer 1112 is within the above range, it is beneficial to improve the energy density of the battery cell 10; and since the positive electrode active material in the positive electrode film layer 1112 is packed more tightly and the contact resistance between particles is smaller, it can further reduce the resistance of the positive electrode sheet 111, thereby reducing the heat generation under fast charging.

在本申请实施方式中,正极膜层1112于电池单体100%SOC下的压实密度为本领域公知的含义,也即对100%SOC下的电池单体10拆解出正极片111,测定正极膜层1112的压实密度。示例性地,正极膜层1112的压实密度的测试方法可与负极膜层1122的压实密度的测试方法相同。In this embodiment, the compaction density of the positive electrode film 1112 at 100% SOC of the battery cell is a term known in the art, meaning that the positive electrode sheet 111 is separated from the battery cell 10 at 100% SOC, and the compaction density of the positive electrode film 1112 is measured. Exemplarily, the method for testing the compaction density of the positive electrode film 1112 can be the same as the method for testing the compaction density of the negative electrode film 1122.

在一些实施例中,正极膜层1112的单面涂布重量为200mg/1540mm2-370mg/1540/mm2;可选为240mg/1540mm2至330mg/1540mm2。示例性地,正极膜层1112的单面涂布重量为200mg/1540.25mm2、210mg/1540.25mm2、220mg/1540.25mm2、230mg/1540.25mm2、240mg/1540.25mm2、250mg/1540.25mm2、260mg/1540.25mm2、270mg/1540.25mm2、280mg/1540.25mm2、290mg/1540.25mm2、300mg/1540.25mm2、 310mg/1540.25mm2、320mg/1540.25mm2、330mg/1540.25mm2、340mg/1540.25mm2、350mg/1540.25mm2、360mg/1540.25mm2、370mg/1540.25mm2或是上述任意两个数值组成的范围。In some embodiments, the coating weight of the positive electrode film 1112 on one side is 200mg/1540mm² - 370mg/ 1540mm² ; optionally, it is 240mg/1540mm² to 330mg/ 1540mm² . For example, the single-sided coating weight of the positive electrode film layer 1112 is 200mg/1540.25mm², 210mg / 1540.25mm² , 220mg /1540.25mm², 230mg/1540.25mm² , 240mg /1540.25mm² , 250mg/1540.25mm², 260mg/1540.25mm², 270mg / 1540.25mm², 280mg /1540.25mm², 290mg/1540.25mm², or 300mg /1540.25mm². 310mg/1540.25mm², 320mg /1540.25mm² , 330mg/1540.25mm² , 340mg/1540.25mm² , 350mg/1540.25mm² , 360mg/1540.25mm² , 370mg/1540.25mm² , or a range consisting of any two of the above values.

在本申请实施方式中,正极膜层1112的单面涂布重量为本领域公知的含义,可以采用本领域公知的设备和方法进行检测,其检测方法如前文负极膜层1122的单面涂布重量测试方法。In the embodiments of this application, the single-sided coating weight of the positive electrode film layer 1112 has a meaning known in the art and can be detected using equipment and methods known in the art, such as the single-sided coating weight test method of the negative electrode film layer 1122 described above.

将正极膜层1112的单面涂布重量设置在200mg/1540mm2-370mg/1540/mm2,可限制正极片111单位面积内的产热量,且能够兼顾提升电池单体10的能量密度和充电倍率性能。Setting the single-sided coating weight of the positive electrode film 1112 to 200mg/1540mm² - 370mg/ 1540mm² can limit the heat generation per unit area of the positive electrode sheet 111, while also improving the energy density and charging rate performance of the battery cell 10.

在一些实施例中,正极片111的孔隙率为25%-32%。作为示例,正极片111的孔隙率可为25%、26%、27%、28%、29%、30%、31%、32%或是上述任意两个数值组成的范围。In some embodiments, the porosity of the positive electrode 111 is 25%-32%. As an example, the porosity of the positive electrode 111 may be 25%, 26%, 27%, 28%, 29%, 30%, 31%, 32%, or any combination of two of the above values.

在本申请实施方式中,正极片111的孔隙率为本领域公知的含义,可以采用本领域公知的设备和方法进行检测,其检测方法如负极片112的孔隙率测试方法。In the embodiments of this application, the porosity of the positive electrode 111 has a meaning known in the art and can be detected using equipment and methods known in the art, such as the porosity testing method for the negative electrode 112.

正极片111的孔隙率大于或等于25%,可为正极片111因发生副反应所产生的杂质提供空间,减小电池单体的膨胀压强,降低电池单体10的变形,改善电池单体10的循环性能,降低电池单体与汇流部件连接失效的风险。正极片111的孔隙率小于或等于32%,可在一定程度上兼顾电池单体10的能量密度。The porosity of the positive electrode 111 is greater than or equal to 25%, which provides space for impurities generated by side reactions in the positive electrode 111, reduces the expansion pressure of the battery cell 10, reduces the deformation of the battery cell 10, improves the cycle performance of the battery cell 10, and reduces the risk of connection failure between the battery cell and the busbar component. The porosity of the positive electrode 111 is less than or equal to 32%, which can, to some extent, maintain the energy density of the battery cell 10.

在一些实施例中,正极片111的厚度可为0.13mm-0.2mm。作为示例,正极片111的厚度可为0.13mm、0.14mm、0.15mm、0.16mm、0.17mm、0.18mm、0.19mm、0.2mm或是上述任意两个数值组成的范围。In some embodiments, the thickness of the positive electrode 111 may be 0.13mm-0.2mm. As an example, the thickness of the positive electrode 111 may be 0.13mm, 0.14mm, 0.15mm, 0.16mm, 0.17mm, 0.18mm, 0.19mm, 0.2mm or any range of two of the above values.

在本申请实施方式中,正极片111的厚度为本领域公知的含义,可以采用本领域公知的设备和方法进行检测,例如,采用万分尺测量正极片111的厚度。In the embodiments of this application, the thickness of the positive electrode 111 has a meaning known in the art and can be detected using equipment and methods known in the art, such as measuring the thickness of the positive electrode 111 using a micrometer.

采用具有较小厚度的正极片111,可以缩短离子迁移路径,提升离子迁移速率,减少电池单体10的产热,提升电池单体10的快速充电性能。By using a positive electrode 111 with a smaller thickness, the ion migration path can be shortened, the ion migration rate can be increased, the heat generation of the battery cell 10 can be reduced, and the fast charging performance of the battery cell 10 can be improved.

在一些实施例中,正极集流体1111的厚度与正极膜层1112的厚度之比为0.05至0.3。示例性地,在本申请实施例中,正极膜层1112的厚度为位于正极集流体1111一侧的正极膜层1112的厚度。In some embodiments, the ratio of the thickness of the positive current collector 1111 to the thickness of the positive electrode film 1112 is 0.05 to 0.3. Exemplarily, in an embodiment of this application, the thickness of the positive electrode film 1112 is the thickness of the positive electrode film 1112 located on one side of the positive current collector 1111.

示例性地,正极集流体1111的厚度与正极膜层1112的厚度的比值为0.05、0.06、0.07、0.08、0.09、0.1、0.12、0.15、0.18、0.2、0.22、0.25、0.28、0.3或是上述任意两个数值组成的范围。For example, the ratio of the thickness of the positive current collector 1111 to the thickness of the positive electrode film layer 1112 is 0.05, 0.06, 0.07, 0.08, 0.09, 0.1, 0.12, 0.15, 0.18, 0.2, 0.22, 0.25, 0.28, 0.3 or any two of the above values.

将正极集流体1111的厚度与正极膜层1112的厚度之比限定为大于或等于0.05,可以提升正极集流体1111的过流能力,减少正极片111的温升,提升电池单体10的快速充电性能;将正极集流体1111的厚度与正极膜层1112的厚度之比限定为小于或等于0.3,可降低正极片111的容量的损失。本申请实施例将正极集流体1111的厚度与正极膜层1112的厚度之比限定在0.05至0.3,可以在一定程度上兼顾电池单体10的快速充电能力和能量密度。Limiting the ratio of the thickness of the positive current collector 1111 to the thickness of the positive electrode film 1112 to greater than or equal to 0.05 can improve the current-carrying capacity of the positive current collector 1111, reduce the temperature rise of the positive electrode sheet 111, and improve the fast-charging performance of the battery cell 10. Limiting the ratio of the thickness of the positive current collector 1111 to the thickness of the positive electrode film 1112 to less than or equal to 0.3 can reduce the capacity loss of the positive electrode sheet 111. In this embodiment, the ratio of the thickness of the positive current collector 1111 to the thickness of the positive electrode film 1112 is limited to 0.05 to 0.3, which can, to a certain extent, balance the fast-charging capability and energy density of the battery cell 10.

正极膜层的厚度和正极集流体的厚度为本领域公知的含义,可以采用本领域公知 的设备和方法进行检测,例如,采用万分尺测量正极片的厚度,除去正极集流体表面的膜层,用万分尺测量正极集流体的厚度,在正极膜层为单侧涂布时,正极膜层的厚度为正极片的厚度减去正极集流体的厚度;在正极膜层为双侧涂布时,正极膜层的厚度为:(正极片的厚度减去正极集流体的厚度)/2。The thickness of the positive electrode film and the thickness of the positive electrode current collector have meanings known in the art and can be adopted using methods known in the art. The equipment and methods are used for testing. For example, the thickness of the positive electrode sheet is measured with a micrometer, the film layer on the surface of the positive electrode current collector is removed, and the thickness of the positive electrode current collector is measured with a micrometer. When the positive electrode film layer is coated on one side, the thickness of the positive electrode film layer is the thickness of the positive electrode sheet minus the thickness of the positive electrode current collector. When the positive electrode film layer is coated on both sides, the thickness of the positive electrode film layer is: (thickness of the positive electrode sheet minus the thickness of the positive electrode current collector)/2.

在一些实施例中,正极集流体1111的厚度为10μm至15μm,可选为12μm至15μm。示例性地,正极集流体1111的厚度为10μm、10.5μm、11μm、11.5μm、12μm、12.5μm、13μm、13.5μm、14μm、14.5μm、15μm或是上述任意两个数值组成的范围。正极集流体1111的厚度在上述范围时,正极集流体1111的过流能力较为优异,而且能够使得电池单体10具有较高的能量密度。In some embodiments, the thickness of the positive electrode current collector 1111 is 10 μm to 15 μm, optionally 12 μm to 15 μm. Exemplarily, the thickness of the positive electrode current collector 1111 is 10 μm, 10.5 μm, 11 μm, 11.5 μm, 12 μm, 12.5 μm, 13 μm, 13.5 μm, 14 μm, 14.5 μm, 15 μm, or any combination of two of the above values. When the thickness of the positive electrode current collector 1111 is within the above range, the current-carrying capacity of the positive electrode current collector 1111 is superior, and the battery cell 10 can have a higher energy density.

在一些实施例中,正极集流体1111的一部分未被正极膜层1112覆盖;正极集流体1111的未被正极膜层1112覆盖的部分可用于形成正极耳11b。In some embodiments, a portion of the positive current collector 1111 is not covered by the positive electrode film layer 1112; the portion of the positive current collector 1111 not covered by the positive electrode film layer 1112 can be used to form the positive electrode tab 11b.

在一些实施例中,正极活性材料包括橄榄石结构的含锂磷酸盐或其改性材料。In some embodiments, the positive electrode active material includes a lithium phosphate with an olivine structure or a modified version thereof.

橄榄石结构的含锂磷酸盐或其改性材料可以为橄榄石结构的含锂磷酸盐,或者对其进行包覆改性后得到的材料。例如,橄榄石结构的含锂磷酸盐包括磷酸盐颗粒和导离子层,导离子层包覆于磷酸盐颗粒表面,导离子层中含有C、Fe、Ti、Zr、Hf、Ge以及Sn中的一种或多种元素。The lithium-containing phosphate with an olivine structure or its modified material can be either an olivine-structured lithium-containing phosphate or a material obtained by coating and modifying it. For example, an olivine-structured lithium-containing phosphate includes phosphate particles and an ion-conducting layer, wherein the ion-conducting layer is coated on the surface of the phosphate particles and contains one or more elements selected from C, Fe, Ti, Zr, Hf, Ge, and Sn.

在一些实施例中,正极活性材料中橄榄石结构的含锂磷酸盐或其改性材料的质量占比可以大于或等于80%,小于或等于100%,可以认为本申请正极活性材料为橄榄石结构的含锂磷酸盐或其改性材料体系。在橄榄石结构的含锂磷酸盐或其改性材料的质量占比小于100%时,正极活性材料还可以包括常用的正极活性材料,例如可包括但不限于含锂过渡金属氧化物中的至少一种。含锂过渡金属氧化物的示例可包括但不限于锂钴氧化物、锂镍氧化物、锂锰氧化物、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、锂镍钴铝氧化物及其各自的改性化合物中的至少一种。In some embodiments, the mass percentage of olivine-structured lithium phosphate or its modified material in the positive electrode active material may be greater than or equal to 80% and less than or equal to 100%, and the positive electrode active material of this application can be considered as an olivine-structured lithium phosphate or its modified material system. When the mass percentage of olivine-structured lithium phosphate or its modified material is less than 100%, the positive electrode active material may also include commonly used positive electrode active materials, such as, but not limited to, at least one of lithium transition metal oxides. Examples of lithium transition metal oxides may include, but are not limited to, at least one of lithium cobalt oxide, lithium nickel oxide, lithium manganese oxide, lithium nickel cobalt oxide, lithium manganese cobalt oxide, lithium nickel manganese oxide, lithium nickel cobalt manganese oxide, lithium nickel cobalt aluminum oxide, and their respective modified compounds.

可选地,正极活性材料中橄榄石结构的含锂磷酸盐或其改性材料的质量占比为100%。Optionally, the positive electrode active material comprises 100% by mass of lithium phosphate with an olivine structure or its modified material.

在一些实施例中,正极活性材料的体积平均粒径满足1μm≤Dv50≤2μm,0.4μm≤Dv10≤0.7μm。In some embodiments, the volume average particle size of the positive electrode active material satisfies 1μm≤Dv50≤2μm and 0.4μm≤Dv10≤0.7μm.

示例性地,正极活性材料的Dv50可以为1μm、1.1μm、1.15μm、1.2μm、1.25μm、1.3μm、1.35μm、1.4μm、1.45μm、1.5μm、1.55μm、1.6μm、1.65μm、1.7μm、1.75μm、1.8μm、1.85μm、1.9μm、1.95μm、2μm或是上述任意两个数值组成的范围。For example, the Dv50 of the positive electrode active material can be 1 μm, 1.1 μm, 1.15 μm, 1.2 μm, 1.25 μm, 1.3 μm, 1.35 μm, 1.4 μm, 1.45 μm, 1.5 μm, 1.55 μm, 1.6 μm, 1.65 μm, 1.7 μm, 1.75 μm, 1.8 μm, 1.85 μm, 1.9 μm, 1.95 μm, 2 μm, or any range of two of the above values.

示例性地,正极活性材料的Dv10可以为0.4μm、0.45μm、0.5μm、0.55μm、0.6μm、0.65μm、0.7μm或是上述任意两个数值组成的范围。For example, the Dv10 of the positive electrode active material can be 0.4 μm, 0.45 μm, 0.5 μm, 0.55 μm, 0.6 μm, 0.65 μm, 0.7 μm, or any combination of two of the above values.

正极活性材料的粒径相对较小,锂离子在正极活性材料中的脱嵌锂路径较短,产热量较少;而且上述正极活性材料的粒径不会过小,可在加工制备过程中减少团聚,使得正极活性材料的性能稳定。The particle size of the positive electrode active material is relatively small, the lithium ion insertion and extraction path in the positive electrode active material is shorter, and the heat generation is less; moreover, the particle size of the above positive electrode active material is not too small, which can reduce agglomeration during the processing and preparation process, so as to make the performance of the positive electrode active material stable.

材料的体积平均粒度Dv50是指体积分布中50%所对应的粒度,材料的体积平均粒度Dv10是指体积分布中10%所对应的粒度,可以采用本领域公知的设备和方法进行检测,例如将正极活性材料作为样品,依据测试标准GB/T 19077-2016,通过Mastersizer  2000E型激光粒度分析仪测试颗粒的Dv50和Dv10等。The volume average particle size (Dv50) of a material refers to the particle size corresponding to 50% of its volume distribution, and the volume average particle size (Dv10) refers to the particle size corresponding to 10% of its volume distribution. Both can be detected using equipment and methods known in the art. For example, using the positive electrode active material as a sample, and according to the testing standard GB/T 19077-2016, the particle size can be measured using a Mastersizer. The 2000E laser particle size analyzer tests particle Dv50 and Dv10, etc.

在一些实施例中,电池单体10包括容纳于外壳12内的电解液。在电池单体10充放电过程中,活性离子在正极片111和负极片112之间往返嵌入和脱出,电解液在正极片111和负极片112之间起到传导活性离子的作用。In some embodiments, the battery cell 10 includes an electrolyte contained within the housing 12. During the charging and discharging process of the battery cell 10, active ions are inserted and extracted back and forth between the positive electrode 111 and the negative electrode 112, and the electrolyte plays a role in conducting active ions between the positive electrode 111 and the negative electrode 112.

在一些实施例中,电解液于室温下的电导率为13mS/cm至20mS/cm,可选为15mS/cm至20mS/cm。示例性地,电解液于室温下的电导率为13mS/cm、13.5mS/cm、14mS/cm、14.5mS/cm、15mS/cm、15.5mS/cm、16mS/cm、16.5mS/cm、17mS/cm、17.5mS/cm、18mS/cm、18.5mS/cm、19mS/cm、19.5mS/cm、20mS/cm或是上述任意两个数值组成的范围。In some embodiments, the conductivity of the electrolyte at room temperature is from 13 mS/cm to 20 mS/cm, optionally from 15 mS/cm to 20 mS/cm. Exemplarily, the conductivity of the electrolyte at room temperature is 13 mS/cm, 13.5 mS/cm, 14 mS/cm, 14.5 mS/cm, 15 mS/cm, 15.5 mS/cm, 16 mS/cm, 16.5 mS/cm, 17 mS/cm, 17.5 mS/cm, 18 mS/cm, 18.5 mS/cm, 19 mS/cm, 19.5 mS/cm, 20 mS/cm, or any range of two of the above values.

作为示例,室温可为25℃。As an example, the room temperature could be 25°C.

电解液的电导率在上述范围时,离子在该电解液中的迁移速率较高,从而进一步降低电池单体10的内阻,减少产热,并能够提升电池单体10的快速充电性能。When the conductivity of the electrolyte is within the above range, the migration rate of ions in the electrolyte is relatively high, thereby further reducing the internal resistance of the battery cell 10, reducing heat generation, and improving the fast charging performance of the battery cell 10.

电解液的电导率为离子电导率,可以采用本领域公知的设备和方法进行检测,例如参考行业标准HG-T 4067-2015进行测试。The conductivity of the electrolyte is the ionic conductivity, which can be detected using equipment and methods known in the art, such as by referring to industry standard HG-T 4067-2015.

在一些实施例中,电解液于室温下的密度ρ满足:1.05g/mL≤ρ≤1.35g/mL。In some embodiments, the density ρ of the electrolyte at room temperature satisfies: 1.05 g/mL ≤ ρ ≤ 1.35 g/mL.

示例性地,电解液的密度ρ为1.05g/mL、1.10g/mL、1.15g/mL、1.2g/mL、1.25g/mL、1.3g/mL、1.35g/mL或是上述任意两个数值组成的范围。For example, the density ρ of the electrolyte is 1.05 g/mL, 1.10 g/mL, 1.15 g/mL, 1.2 g/mL, 1.25 g/mL, 1.3 g/mL, 1.35 g/mL, or a range of any two of the above values.

电解液的密度ρ在上述范围时,锂离子在电解液中的迁移速率较高,能够进一步降低电池单体10的内阻,从而降低产热,并能够提升电池单体10的快速充电性能。When the electrolyte density ρ is within the above range, the migration rate of lithium ions in the electrolyte is relatively high, which can further reduce the internal resistance of the battery cell 10, thereby reducing heat generation and improving the fast charging performance of the battery cell 10.

在本申请实施方式中,电解液的密度为本领域公知的含义,可以采用本领域公知的设备和方法进行检测,例如参考GB/T 2013-2010进行测试。In the embodiments of this application, the density of the electrolyte has a meaning known in the art and can be detected using equipment and methods known in the art, such as referring to GB/T 2013-2010 for testing.

在一些实施例中,电解液包括有机溶剂,有机溶剂包括包括碳酸酯类溶剂和羧酸酯类溶剂中的一种或多种。In some embodiments, the electrolyte comprises an organic solvent, which includes one or more of carbonate solvents and carboxylic acid ester solvents.

在一些实施例中,羧酸酯类溶剂包括链状羧酸酯类溶剂,链状羧酸酯类溶剂在有机溶剂的质量含量为5%至75%。示例性地,链状羧酸酯类溶剂的质量含量为10%、15%、20%、25%、30%、35%、40%、45%、50%、55%、60%、65%、70%、75%或是上述任意两个数值组成的范围。链状羧酸酯类溶剂的质量含量在上述范围时,使得电解液体系的粘度相对较小,有利于锂离子的迁移。In some embodiments, the carboxylic acid ester solvent includes a chain-like carboxylic acid ester solvent, wherein the chain-like carboxylic acid ester solvent comprises 5% to 75% by mass of the organic solvent. Exemplarily, the mass content of the chain-like carboxylic acid ester solvent is 10%, 15%, 20%, 25%, 30%, 35%, 40%, 45%, 50%, 55%, 60%, 65%, 70%, 75%, or a range consisting of any two of the above values. When the mass content of the chain-like carboxylic acid ester solvent is within the above range, the viscosity of the electrolyte system is relatively low, which is beneficial for lithium ion migration.

在一些实施例中,链状羧酸酯类溶剂在有机溶剂的质量含量为30%至70%。In some embodiments, the chain carboxylic acid ester solvent has a mass content of 30% to 70% in the organic solvent.

在一些实施例中,羧酸酯包括R1-COO-R2,R1和R2分别独立地包括碳原子数为1-5的烷基或碳原子数为1-5的卤代烷基。上述链状羧酸酯类溶剂的电导率较高,有利于提升电池单体10的快速充电能力。In some embodiments, the carboxylic acid ester comprises R1 -COO- R2 , where R1 and R2 each independently comprise an alkyl group having 1-5 carbon atoms or a haloalkyl group having 1-5 carbon atoms. The aforementioned chain-like carboxylic acid ester solvents have high conductivity, which is beneficial for improving the fast-charging capability of the battery cell 10.

在一些实施例中,碳酸酯类溶剂包括碳酸乙烯酯、碳酸丙烯酯、碳酸二甲酯、碳酸二乙酯和碳酸甲乙酯中的一种或多种。In some embodiments, carbonate solvents include one or more of ethylene carbonate, propylene carbonate, dimethyl carbonate, diethyl carbonate, and ethyl methyl carbonate.

进一步可选地,碳酸酯类溶剂包括碳酸乙烯酯、碳酸二甲酯、碳酸甲乙酯中的一种或多种。Further optionally, the carbonate solvent includes one or more of ethylene carbonate, dimethyl carbonate, and ethyl methyl carbonate.

上述碳酸酯类溶剂和链状羧酸酯类溶剂配合使用,使得电解液的电导率得到提高,有利于锂离子的迁移。 The combined use of the aforementioned carbonate solvents and chain carboxylic acid ester solvents improves the conductivity of the electrolyte, which is beneficial for lithium ion migration.

进一步可选地,碳酸酯类溶剂在有机溶剂中的质量含量为5%至95%,可选为25%至60%,可选为30%至45%。示例性地,碳酸酯类溶剂在有机溶剂中的质量含量为25%、26%、27%、28%、29%、30%、31%、32%、33%、34%、35%、36%、37%、38%、40%、45%、48%、50%、55%、60%或是上述任意两个数值组成的范围。上述质量含量的碳酸酯类溶剂,能够进一步提高电解液的电导率得到提高,有利于锂离子的迁移。Further optionally, the carbonate solvent in the organic solvent has a mass content of 5% to 95%, optionally 25% to 60%, and optionally 30% to 45%. Exemplarily, the mass content of the carbonate solvent in the organic solvent is 25%, 26%, 27%, 28%, 29%, 30%, 31%, 32%, 33%, 34%, 35%, 36%, 37%, 38%, 40%, 45%, 48%, 50%, 55%, 60%, or any combination of two of the above values. The carbonate solvent at the above mass contents can further improve the conductivity of the electrolyte, which is beneficial for lithium ion migration.

示例性地,碳酸酯类溶剂包括碳酸乙烯酯、碳酸二甲酯、碳酸甲乙酯中的一种或多种,碳酸酯类溶剂的质量含量为25%至60%。For example, the carbonate solvent includes one or more of ethylene carbonate, dimethyl carbonate, and ethyl methyl carbonate, and the carbonate solvent content is 25% to 60% by mass.

有机溶剂搭配可提高电解液电导率、降低粘度,从而提高电池2快速充电性能。The use of organic solvents can improve the conductivity of the electrolyte and reduce its viscosity, thereby improving the fast charging performance of the battery.

在一些实施例中,电解液包括锂盐。锂盐包括含氟磺酰亚胺盐和六氟磷酸锂LiPF6中的一种或多种。上述锂盐易于解离,有利于锂离子的快速迁移;且电解液体系相对稳定,不易分解,能够提升电池单体10的循环性能。In some embodiments, the electrolyte comprises a lithium salt. The lithium salt includes one or more of fluorosulfonyl imide salts and lithium hexafluorophosphate (LiPF6). The above-mentioned lithium salts are readily dissociated, which is beneficial for the rapid migration of lithium ions; and the electrolyte system is relatively stable and not easily decomposed, which can improve the cycle performance of the battery cell 10.

可选地,含氟磺酰亚胺盐包括双氟磺酰亚胺锂LiFSI、双三氟甲基磺酸亚酰胺锂LiTFSI中一种或多种。Optionally, the fluorosulfonyl imide salt includes one or more of lithium bisfluorosulfonyl imide (LiFSI) and lithium bistrifluoromethanesulfonate (LiTFSI).

在一些实施例中,锂盐包括双氟磺酰亚胺锂LiFSI和六氟磷酸锂LiPF6,双氟磺酰亚胺锂LiFSI的摩尔浓度为0.2mol/L至0.5mol/L,六氟磷酸锂LiPF6的摩尔浓度为0.5mol/L至1.0mol/L。示例性地,双氟磺酰亚胺锂LiFSI的摩尔浓度为0.4mol/L至0.5mol/L,六氟磷酸锂LiPF6的摩尔浓度为0.7mol/L。示例性地,双氟磺酰亚胺锂LiFSI的摩尔浓度为0.5mol/L,六氟磷酸锂LiPF6的摩尔浓度为0.5mol/L。示例性地,双氟磺酰亚胺锂LiFSI的摩尔浓度为0.2mol/L,六氟磷酸锂LiPF6的摩尔浓度为0.8mol/L。In some embodiments, the lithium salt comprises lithium bis(fluorosulfonyl)imide (LiFSI) and lithium hexafluorophosphate (LiPF6 ) , wherein the molar concentration of lithium bis(fluorosulfonyl)imide (LiFSI) is 0.2 mol/L to 0.5 mol/L, and the molar concentration of lithium hexafluorophosphate (LiPF6 ) is 0.5 mol/L to 1.0 mol/L. Exemplarily, the molar concentration of lithium bis(fluorosulfonyl)imide (LiFSI) is 0.4 mol/L to 0.5 mol/L, and the molar concentration of lithium hexafluorophosphate (LiPF6 ) is 0.7 mol/L. Exemplarily, the molar concentration of lithium bis(fluorosulfonyl)imide (LiFSI) is 0.5 mol/L, and the molar concentration of lithium hexafluorophosphate (LiPF6 ) is 0.5 mol/L. Exemplarily, the molar concentration of lithium bis(fluorosulfonyl)imide (LiFSI) is 0.2 mol/L, and the molar concentration of lithium hexafluorophosphate (LiPF6 ) is 0.8 mol/L.

可选地,双氟磺酰亚胺锂的摩尔浓度和六氟磷酸锂LiPF6中的摩尔浓度的比值为(2至5):10。示例性地,双氟磺酰亚胺锂的摩尔浓度和六氟磷酸锂LiPF6中的摩尔浓度的比值为2:10、2.5:10、3:10、3.5:10、4:10、4.5:10、5:10或是上述任意两个数值组成的范围。Optionally, the molar concentration ratio of lithium bis(fluorosulfonyl)imide to lithium hexafluorophosphate ( LiPF6 ) is (2 to 5):10. Exemplarily, the molar concentration ratio of lithium bis(fluorosulfonyl)imide to lithium hexafluorophosphate (LiPF6 ) is 2:10, 2.5:10, 3:10, 3.5:10, 4:10, 4.5:10, 5:10, or a range of any two of the above values.

在一些实施例中,电极组件11沿厚度方向X上的尺寸为T,单层负极片112的厚度为T1,负极片112在厚度方向X上层叠的层数为N。T、T1以及N满足:0.3≤(N×T1)/T≤0.5。In some embodiments, the electrode assembly 11 has a dimension of T along the thickness direction X, the thickness of the single-layer negative electrode 112 is T1, and the number of layers of the negative electrode 112 stacked in the thickness direction X is N. T, T1, and N satisfy: 0.3≤(N×T1)/T≤0.5.

负极片112至少一个包括垂直于厚度方向X的平直层112a,在电极组件11中,平直层112a的层数即为N。The negative electrode 112 includes at least one flat layer 112a perpendicular to the thickness direction X. In the electrode assembly 11, the number of flat layers 112a is N.

示例性地,将电池单体10于0%荷电状态下拆解,并取出电极组件11;采用万分尺测量T和T1。For example, the battery cell 10 is disassembled at 0% charge and the electrode assembly 11 is removed; T and T1 are measured using a micrometer.

示例性地,电极组件11为卷绕结构,负极片112包括N个平直层112a;可替代地,电极组件11为叠片结构,电极组件11包括N个负极片112,各负极片112包括一个平直层112a。For example, the electrode assembly 11 is a wound structure, and the negative electrode 112 includes N flat layers 112a; alternatively, the electrode assembly 11 is a stacked structure, and the electrode assembly 11 includes N negative electrode 112, each negative electrode 112 including a flat layer 112a.

在电池单体10的循环过程中,负极片112由于不可逆的副反应会出现厚度增大,从而使电池单体10膨胀;将(N×T1)/T限定在0.3-0.5,可以减小的电池单体10的膨胀,降低电池单体10与汇流部件30连接失效的风险。During the cycling process of the battery cell 10, the negative electrode 112 will increase in thickness due to irreversible side reactions, thereby causing the battery cell 10 to expand. Limiting (N×T1)/T to 0.3-0.5 can reduce the expansion of the battery cell 10 and reduce the risk of connection failure between the battery cell 10 and the busbar component 30.

在一些实施例中,限位梁21为一体成型结构,这样可以减少限位梁21的连接薄弱 点,有利于提高限位梁21的结构强度和刚度。可替代地,限位梁21也可以由多个部件拼接而成,例如,限位梁21由多个钣金件拼焊而成。In some embodiments, the limiting beam 21 is a one-piece molded structure, which can reduce the weak connection of the limiting beam 21. This design improves the structural strength and stiffness of the limiting beam 21. Alternatively, the limiting beam 21 can be assembled from multiple components, for example, by welding together multiple sheet metal parts.

在一些实施例中,限位梁21为型材梁。In some embodiments, the limiting beam 21 is a profile beam.

限位梁21可以为板体或者杆材通过冲压/挤压或者金属铸造等工艺一体成型的空心梁结构。限位梁21的壁厚可根据实际需要采用1mm-8mm,通常以3mm-5mm较为常见,在此壁厚上,限位梁21具有较好的性价比,既能有较轻的质量,又具有不错的结构强度,可有效的抑制电池单体10在循环过程中产生的膨胀变形。The limiting beam 21 can be a hollow beam structure integrally formed from a plate or rod through processes such as stamping/extrusion or metal casting. The wall thickness of the limiting beam 21 can be 1mm-8mm depending on actual needs, with 3mm-5mm being the most common. At this wall thickness, the limiting beam 21 has a good cost-performance ratio, achieving both light weight and good structural strength, effectively suppressing the expansion and deformation of the battery cell 10 during cycling.

限位梁21可以但不局限于采用钢、铁、铝及铝合金等材料制成。The limiting beam 21 may be made of materials such as steel, iron, aluminum and aluminum alloys, but is not limited to steel.

在一些实施例中,箱体20包括框体22和支撑梁23,框体22限定出容纳空间,限位梁21和多个电池单体10设置于容纳空间。支撑梁23设置于限位梁21背离多个电池单体10的一侧并连接框体22和限位梁21。In some embodiments, the housing 20 includes a frame 22 and a support beam 23. The frame 22 defines an accommodating space, and a limiting beam 21 and a plurality of battery cells 10 are disposed in the accommodating space. The support beam 23 is disposed on the side of the limiting beam 21 opposite to the plurality of battery cells 10 and connects the frame 22 and the limiting beam 21.

可选地,框体22可为矩形框体。Optionally, the frame 22 can be a rectangular frame.

支撑梁23可以为一个,也可以为多个。There can be one or more support beams 23.

对于相邻的两个限位梁21,可以是一个限位梁21连接于支撑梁23,也可以两个限位梁21均连接有支撑梁23。For two adjacent limiting beams 21, one limiting beam 21 can be connected to the support beam 23, or both limiting beams 21 can be connected to the support beam 23.

在电池2的循环过程中,限位梁21用于抵抗电池单体10在循环过程中的膨胀作用力,框体22可通过支撑梁23支撑限位梁21,从而为限位梁21提供有效地支撑,减小限位梁21的变形,进而向电池单体10提供约束,减小电池单体10的膨胀,提高电池单体10的循环寿命。During the cycle of battery 2, the limiting beam 21 is used to resist the expansion force of battery cell 10 during the cycle. The frame 22 can support the limiting beam 21 through the support beam 23, thereby providing effective support for the limiting beam 21, reducing the deformation of the limiting beam 21, and thus providing constraint to battery cell 10, reducing the expansion of battery cell 10, and improving the cycle life of battery cell 10.

通过设置连接框体22和限位梁21的支撑力,可以提高箱体20的整体结构强度和刚度,降低箱体20开裂的风险。By setting the supporting force between the connecting frame 22 and the limiting beam 21, the overall structural strength and rigidity of the box 20 can be improved, and the risk of cracking of the box 20 can be reduced.

在一些实施例中,框体22包括多个边梁,多个边梁依次设置并连接,从而形成环状框体22。In some embodiments, the frame 22 includes a plurality of side beams, which are arranged and connected in sequence to form an annular frame 22.

在一些实施例中,支撑梁23沿厚度方向X延伸。可选地,支撑梁23的垂直于厚度方向X上的截面可为矩形、梯形、椭圆形、圆形、L形或其它形状。In some embodiments, the support beam 23 extends along the thickness direction X. Optionally, the cross-section of the support beam 23 perpendicular to the thickness direction X may be rectangular, trapezoidal, elliptical, circular, L-shaped, or other shapes.

在一些实施例中,支撑梁23为板体或空心梁结构。支撑梁23可以由钢、铝或铝合金制成。In some embodiments, the support beam 23 is a plate or hollow beam structure. The support beam 23 may be made of steel, aluminum, or aluminum alloy.

在一些实施例中,支撑梁23与框体22可以采用焊接,螺栓连接或者卡接等方式固定连接。In some embodiments, the support beam 23 and the frame 22 can be fixedly connected by welding, bolting, or snap-fitting.

在一些实施例中,限位梁21沿与厚度方向X垂直的方向延伸。箱体20包括多个沿限位梁21的宽度方向Y间隔布置的支撑梁23。多个支撑梁23可以增大限位梁21受到的约束力,提高限位梁21不同区域受力的均匀性,减小限位梁21在电池单体10的循环过程中变形,改善电池2的循环性能。In some embodiments, the limiting beam 21 extends in a direction perpendicular to the thickness direction X. The housing 20 includes a plurality of support beams 23 spaced apart along the width direction Y of the limiting beam 21. The plurality of support beams 23 can increase the constraint force on the limiting beam 21, improve the uniformity of force on different areas of the limiting beam 21, reduce the deformation of the limiting beam 21 during the cycling process of the battery cell 10, and improve the cycle performance of the battery 2.

在一些实施例中,箱体20还包括承载板24,多个电池单体10和限位梁21位于承载板24的同一侧并固定于承载板24。示例性地,承载板24和多个电池单体10沿电池单体10的高度方向Z设置。In some embodiments, the housing 20 further includes a support plate 24, with a plurality of battery cells 10 and a limiting beam 21 located on the same side of the support plate 24 and fixed to the support plate 24. Exemplarily, the support plate 24 and the plurality of battery cells 10 are arranged along the height direction Z of the battery cells 10.

在一些实施例中,箱体20还包括盖板(未示出),盖板与承载板24沿高度方向Z相对设置并固定于框体22。电池单体和限位梁位于盖板和承载板之间。 In some embodiments, the housing 20 further includes a cover plate (not shown), which is disposed opposite to the support plate 24 along the height direction Z and fixed to the frame 22. The battery cell and the limiting beam are located between the cover plate and the support plate.

在一些示例中,承载板24位于电池单体的上侧,电池单体倒置;可替代地,在另一些示例中,承载板24位于电池单体的下侧,电池单体正置。In some examples, the support plate 24 is located on top of the battery cell, which is inverted; alternatively, in other examples, the support plate 24 is located on the bottom of the battery cell, which is upright.

图13为本申请另一些实施例提供的电池的俯视示意图;图14为图13在方框处的放大示意图;图15为图14中的第二汇流部件的结构示意图。Figure 13 is a top view of a battery provided in some other embodiments of this application; Figure 14 is an enlarged view of Figure 13 at the box; Figure 15 is a structural schematic diagram of the second busbar in Figure 14.

请参照图6以及图13-图15,在一些实施例中,电池2还包括至少一个第二汇流部件30b,第二汇流部件30b为单层结构并电连接至少两个电池单体10,第二汇流部件30b的厚度大于第一汇流层31的厚度,且第二汇流部件30b的厚度大于第二汇流层32的厚度。Referring to Figures 6 and 13-15, in some embodiments, the battery 2 further includes at least one second busbar component 30b. The second busbar component 30b has a single-layer structure and is electrically connected to at least two battery cells 10. The thickness of the second busbar component 30b is greater than the thickness of the first busbar layer 31, and the thickness of the second busbar component 30b is greater than the thickness of the second busbar layer 32.

示例性地。在多个汇流部件30中,一部分的汇流部件30为第一汇流部件30a,另一部分的汇流部件30为第二汇流部件30b。For example, among the plurality of bus components 30, a portion of the bus components 30 is a first bus component 30a, and another portion of the bus components 30 is a second bus component 30b.

在电池2中,不同位置的电池单体10的膨胀量可能会存在差异。对于膨胀量较小的电池单体10,可以采用具有单层结构的第二汇流部件30b;相较于第一汇流部件30a,第二汇流部件30b结构简单,易于制造,可节省成本。第二汇流部件30b的厚度大于第一汇流层31的厚度和第二汇流层32的厚度,其过流能力可满足要求。In battery 2, the expansion amount of battery cells 10 at different locations may vary. For battery cells 10 with smaller expansion amounts, a second busbar component 30b with a single-layer structure can be used; compared to the first busbar component 30a, the second busbar component 30b has a simpler structure, is easier to manufacture, and can save costs. The thickness of the second busbar component 30b is greater than the thickness of the first busbar layer 31 and the thickness of the second busbar layer 32, and its current carrying capacity meets the requirements.

在一些实施例中,第一汇流层31的厚度与第二汇流层32的厚度之和等于第二汇流部件30b的厚度。本申请实施例可减小第一汇流部件30a与第二汇流部件30b的过流能力的差异,改善电流一致性。In some embodiments, the sum of the thickness of the first busbar 31 and the thickness of the second busbar 32 is equal to the thickness of the second busbar component 30b. Embodiments of this application can reduce the difference in current-carrying capacity between the first busbar component 30a and the second busbar component 30b, thereby improving current consistency.

在一些实施例中,第二汇流部件30b连接沿厚度方向X排列的至少两个电池单体10。In some embodiments, the second busbar 30b connects at least two battery cells 10 arranged along the thickness direction X.

在一些实施例中,在多个电池单体10中,沿厚度方向X位于最外侧电池单体10连接于第一汇流部件30a。In some embodiments, among a plurality of battery cells 10, the outermost battery cell 10 along the thickness direction X is connected to the first busbar 30a.

在充电过程中,多个电池单体10的膨胀可能会在厚度方向X上叠加,这造成在厚度方向X上位于最外侧的电池单体10出现的位移较大;采用具有双层结构的第一汇流部件30a来连接最外侧电池单体10,可以降低第一汇流部件30a与电池单体10连接失效的风险。During charging, the expansion of multiple battery cells 10 may overlap in the thickness direction X, which causes a large displacement of the outermost battery cell 10 in the thickness direction X. Using a first busbar 30a with a double-layer structure to connect the outermost battery cell 10 can reduce the risk of connection failure between the first busbar 30a and the battery cell 10.

示例性地,沿厚度方向X位于最外侧电池单体10连接于第一汇流层31。For example, the outermost battery cell 10 along the thickness direction X is connected to the first busbar layer 31.

在一些实施例中,与限位梁21相邻的电池单体10可连接于第一汇流部件30a。In some embodiments, the battery cell 10 adjacent to the limiting beam 21 may be connected to the first busbar 30a.

在一些实施例中,多个汇流部件30还包括第三汇流部件30c,第三汇流部件30c可连接沿宽度方向Y相邻的两个电池单体10。In some embodiments, the plurality of busbar components 30 may further include a third busbar component 30c, which may connect two adjacent battery cells 10 along the width direction Y.

在一些实施例中,于25℃至35℃的外界环境中,电池单体10从10%SOC充电至80%SOC的充电时间为5分钟至10.5分钟。可选地,于25℃至35℃的外界环境中,电池单体10从10%SOC充电至80%SOC的充电时间可为5min至10.5min。示例性地,电池单体10从10%荷电状态至80%荷电状态的充电时间为10.5min、10min、9.5min、9min、8.5min、8min、7.5min、7min、6.5min、6min、5.5min、5min或是上述任意两个数值组成的范围。In some embodiments, in an external environment of 25°C to 35°C, the charging time for battery cell 10 from 10% SOC to 80% SOC is 5 minutes to 10.5 minutes. Optionally, in an external environment of 25°C to 35°C, the charging time for battery cell 10 from 10% SOC to 80% SOC may be 5 minutes to 10.5 minutes. Exemplarily, the charging time for battery cell 10 from 10% SOC to 80% SOC is 10.5 minutes, 10 minutes, 9.5 minutes, 9 minutes, 8.5 minutes, 8 minutes, 7.5 minutes, 7 minutes, 6.5 minutes, 6 minutes, 5.5 minutes, 5 minutes, or a range of any two of the above values.

本申请实施例的电池单体10具有快速充电能力,可节省充电时间。The battery cell 10 in this embodiment has fast charging capability, which can save charging time.

在一些实施例中,电池2或组成电池2的任意电池单体10从10%到80%的充电步骤可以按照如下方式进行: In some embodiments, the charging steps of the battery 2 or any of the battery cells 10 comprising the battery 2 from 10% to 80% can be performed as follows:

以5.0C恒流从10%SOC充电至15%SOC;Charge from 10% SOC to 15% SOC at a constant current of 5.0C;

以5.0C恒流从15%SOC充电至20%SOC;Charge from 15% SOC to 20% SOC at a constant current of 5.0C;

以5.0C恒流从20%SOC充电至25%SOC;Charge from 20% SOC to 25% SOC at a constant current of 5.0C;

以5.0C恒流从25%SOC充电至30%SOC;Charge from 25% SOC to 30% SOC at a constant current of 5.0C;

以5.0C恒流从30%SOC充电至35%SOC;Charge from 30% SOC to 35% SOC at a constant current of 5.0C;

以5.0C恒流从35%SOC充电至40%SOC;Charge from 35% SOC to 40% SOC at a constant current of 5.0C;

以4.6C恒流从40%SOC充电至45%SOC;Charge from 40% SOC to 45% SOC at a constant current of 4.6C;

以4.3C恒流从45%SOC充电至50%SOC;Charge from 45% SOC to 50% SOC at a constant current of 4.3C;

以4.0C恒流从50%SOC充电至55%SOC;Charge from 50% SOC to 55% SOC at a constant current of 4.0C;

以3.7C恒流从55%SOC充电至60%SOC;Charge from 55% SOC to 60% SOC at a constant current of 3.7C;

以3.4C恒流从60%SOC充电至65%SOC;Charge from 60% SOC to 65% SOC at a constant current of 3.4C;

以3.1C恒流从65%SOC充电至70%SOC;Charge from 65% SOC to 70% SOC at a constant current of 3.1C;

以2.9C恒流从70%SOC充电至75%SOC;Charge from 70% SOC to 75% SOC at a constant current of 2.9C;

以2.7C恒流从75%SOC充电至80%SOC。Charge from 75% SOC to 80% SOC at a constant current of 2.7C.

作为示例,上述充电策略在30℃的环境中进行。As an example, the above charging strategy is carried out in an environment of 30°C.

在一些实施例中,电池单体10从0%SOC到10%的SOC充电步骤可以按照如下方式进行:以5.0C恒流从0%SOC充电至10%SOC。In some embodiments, the charging step of the battery cell 10 from 0% SOC to 10% SOC can be performed as follows: charging from 0% SOC to 10% SOC at a constant current of 5.0C.

在一些实施例中,电池单体10从80%SOC到98%的SOC充电步骤可以按照如下方式进行:In some embodiments, the charging step of the battery cell 10 from 80% SOC to 98% SOC can be performed as follows:

以1.8C恒流从80%SOC充电至85%SOC;Charge from 80% SOC to 85% SOC at a constant current of 1.8C;

以1.3C恒流从85%SOC充电至90%SOC;Charge from 85% SOC to 90% SOC at a constant current of 1.3C;

以0.7C恒流从90%SOC充电至95%SOC;Charge from 90% SOC to 95% SOC at a constant current of 0.7C;

以0.33C恒流从95%SOC充电至98%SOC。Charge from 95% SOC to 98% SOC at a constant current of 0.33C.

在一些实施例中,电池单体10从98%SOC到100%的SOC充电步骤可以按照如下方式进行:以0.01C、0.05C、0.1C或0.3C恒流从98%SOC充电至100%SOC。可选地,电池单体10从98%SOC到100%的SOC充电步骤可以按照如下方式进行:以0.01C、0.05C或0.1C恒流从98%SOC充电至100%SOC。In some embodiments, the charging step of the battery cell 10 from 98% SOC to 100% SOC can be performed as follows: charging from 98% SOC to 100% SOC at a constant current of 0.01C, 0.05C, 0.1C, or 0.3C. Optionally, the charging step of the battery cell 10 from 98% SOC to 100% SOC can be performed as follows: charging from 98% SOC to 100% SOC at a constant current of 0.01C, 0.05C, or 0.1C.

在一些实施例中,电池单体10从10%SOC充电至80%的SOC的过程中,充电电流可为2C-6C,可选为2.7C-5C。电池单体10在充电过程中,充电电流可根据电池单体10的SOC变化。In some embodiments, during the charging process of battery cell 10 from 10% SOC to 80% SOC, the charging current can be 2C-6C, optionally 2.7C-5C. The charging current of battery cell 10 can vary according to the SOC of battery cell 10 during charging.

在一些实施例中,电池单体10为锂离子电池单体。在将电池单体10按照充电策略和放电策略循环20圈后,拆解电池单体10出的负极片,并观察和测量负极片的析锂面积。析锂区域的面积与负极片的总面积之比小于2%。In some embodiments, the battery cell 10 is a lithium-ion battery cell. After cycling the battery cell 10 20 times according to the charging and discharging strategies, the negative electrode sheet of the battery cell 10 is disassembled, and the lithium plating area of the negative electrode sheet is observed and measured. The ratio of the area of the lithium plating region to the total area of the negative electrode sheet is less than 2%.

作为示例,放电策略采用以0.33C恒电流放电至2.0V。As an example, the discharge strategy employs a constant current discharge of 0.33C to 2.0V.

作为示例,充电策略可为:As an example, a charging strategy could be:

以5.0C恒流从0%SOC充电至5%SOC;Charge from 0% SOC to 5% SOC at a constant current of 5.0C;

以5.0C恒流从5%SOC充电至10%SOC;Charge from 5% SOC to 10% SOC at a constant current of 5.0C;

以5.0C恒流从10%SOC充电至15%SOC; Charge from 10% SOC to 15% SOC at a constant current of 5.0C;

以5.0C恒流从15%SOC充电至20%SOC;Charge from 15% SOC to 20% SOC at a constant current of 5.0C;

以5.0C恒流从20%SOC充电至25%SOC;Charge from 20% SOC to 25% SOC at a constant current of 5.0C;

以5.0C恒流从25%SOC充电至30%SOC;Charge from 25% SOC to 30% SOC at a constant current of 5.0C;

以5.0C恒流从30%SOC充电至35%SOC;Charge from 30% SOC to 35% SOC at a constant current of 5.0C;

以5.0C恒流从35%SOC充电至40%SOC;Charge from 35% SOC to 40% SOC at a constant current of 5.0C;

以4.6C恒流从40%SOC充电至45%SOC;Charge from 40% SOC to 45% SOC at a constant current of 4.6C;

以4.3C恒流从45%SOC充电至50%SOC;Charge from 45% SOC to 50% SOC at a constant current of 4.3C;

以4.0C恒流从50%SOC充电至55%SOC;Charge from 50% SOC to 55% SOC at a constant current of 4.0C;

以3.7C恒流从55%SOC充电至60%SOC;Charge from 55% SOC to 60% SOC at a constant current of 3.7C;

以3.4C恒流从60%SOC充电至65%SOC;Charge from 60% SOC to 65% SOC at a constant current of 3.4C;

以3.1C恒流从65%SOC充电至70%SOC;Charge from 65% SOC to 70% SOC at a constant current of 3.1C;

以2.9C恒流从70%SOC充电至75%SOC;Charge from 70% SOC to 75% SOC at a constant current of 2.9C;

以2.7C恒流从75%SOC充电至80%SOC;Charge from 75% SOC to 80% SOC at a constant current of 2.7C;

以1.8C恒流从80%SOC充电至85%SOC;Charge from 80% SOC to 85% SOC at a constant current of 1.8C;

以1.3C恒流从85%SOC充电至90%SOC;Charge from 85% SOC to 90% SOC at a constant current of 1.3C;

以0.7C恒流从90%SOC充电至95%SOC;Charge from 90% SOC to 95% SOC at a constant current of 0.7C;

以0.33C恒流从95%SOC充电至98%SOC;Charge from 95% SOC to 98% SOC at a constant current of 0.33C;

以0.1C恒流从98%SOC充电至100%SOC。Charge from 98% SOC to 100% SOC at a constant current of 0.1C.

本申请实施例的电池单体10,能够在10.5分钟内从10%SOC充电至80%SOC,且不析锂或轻微析锂,具有较好的快速充电能力。示例性地,析锂区域的面积与负极片的总面积之比小于0.05%可认为不析锂,析锂区域的面积与负极片的总面积之比小于2%,且大于或等于0.05%,可认为是轻微析锂。The battery cell 10 of this embodiment can be charged from 10% SOC to 80% SOC in 10.5 minutes without lithium plating or with only slight lithium plating, demonstrating good fast charging capability. For example, a ratio of the area of the lithium plating region to the total area of the negative electrode sheet of less than 0.05% can be considered as no lithium plating, and a ratio of the area of the lithium plating region to the total area of the negative electrode sheet of less than 2% and greater than or equal to 0.05% can be considered as slight lithium plating.

根据本申请的一些实施例,本申请还提供了一种用电装置,包括以上任一实施例的电池2,电池2用于为用电装置提供电能。用电装置可以是前述任一应用电池2的设备或系统。According to some embodiments of this application, this application also provides an electrical device, including a battery 2 from any of the above embodiments, wherein the battery 2 is used to provide electrical energy to the electrical device. The electrical device can be any of the aforementioned devices or systems that utilize the battery 2.

参照图2至图12,本申请实施例提供了一种电池2,其包括多个电池单体10、箱体20和多个汇流部件30。多个电池单体10容纳于箱体20内。Referring to Figures 2 to 12, an embodiment of this application provides a battery 2, which includes a plurality of battery cells 10, a housing 20, and a plurality of busbar components 30. The plurality of battery cells 10 are housed within the housing 20.

电池单体10包括外壳12和容纳于外壳12内的电极组件11。电池单体在厚度方向X上的膨胀压强为0.5MPa-2.4MPa。The battery cell 10 includes a housing 12 and an electrode assembly 11 housed within the housing 12. The expansion pressure of the battery cell in the thickness direction X is 0.5 MPa-2.4 MPa.

电极组件11包括正极片111、负极片112和隔离膜113,隔离膜113将正极片111和负极片112隔开。可选地,正极片111、负极片112和隔离膜113卷绕设置。The electrode assembly 11 includes a positive electrode 111, a negative electrode 112, and a separator 113, which separates the positive electrode 111 and the negative electrode 112. Optionally, the positive electrode 111, the negative electrode 112, and the separator 113 are wound together.

负极片112包括负极集流体1121和设置于负极集流体1121至少一侧的负极膜层1122,负极膜层1122包括负极活性材料。负极片112的孔隙率为27%-40%。负极膜层1122于电池单体100%SOC下的压实密度为1.15g/cm3至1.36g/cm3The negative electrode 112 includes a negative electrode current collector 1121 and a negative electrode film layer 1122 disposed on at least one side of the negative electrode current collector 1121, the negative electrode film layer 1122 including a negative electrode active material. The porosity of the negative electrode 112 is 27%-40%. The compaction density of the negative electrode film layer 1122 at 100% SOC of the battery cell is 1.15 g/ cm³ to 1.36 g/ cm³ .

负极膜层1122包括第一负极膜层11221和第二负极膜层11222,第二负极膜层11222设置于第一负极膜层11221和负极集流体1121之间。负极活性材料包括设置于第一负极膜层11221的第一负极活性材料和设置于第二负极膜层11222的第二负极活性材料,第一负极活性材料包括人造石墨,第二负极活性材料包括人造石墨、天然石墨和 硅基材料的一种或多种。第一负极活性材料的体积平均粒径Dv50小于或等于第二负极活性材料的体积平均粒径Dv50。The negative electrode film layer 1122 includes a first negative electrode film layer 11221 and a second negative electrode film layer 11222, wherein the second negative electrode film layer 11222 is disposed between the first negative electrode film layer 11221 and the negative electrode current collector 1121. The negative electrode active material includes a first negative electrode active material disposed in the first negative electrode film layer 11221 and a second negative electrode active material disposed in the second negative electrode film layer 11222. The first negative electrode active material includes artificial graphite, and the second negative electrode active material includes artificial graphite, natural graphite, and... One or more silicon-based materials. The volume average particle size Dv50 of the first negative electrode active material is less than or equal to the volume average particle size Dv50 of the second negative electrode active material.

正极片111包括正极集流体1111和设置于正极集流体1111至少一侧的正极膜层1112。正极膜层1112于电池单体100%SOC下的压实密度为2.50g/cm3至2.80g/cm3。正极片111的孔隙率为25%-32%。正极集流体1111的厚度与正极膜层1112的厚度之比为0.05至0.3。正极活性材料包括橄榄石结构的含锂磷酸盐或其改性材料。正极活性材料的体积平均粒径满足1μm≤Dv50≤2μm,0.4μm≤Dv10≤0.7μm。The positive electrode 111 includes a positive current collector 1111 and a positive electrode film 1112 disposed on at least one side of the positive current collector 1111. The compaction density of the positive electrode film 1112 at 100% SOC of the battery cell is 2.50 g/ cm³ to 2.80 g/ cm³ . The porosity of the positive electrode 111 is 25%-32%. The ratio of the thickness of the positive current collector 1111 to the thickness of the positive electrode film 1112 is 0.05 to 0.3. The positive electrode active material includes a lithium phosphate with an olivine structure or a modified material thereof. The volume average particle size of the positive electrode active material satisfies 1 μm ≤ Dv50 ≤ 2 μm and 0.4 μm ≤ Dv10 ≤ 0.7 μm.

箱体20包括两个限位梁21,两个限位梁21沿电池单体10的厚度方向X间隔设置。多个电池单体10阵列排布并构成多个电池单体列100,多个电池单体列100沿限位梁21的宽度方向Y排列,各电池单体列100包括至少两个沿电池单体10的厚度方向X排列的电池单体10。多个电池单体10布置于两个限位梁21之间。The housing 20 includes two limiting beams 21, which are spaced apart along the thickness direction X of the battery cells 10. Multiple battery cells 10 are arranged in an array to form multiple battery cell rows 100, which are arranged along the width direction Y of the limiting beams 21. Each battery cell row 100 includes at least two battery cells 10 arranged along the thickness direction X of the battery cells 10. The multiple battery cells 10 are arranged between the two limiting beams 21.

箱体20包括框体22和支撑梁23,框体22限定出容纳空间,限位梁21和多个电池单体10设置于容纳空间。支撑梁23设置于限位梁21背离多个电池单体10的一侧并连接框体22和限位梁21。约束件40连接相邻的限位梁21并粘接于电池单体10。The housing 20 includes a frame 22 and a support beam 23. The frame 22 defines an accommodating space, and a limiting beam 21 and multiple battery cells 10 are disposed within the accommodating space. The support beam 23 is disposed on the side of the limiting beam 21 opposite to the multiple battery cells 10 and connects the frame 22 and the limiting beam 21. A constraint member 40 connects adjacent limiting beams 21 and is bonded to the battery cells 10.

多个汇流部件30将多个电池单体10电连接。多个汇流部件30包括至少一个第一汇流部件30a,第一汇流部件30a包括层叠并连接的第一汇流层31和第二汇流层32,第一汇流层31连接至少两个沿厚度方向X设置的电池单体10。Multiple busbars 30 electrically connect multiple battery cells 10. The multiple busbars 30 include at least one first busbar 30a, the first busbar 30a including a first busbar layer 31 and a second busbar layer 32 stacked and connected, the first busbar layer 31 connecting at least two battery cells 10 disposed along the thickness direction X.

实施例Example

下述实施例更具体地描述了本申请实施方式公开的内容,这些实施例仅仅用于阐述性说明,因为在本申请实施方式公开内容的范围内进行各种修改和变化对本领域技术人员来说是明显的。除非另有声明,以下实施例中所报道的所有份、百分比和比值都是基于质量计,而且实施例中使用的所有试剂都可商购获得或是按照常规方法进行合成获得,并且可直接使用而无需进一步处理,以及实施例中使用的仪器均可商购获得。The following embodiments describe the contents disclosed in this application in more detail. These embodiments are merely illustrative, as various modifications and variations will be apparent to those skilled in the art within the scope of the disclosure of the embodiments of this application. Unless otherwise stated, all parts, percentages, and ratios reported in the following embodiments are based on mass, and all reagents used in the embodiments are commercially available or synthesized by conventional methods and can be used directly without further processing, and the instruments used in the embodiments are commercially available.

实施例1Example 1

1、正极极片的制备1. Preparation of positive electrode sheet

正极极片包括正极集流体和设置于正极集流体两侧的正极膜层,正极集流体为厚度15μm铝箔。The positive electrode includes a positive current collector and a positive film layer disposed on both sides of the positive current collector. The positive current collector is an aluminum foil with a thickness of 15μm.

正极膜层包括由正极浆料(溶剂为N-甲基吡咯烷酮NMP)均匀涂覆于正极导电层的表面上,经干燥、冷压后形成的膜层,正极膜层包括重量比为97:2:1的正极活性材料、粘结剂聚偏二氟乙烯(PVDF)和导电剂乙炔黑。The positive electrode film layer comprises a film layer formed by uniformly coating a positive electrode slurry (solvent being N-methylpyrrolidone, NMP) onto the surface of a positive electrode conductive layer, followed by drying and cold pressing. The positive electrode film layer comprises positive electrode active material, binder polyvinylidene fluoride (PVDF), and conductive agent acetylene black in a weight ratio of 97:2:1.

正极活性材料包括磷酸铁锂和导离子层,导离子层包覆于磷酸铁锂表面,导离子层包括磷酸钛铁锂Li2FeTi(PO4)3和无定形碳。正极活性材料的Dv50为1.6μm,Dv10为0.64μm。The positive electrode active material includes lithium iron phosphate and an ion-conducting layer. The ion-conducting layer is coated on the surface of the lithium iron phosphate and consists of lithium titanium iron phosphate (Li₂FeTi( PO₄ ) ) and amorphous carbon. The Dv50 of the positive electrode active material is 1.6 μm, and the Dv10 is 0.64 μm.

正极膜层的单面涂布重量为0.21g/1540.25mm2,正极膜层在冷压后压实密度为2.6g/cm3The single-sided coating weight of the positive electrode film is 0.21g/ 1540.25mm² , and the compaction density of the positive electrode film after cold pressing is 2.6g/ cm³ .

2、负极极片的制备2. Preparation of negative electrode sheet

负极极片包括负极集流体和设置于负极集流体两侧的负极膜层,负极集流体为厚 度6μm的铜箔。The negative electrode includes a negative current collector and a negative electrode film layer disposed on both sides of the negative current collector. The negative current collector is thick. Copper foil with a thickness of 6μm.

负极膜层包括由负极浆料(溶剂为去离子水)均匀涂覆于负极导电层的表面上,经干燥、冷压后形成的膜层。The negative electrode film layer comprises a film layer formed by uniformly coating a negative electrode slurry (with deionized water as the solvent) onto the surface of a negative electrode conductive layer, followed by drying and cold pressing.

负极膜层的单面涂布重量为0.096g/1540.25mm2,负极膜层在冷压后压实密度为1.6g/cm3The single-sided coating weight of the negative electrode film is 0.096g/ 1540.25mm² , and the compaction density of the negative electrode film after cold pressing is 1.6g/ cm³ .

负极膜层包括第一负极膜层和第二负极膜层,第二负极膜层位于第一负极膜层和负极集流体之间。The negative electrode film layer includes a first negative electrode film layer and a second negative electrode film layer, with the second negative electrode film layer located between the first negative electrode film layer and the negative electrode current collector.

第二负极膜层包括质量比为96.5:0.5:0.5:1.5:1的石墨颗粒、导电剂乙炔黑、第二含锂粘结剂(丙烯酸锂-丙烯腈-丙烯酰胺-丙烯酸羟乙酯共聚物,其中丙烯酸锂单体、丙烯腈单体、丙烯酰胺单体和丙烯酸羟乙酯单体的摩尔比为35%:30%:15%:20%)、负极粘结剂丁苯橡胶、增稠剂羧甲基纤维素钠,第二含锂粘结剂中锂元素的质量含量为4.8%,石墨颗粒的Dv50为11.3μm,石墨颗粒包括人造石墨和碳包覆层,碳包覆层包覆于人造石墨表面,碳包覆层的质量含量为3.5%。The second negative electrode film layer comprises graphite particles in a mass ratio of 96.5:0.5:0.5:1.5:1, conductive agent acetylene black, a second lithium-containing binder (lithium acrylate-acrylonitrile-acrylamide-hydroxyethyl acrylate copolymer, wherein the molar ratio of lithium acrylate monomer, acrylonitrile monomer, acrylamide monomer and hydroxyethyl acrylate monomer is 35%:30%:15%:20%), negative electrode binder styrene-butadiene rubber, and thickener sodium carboxymethyl cellulose. The lithium content in the second lithium-containing binder is 4.8% by mass. The Dv50 of the graphite particles is 11.3 μm. The graphite particles include artificial graphite and a carbon coating layer. The carbon coating layer coats the surface of the artificial graphite, and the carbon coating layer has a mass content of 3.5%.

第一负极膜层包括质量比为97.5:0.5:0.5:0.5:1的石墨颗粒、导电剂乙炔黑、第一含锂粘结剂(丙烯酸锂-丙烯腈-丙烯酰胺-丙烯酸羟乙酯共聚物,其中丙烯酸锂单体、丙烯腈单体、丙烯酰胺单体和丙烯酸羟乙酯单体的摩尔比为35%:30%:15%:20%)、负极粘结剂丁苯橡胶、增稠剂羧甲基纤维素钠,第一含锂粘结剂中锂元素的质量含量为4.8%,石墨颗粒的Dv50为11.3μm,石墨颗粒包括人造石墨和碳包覆层,碳包覆层包覆于人造石墨表面,碳包覆层的质量含量为3.5%。The first negative electrode film layer comprises graphite particles in a mass ratio of 97.5:0.5:0.5:0.5:1, conductive agent acetylene black, a first lithium-containing binder (lithium acrylate-acrylonitrile-acrylamide-hydroxyethyl acrylate copolymer, wherein the molar ratio of lithium acrylate monomer, acrylonitrile monomer, acrylamide monomer and hydroxyethyl acrylate monomer is 35%:30%:15%:20%), negative electrode binder styrene-butadiene rubber, and thickener sodium carboxymethyl cellulose. The lithium content in the first lithium-containing binder is 4.8% by mass. The Dv50 of the graphite particles is 11.3 μm. The graphite particles include artificial graphite and a carbon coating layer. The carbon coating layer coats the surface of the artificial graphite, and the carbon coating layer has a mass content of 3.5%.

3、隔离膜3. Separating membrane

隔离膜包括基膜,基膜为7μm的聚乙烯膜层,孔隙率为42%。The separator includes a base membrane, which is a 7μm polyethylene film layer with a porosity of 42%.

4、电解液的制备4. Preparation of electrolyte

电解液包括有机溶剂、锂盐和添加剂。The electrolyte consists of organic solvents, lithium salts, and additives.

有机溶剂包括60%链状羧酸酯类溶剂(乙酸乙酯)和40%碳酸酯类溶剂(30%的碳酸乙烯酯EC,剩余为碳酸二甲酯),有机溶剂中各组分的质量含量基于有机溶剂的质量进行计算。The organic solvents consist of 60% chain carboxylic acid ester solvents (ethyl acetate) and 40% carbonate solvents (30% ethylene carbonate EC, the remainder being dimethyl carbonate). The mass content of each component in the organic solvents is calculated based on the mass of the organic solvents.

基于电解液的质量,添加剂的质量含量6.5%,其包括质量比为5:0.5:0.5:0.5的碳酸亚乙烯酯VC、氟代碳酸乙烯酯FEC、亚硫酸乙烯酯ES和二氟草酸硼酸锂LiDFOB。Based on the mass of the electrolyte, the additive content is 6.5%, which includes vinylene carbonate (VC), fluoroethylene carbonate (FEC), vinyl sulfite (ES), and lithium difluorooxalate borate (LiDFOB) in a mass ratio of 5:0.5:0.5:0.5.

锂盐包括1mol/L的六氟磷酸锂LiPF6The lithium salts include 1 mol/L lithium hexafluorophosphate (LiPF6 ) .

电解液于室温下的电导率为16.4mS/cm。The electrolyte has a conductivity of 16.4 mS/cm at room temperature.

5、电池单体的制备5. Preparation of battery cells

将上述正极极片、隔离膜、负极极片按顺序叠好,使隔离膜处于正极极片和负极极片之间起到隔离作用,得到电极组件,将电极组件置于外壳中,干燥后注入电解液,经过真空封装、静置、化成、整形等工序,得到电池单体。The positive electrode, separator, and negative electrode are stacked in sequence, with the separator positioned between the positive and negative electrodes to provide isolation, thus obtaining an electrode assembly. The electrode assembly is placed in a housing, dried, and then injected with electrolyte. After vacuum sealing, settling, formation, and shaping, a single battery cell is obtained.

6、电池的制备6. Battery manufacturing

将制备出的多个电池单体安装到箱体内,然后将多个汇流部件与多个电池单体的电极端子焊接,并安装高低压线束,以得到电池。Multiple battery cells are installed into a housing, and then multiple busbars are welded to the electrode terminals of the battery cells. High and low voltage wiring harnesses are then installed to obtain the battery.

其中,汇流部件可为图6所示的第一汇流部件,第一汇流部件具有双层结构第一汇 流部件的单层结构的厚度Th为1.5mm,即第一汇流层的厚度为1.5mm,第二汇流层的厚度为1.5mm。The busbar component can be the first busbar component shown in Figure 6, which has a double-layer structure. The thickness Th of the single-layer structure of the flow component is 1.5 mm, that is, the thickness of the first busbar layer is 1.5 mm and the thickness of the second busbar layer is 1.5 mm.

实施例2Example 2

采用与实施例1相似的方法制备电池单体和电池,与实施例1不同的是,正极膜层的单面涂布重量、正极膜层冷压后的压实密度、负极膜层的单面涂布重量、负极膜层冷压后的压实密度作了调整。Battery cells and batteries were prepared using a method similar to that in Example 1. The difference from Example 1 is that the single-sided coating weight of the positive electrode film, the compaction density of the positive electrode film after cold pressing, the single-sided coating weight of the negative electrode film, and the compaction density of the negative electrode film after cold pressing were adjusted.

实施例3Example 3

采用与实施例1相似的方法制备电池单体和电池,与实施例1不同的是,正极膜层的单面涂布重量、正极膜层冷压后的压实密度、负极膜层的单面涂布重量、负极膜层冷压后的压实密度作了调整。Battery cells and batteries were prepared using a method similar to that in Example 1. The difference from Example 1 is that the single-sided coating weight of the positive electrode film, the compaction density of the positive electrode film after cold pressing, the single-sided coating weight of the negative electrode film, and the compaction density of the negative electrode film after cold pressing were adjusted.

实施例4Example 4

采用与实施例1相似的方法制备电池单体和电池,与实施例1不同的是,正极膜层的单面涂布重量、正极膜层冷压后的压实密度、负极膜层的单面涂布重量、负极膜层冷压后的压实密度、第一汇流部件的单层结构的厚度Th作了调整。Battery cells and batteries were prepared using a method similar to that in Example 1. The difference from Example 1 is that the single-sided coating weight of the positive electrode film, the compaction density of the positive electrode film after cold pressing, the single-sided coating weight of the negative electrode film, the compaction density of the negative electrode film after cold pressing, and the thickness Th of the single-layer structure of the first busbar were adjusted.

实施例5Example 5

采用与实施例1相似的方法制备电池单体和电池,与实施例1不同的是,正极膜层的单面涂布重量、正极膜层冷压后的压实密度、负极膜层的单面涂布重量、负极膜层冷压后的压实密度、第一汇流部件的单层结构的厚度Th作了调整。Battery cells and batteries were prepared using a method similar to that in Example 1. The difference from Example 1 is that the single-sided coating weight of the positive electrode film, the compaction density of the positive electrode film after cold pressing, the single-sided coating weight of the negative electrode film, the compaction density of the negative electrode film after cold pressing, and the thickness Th of the single-layer structure of the first busbar were adjusted.

实施例6Example 6

采用与实施例1相似的方法制备电池单体和电池,与实施例1不同的是,正极膜层的单面涂布重量、正极膜层冷压后的压实密度、负极膜层的单面涂布重量、负极膜层冷压后的压实密度、第一汇流部件的单层结构的厚度Th作了调整。Battery cells and batteries were prepared using a method similar to that in Example 1. The difference from Example 1 is that the single-sided coating weight of the positive electrode film, the compaction density of the positive electrode film after cold pressing, the single-sided coating weight of the negative electrode film, the compaction density of the negative electrode film after cold pressing, and the thickness Th of the single-layer structure of the first busbar were adjusted.

实施例7Example 7

采用与实施例1相似的方法制备电池单体和电池,与实施例1不同的是,正极膜层的单面涂布重量、正极膜层冷压后的压实密度、负极膜层的单面涂布重量、负极膜层冷压后的压实密度、第一汇流部件的单层结构的厚度Th作了调整。Battery cells and batteries were prepared using a method similar to that in Example 1. The difference from Example 1 is that the single-sided coating weight of the positive electrode film, the compaction density of the positive electrode film after cold pressing, the single-sided coating weight of the negative electrode film, the compaction density of the negative electrode film after cold pressing, and the thickness Th of the single-layer structure of the first busbar were adjusted.

对比例1Comparative Example 1

采用与实施例1相似的方法制备电池单体和电池,与实施例1不同的是,正极膜层的单面涂布重量、负极膜层的单面涂布重量、负极膜层冷压后的压实密度作了调整。Battery cells and batteries were prepared using a method similar to that in Example 1. The difference from Example 1 was that the single-sided coating weight of the positive electrode film, the single-sided coating weight of the negative electrode film, and the compaction density of the negative electrode film after cold pressing were adjusted.

对比例2Comparative Example 2

采用与实施例1相似的方法制备电池单体和电池,与实施例1不同的是,正极膜层的单面涂布重量、正极膜层冷压后的压实密度、负极膜层的单面涂布重量、负极膜层冷压后的压实密度、第一汇流部件的单层结构的厚度Th作了调整作了调整。Battery cells and batteries were prepared using a method similar to that in Example 1. The differences from Example 1 are that the single-sided coating weight of the positive electrode film, the compaction density of the positive electrode film after cold pressing, the single-sided coating weight of the negative electrode film, the compaction density of the negative electrode film after cold pressing, and the thickness Th of the single-layer structure of the first busbar were adjusted.

对比例3Comparative Example 3

采用与实施例1相似的方法制备电池单体和电池,与实施例1不同的是,正极膜层的单面涂布重量、正极膜层冷压后的压实密度、负极膜层的单面涂布重量、负极膜层冷压后的压实密度、第一汇流部件的单层结构的厚度Th作了调整作了调整。 Battery cells and batteries were prepared using a method similar to that in Example 1. The differences from Example 1 are that the single-sided coating weight of the positive electrode film, the compaction density of the positive electrode film after cold pressing, the single-sided coating weight of the negative electrode film, the compaction density of the negative electrode film after cold pressing, and the thickness Th of the single-layer structure of the first busbar were adjusted.

对比例4Comparative Example 4

采用与实施例1相似的方法制备电池单体和电池,与实施例1不同的是,正极膜层的单面涂布重量、正极膜层冷压后的压实密度、负极膜层的单面涂布重量、负极膜层冷压后的压实密度、第一汇流部件的单层结构的厚度Th作了调整作了调整。Battery cells and batteries were prepared using a method similar to that in Example 1. The differences from Example 1 are that the single-sided coating weight of the positive electrode film, the compaction density of the positive electrode film after cold pressing, the single-sided coating weight of the negative electrode film, the compaction density of the negative electrode film after cold pressing, and the thickness Th of the single-layer structure of the first busbar were adjusted.

性能测试Performance testing

1、测试电池单体的膨胀压强:1. Test the expansion pressure of a single battery cell:

于45℃的环境温度中,将上述制备出的电池单体以1C的恒流放电倍率放电至2.0V;The prepared battery cell was discharged to 2.0V at a constant current discharge rate of 1C at an ambient temperature of 45℃.

将电池单体夹持于两个夹板之间,其中,两个夹板分别位于电池单体沿厚度方向的两侧,并覆盖大面;The battery cell is clamped between two clamping plates, which are located on both sides of the battery cell along its thickness direction and cover its large surface area.

于45℃的环境温度中,将电池单体以0.8C的恒流充电倍率充电至3.8V,检测并记录电池单体对夹板施加的压力;At an ambient temperature of 45°C, the battery cells were charged to 3.8V at a constant current charging rate of 0.8C, and the pressure exerted by the battery cells on the clamping plate was detected and recorded.

按照上述充电策略和充电策略对电池单体进行循环充放电,直至电池单体衰减至70%SOH(电池单体的放电容量衰减至电池单体标称容量的70%),记录电池单体对夹板施加的最大压力;The battery cells were cyclically charged and discharged according to the above charging strategy until the battery cells degraded to 70% SOH (the discharge capacity of the battery cells degraded to 70% of the nominal capacity of the battery cells), and the maximum pressure exerted by the battery cells on the clamping plate was recorded.

计算电池单体在厚度方向上的膨胀压强Q为:最大压力/大面面积。The expansion pressure Q of a single battery cell in the thickness direction is calculated as: maximum pressure / large surface area.

2、体积能量密度测试:2. Volumetric energy density test:

首周放电能量按照以下步骤测试:在25℃下,将上述制备出的电池单体以0.33C恒电流充电至3.8V,再以0.33C恒流放电至2.0V,记录此时的放电能量A0,单位:Wh。The discharge energy in the first week was tested according to the following steps: At 25°C, the prepared battery cell was charged to 3.8V with a constant current of 0.33C, and then discharged to 2.0V with a constant current of 0.33C. The discharge energy A0 at this time was recorded, in Wh.

电池单体的体积:使用卡尺测量电池单体的长度、宽度、高度(一般以电池单体的外壳尺寸计算,排除电极端子高度,且排除外壳外的绝缘膜),计算单体电池体积V0,单位L。Volume of a single battery cell: Use calipers to measure the length, width, and height of the single battery cell (generally calculated based on the outer casing dimensions, excluding the height of the electrode terminals and the insulating film outside the casing), and calculate the volume of the single battery cell V0, in liters (L).

电池单体的体积能量密度VED=A0/V0,单位Wh/L。The volumetric energy density of a single battery cell is VED = A0/V0, in Wh/L.

3、循环性能测试一:3. Cyclic performance test one:

于45℃的环境温度中,对上述制备出的电池进行放电,将电池单体以1C的恒流放电倍率放电至2.0V;The battery prepared above was discharged at an ambient temperature of 45°C, and the battery cells were discharged to 2.0V at a constant current discharge rate of 1C.

于45℃的环境温度中,对上述制备出的电池进行充电,将电池单体以0.8C的恒流充电倍率充电至3.8V;The battery prepared above was charged at an ambient temperature of 45°C, and the battery cells were charged to 3.8V at a constant current charging rate of 0.8C.

按照上述充电策略和充电策略对电池进行循环充放电,直至电池衰减至70%SOH(电池的放电容量/电池的标称容量=70%);The battery is cycled through charging and discharging according to the above charging strategy until the battery degrades to 70% SOH (battery discharge capacity / battery nominal capacity = 70%).

在循环过程中,检测电池单体的外壳的端盖的最高温度,并观察第一汇流部件与电极端子的焊接处是否开裂。During the cycle, the highest temperature of the end cap of the battery cell casing is detected, and it is observed whether the weld between the first busbar and the electrode terminal is cracked.

4、循环性能测试二:4. Cyclic performance test two:

于30℃的环境温度中,对上述制备出的电池进行放电,将电池单体以0.33C放电 至2.0V;The battery prepared above was discharged at an ambient temperature of 30°C, with each battery cell discharged at 0.33C. Up to 2.0V;

于30℃的环境温度中,采用下述充电策略进行充电:At an ambient temperature of 30°C, the following charging strategy is used for charging:

以5.0C恒流从0%SOC充电至5%SOC;Charge from 0% SOC to 5% SOC at a constant current of 5.0C;

以5.0C恒流从5%SOC充电至10%SOC;Charge from 5% SOC to 10% SOC at a constant current of 5.0C;

以5.0C恒流从10%SOC充电至15%SOC;Charge from 10% SOC to 15% SOC at a constant current of 5.0C;

以5.0C恒流从15%SOC充电至20%SOC;Charge from 15% SOC to 20% SOC at a constant current of 5.0C;

以5.0C恒流从20%SOC充电至25%SOC;Charge from 20% SOC to 25% SOC at a constant current of 5.0C;

以5.0C恒流从25%SOC充电至30%SOC;Charge from 25% SOC to 30% SOC at a constant current of 5.0C;

以5.0C恒流从30%SOC充电至35%SOC;Charge from 30% SOC to 35% SOC at a constant current of 5.0C;

以5.0C恒流从35%SOC充电至40%SOC;Charge from 35% SOC to 40% SOC at a constant current of 5.0C;

以4.6C恒流从40%SOC充电至45%SOC;Charge from 40% SOC to 45% SOC at a constant current of 4.6C;

以4.3C恒流从45%SOC充电至50%SOC;Charge from 45% SOC to 50% SOC at a constant current of 4.3C;

以4.0C恒流从50%SOC充电至55%SOC;Charge from 50% SOC to 55% SOC at a constant current of 4.0C;

以3.7C恒流从55%SOC充电至60%SOC;Charge from 55% SOC to 60% SOC at a constant current of 3.7C;

以3.4C恒流从60%SOC充电至65%SOC;Charge from 60% SOC to 65% SOC at a constant current of 3.4C;

以3.1C恒流从65%SOC充电至70%SOC;Charge from 65% SOC to 70% SOC at a constant current of 3.1C;

以2.9C恒流从70%SOC充电至75%SOC;Charge from 70% SOC to 75% SOC at a constant current of 2.9C;

以2.7C恒流从75%SOC充电至80%SOC;Charge from 75% SOC to 80% SOC at a constant current of 2.7C;

以1.8C恒流从80%SOC充电至85%SOC;Charge from 80% SOC to 85% SOC at a constant current of 1.8C;

以1.3C恒流从85%SOC充电至90%SOC;Charge from 85% SOC to 90% SOC at a constant current of 1.3C;

以0.7C恒流从90%SOC充电至95%SOC;Charge from 90% SOC to 95% SOC at a constant current of 0.7C;

以0.33C恒流从95%SOC充电至98%SOC;Charge from 95% SOC to 98% SOC at a constant current of 0.33C;

以0.1C恒流从98%SOC充电至100%SOC。Charge from 98% SOC to 100% SOC at a constant current of 0.1C.

按照上述充电策略和充电策略对电池进行循环充放电,直至电池衰减至70%SOH;The battery is cycled through charging and discharging according to the above charging strategy until the battery degrades to 70% SOH.

在循环过程中,检测电池单体的外壳的端盖的最高温度,并观察第一汇流部件与电极端子的焊接处是否开裂。During the cycle, the highest temperature of the end cap of the battery cell casing is detected, and it is observed whether the weld between the first busbar and the electrode terminal is cracked.

在此说明的是,循环性能测试一和循环性能测试二是分别对相同制备方法制备出的两个电池进行测试。It should be noted that cycle performance test one and cycle performance test two were conducted on two batteries prepared by the same preparation method.

实施例1-7以及对比例1-4的测试结果如表1所示。
The test results of Examples 1-7 and Comparative Examples 1-4 are shown in Table 1.

参照表1中的对比例1,正极膜层的单面涂布重量、正极膜层冷压后的压实密度、负极膜层的单面涂布重量、负极膜层冷压后的压实密度较低,虽然电池单体具有较小的膨胀压强,且在循环的过程中电极端子与第一汇流部件之间的焊印不易开裂,但是电池单体的体积能量密度较低。Referring to Comparative Example 1 in Table 1, the single-sided coating weight of the positive electrode film, the compaction density of the positive electrode film after cold pressing, the single-sided coating weight of the negative electrode film, and the compaction density of the negative electrode film after cold pressing are all relatively low. Although the battery cell has a small expansion pressure and the solder joint between the electrode terminal and the first busbar is not easy to crack during cycling, the volumetric energy density of the battery cell is relatively low.

参照实施例1-7和对比例1,本申请实施例可以增大正极膜层的单面涂布重量、正极膜层冷压后的压实密度、负极膜层的单面涂布重量、负极膜层冷压后的压实密度,以使电池单体的体积能量密度大于或等于390Wh/L。虽然电池单体的膨胀压强不低于0.5MPa,但是结合具有双层结构的第一汇流部件,可降低因膨胀压强增大而引发的焊印开裂的风险,提高电池的可靠性。第一汇流部件具有双层结构,其过流能力强,从而减少第一汇流部件在循环过程中的产热,进而减少了传导至端盖和电极组件的热量,降低电池单体的温升,改善电池的循环性能。Referring to Examples 1-7 and Comparative Example 1, the embodiments of this application can increase the single-sided coating weight of the positive electrode film, the compaction density of the positive electrode film after cold pressing, the single-sided coating weight of the negative electrode film, and the compaction density of the negative electrode film after cold pressing, so that the volumetric energy density of the battery cell is greater than or equal to 390Wh/L. Although the expansion pressure of the battery cell is not less than 0.5MPa, the combination of the first busbar component with a double-layer structure can reduce the risk of solder cracking caused by the increase in expansion pressure and improve the reliability of the battery. The first busbar component has a double-layer structure and strong current carrying capacity, thereby reducing the heat generation of the first busbar component during cycling, and further reducing the heat conducted to the end cap and electrode assembly, reducing the temperature rise of the battery cell, and improving the cycle performance of the battery.

参照实施例1-7和对比例2-3,本申请实施例通过调整正极膜层的单面涂布重量、正极膜层冷压后的压实密度、负极膜层的单面涂布重量、负极膜层冷压后的压实密度等参数,可以将电池单体的膨胀压强限制为不超过2.4MPa,并能够使电池单体的体积能量密度达到415Wh/L。Referring to Examples 1-7 and Comparative Examples 2-3, the embodiments of this application can limit the expansion pressure of a single cell to no more than 2.4 MPa and enable the volumetric energy density of the single cell to reach 415 Wh/L by adjusting parameters such as the single-sided coating weight of the positive electrode film, the compaction density of the positive electrode film after cold pressing, the single-sided coating weight of the negative electrode film, and the compaction density of the negative electrode film after cold pressing.

通过调整第一汇流部件的单层结构的厚度,可以平衡第一汇流部件的过流能力和可变形能力。在电池单体的膨胀压强为0.5MPa-2.4Mpa时,将第一汇流部件的单层结构的厚度限定为不超过2.5mm,可以降低电极端子与第一汇流部件之间的焊印被拉裂的风险,并减少第一汇流部件在循环过程中的产热,进而减少了传导至端盖和电极组件的热量,降低电池单体的温升,改善电池的循环性能。By adjusting the thickness of the single-layer structure of the first busbar component, its current-carrying capacity and deformability can be balanced. When the expansion pressure of the battery cell is 0.5MPa-2.4MPa, limiting the thickness of the single-layer structure of the first busbar component to no more than 2.5mm can reduce the risk of the solder joint between the electrode terminals and the first busbar component being torn, and reduce the heat generation of the first busbar component during cycling. This, in turn, reduces the heat conducted to the end cap and electrode assembly, lowers the temperature rise of the battery cell, and improves the cycle performance of the battery.

参照实施例1-7和对比例4,通过调整第一汇流部件的单层结构的厚度,可以平衡第一汇流部件的过流能力和可变形能力。本申请实施例将第一汇流部件的单层结构的厚度限定为不低于1mm,可以在电池单体的膨胀压强为0.5MPa-2.4Mpa时,提升过流能力,减少第一汇流部件在循环过程中的产热,进而减少了传导至端盖和电极组件的热量,降低电池单体的温升,改善电池的循环性能。Referring to Examples 1-7 and Comparative Example 4, by adjusting the thickness of the single-layer structure of the first busbar component, the current-carrying capacity and deformability of the first busbar component can be balanced. In this embodiment, the thickness of the single-layer structure of the first busbar component is limited to not less than 1 mm. This improves the current-carrying capacity and reduces heat generation of the first busbar component during cycling when the expansion pressure of the battery cell is between 0.5 MPa and 2.4 MPa. This, in turn, reduces the heat conducted to the end caps and electrode assemblies, lowers the temperature rise of the battery cell, and improves the battery's cycle performance.

参照表1的实施例1-7,本申请实施例可以在电池快速充电的过程中,降低第一汇流部件的产热,减小电池单体的膨胀,以降低电池失效的风险。本申请的电池单体具有快速充电的能力,电池单体从10%SOC充电至80%SOC的充电时间可为5分钟至10.5分钟。Referring to Examples 1-7 in Table 1, the embodiments of this application can reduce the heat generation of the first busbar component and reduce the expansion of the battery cells during the fast charging process, thereby reducing the risk of battery failure. The battery cells of this application have the ability to be fast charged, and the charging time for the battery cells from 10% SOC to 80% SOC can be 5 minutes to 10.5 minutes.

需要说明的是,在不冲突的情况下,本申请中的实施例及实施例中的特征可以相互组合。It should be noted that, unless otherwise specified, the embodiments and features described in this application can be combined with each other.

最后应说明的是:以上实施例仅用以说明本申请的技术方案,而非对其限制;尽管参照前述实施例对本申请进行了详细的说明,本领域的普通技术人员应当理解:其依然可以对前述各实施例所记载的技术方案进行修改,或者对其中部分技术特征进行等同替换,但这些修改或者替换,并不使相应技术方案的本质脱离本申请各实施例技术方案的精神和范围。 Finally, it should be noted that the above embodiments are only used to illustrate the technical solutions of this application, and are not intended to limit them. Although this application has been described in detail with reference to the foregoing embodiments, those skilled in the art should understand that they can still modify the technical solutions described in the foregoing embodiments, or make equivalent substitutions for some of the technical features. However, these modifications or substitutions do not cause the essence of the corresponding technical solutions to deviate from the spirit and scope of the technical solutions of the embodiments of this application.

Claims (47)

一种电池,包括:A battery comprising: 多个电池单体,沿所述电池单体的厚度方向排列,所述电池单体包括外壳和容纳于所述外壳内的电极组件,所述电池单体在所述厚度方向上的膨胀压强为0.5MPa-2.4MPa;以及,Multiple battery cells are arranged along their thickness direction. Each battery cell includes a casing and an electrode assembly housed within the casing. The expansion pressure of each battery cell in the thickness direction is 0.5 MPa to 2.4 MPa. 第一汇流部件,电连接至少两个沿所述厚度方向排列设置的所述电池单体,所述第一汇流部件为多层结构,The first busbar component electrically connects at least two of the battery cells arranged along the thickness direction. The first busbar component has a multi-layer structure. 其中,所述电极组件包括正极片、负极片以及位于所述正极片和负极片之间的隔离膜,所述正极片包括正极集流体和设置于所述正极集流体至少一侧的正极膜层,所述正极膜层中包括正极活性材料,所述正极活性材料包括橄榄石结构的含锂磷酸盐,所述负极片包括负极集流体和设置于所述负极集流体至少一侧的负极膜层,所述负极膜层包括负极活性材料,所述负极活性材料包括碳基材料。The electrode assembly includes a positive electrode, a negative electrode, and a separator between the positive and negative electrode. The positive electrode includes a positive current collector and a positive electrode film layer disposed on at least one side of the positive current collector. The positive electrode film layer includes a positive active material, which includes a lithium phosphate with an olivine structure. The negative electrode includes a negative current collector and a negative electrode film layer disposed on at least one side of the negative current collector. The negative electrode film layer includes a negative active material, which includes a carbon-based material. 根据权利要求1所述的电池,其中,所述第一汇流部件包括层叠并连接的第一汇流层和第二汇流层,所述第一汇流层连接至少两个沿所述厚度方向排列的所述电池单体。According to claim 1, the battery wherein the first busbar component comprises a first busbar layer and a second busbar layer stacked and connected, the first busbar layer connecting at least two battery cells arranged along the thickness direction. 根据权利要求2所述的电池,其中,所述电池单体包括设置于所述外壳的电极端子,所述电极端子电连接于所述电极组件;According to claim 2, the battery cell includes an electrode terminal disposed on the housing, the electrode terminal being electrically connected to the electrode assembly; 所述第一汇流层的不与所述第二汇流层重叠的部分连接于所述电极端子。The portion of the first bus layer that does not overlap with the second bus layer is connected to the electrode terminal. 根据权利要求3所述的电池,其中,所述第一汇流层焊接于所述电极端子,且所述第一汇流层与所述电极端子的焊接面积大于或等于60mm2According to claim 3, the first busbar is welded to the electrode terminal, and the welding area between the first busbar and the electrode terminal is greater than or equal to 60 mm² . 根据权利要求2-4任一项所述的电池,其中,所述第一汇流部件包括至少一个弯折部,所述弯折部连接所述第一汇流层和所述第二汇流层。The battery according to any one of claims 2-4, wherein the first busbar component includes at least one bend, the bend connecting the first busbar layer and the second busbar layer. 根据权利要求5所述的电池,其中,所述第一汇流层包括第一汇流部、第二汇流部以及第一缓冲部,所述第一汇流部和所述第二汇流部沿所述厚度方向设置并连接于不同的所述电池单体,所述第一缓冲部连接所述第一汇流部与所述第二汇流部;According to claim 5, the battery, wherein the first busbar layer includes a first busbar portion, a second busbar portion and a first buffer portion, the first busbar portion and the second busbar portion are disposed along the thickness direction and connected to different battery cells, and the first buffer portion connects the first busbar portion and the second busbar portion; 所述第一汇流部和所述第二汇流部中的至少一者连接于所述弯折部。At least one of the first busbar and the second busbar is connected to the bend. 根据权利要求6所述的电池,其中,所述弯折部与所述第一缓冲部避开设置。According to claim 6, the battery is provided in a manner that avoids the first buffer portion. 根据权利要求6或7所述的电池,其中,所述第二汇流层包括第一层叠部、第二层叠部和第二缓冲部,所述第一层叠部与所述第一汇流部层叠并通过至少一个所述弯折部连接,所述第二层叠部与所述第二汇流部层叠并通过至少一个所述弯折部连接,According to claim 6 or 7, the battery wherein the second busbar layer includes a first stacked portion, a second stacked portion, and a second buffer portion, the first stacked portion being stacked with the first busbar portion and connected through at least one of the bending portions, and the second stacked portion being stacked with the second busbar portion and connected through at least one of the bending portions. 所述第二缓冲部连接所述第一层叠部和所述第二层叠部;The second buffer section connects the first stacked section and the second stacked section; 在所述第一汇流层与所述第二汇流层的层叠方向上,所述第二缓冲部与所述第一缓冲部至少部分的重叠。In the stacking direction of the first busbar layer and the second busbar layer, the second buffer portion overlaps at least partially with the first buffer portion. 根据权利要求8所述的电池,其中,所述第二缓冲部和所述第一缓冲部贴合设置。According to claim 8, the second buffer portion and the first buffer portion are fitted together. 根据权利要求2-9任一项所述的电池,其中,所述电池还包括至少一个第二汇流部件,所述第二汇流部件为单层结构并电连接至少两个所述电池单体,所述第二汇流部件的厚度大于所述第一汇流层的厚度,且所述第二汇流部件的厚度大于所述第二 汇流层的厚度。The battery according to any one of claims 2-9, wherein the battery further comprises at least one second busbar component, the second busbar component being a single-layer structure and electrically connected to at least two battery cells, the thickness of the second busbar component being greater than the thickness of the first busbar layer, and the thickness of the second busbar component being greater than the thickness of the second battery cell. Thickness of the catchment layer. 根据权利要求10所述的电池,其中,所述第一汇流层的厚度与所述第二汇流层的厚度之和等于所述第二汇流部件的厚度。According to claim 10, the sum of the thickness of the first busbar layer and the thickness of the second busbar layer is equal to the thickness of the second busbar component. 根据权利要求2-11任一项所述的电池,其中,The battery according to any one of claims 2-11, wherein, 所述第一汇流层的厚度为1mm-2.5mm;和/或The thickness of the first busbar layer is 1mm-2.5mm; and/or 所述第二汇流层的厚度为1mm-2.5mm。The thickness of the second busbar is 1mm-2.5mm. 根据权利要求2-12任一项所述的电池,其中,所述电池单体的体积能量密度为390Wh/L-450Wh/L,所述第一汇流层的厚度小于或等于2.5mm;或者,The battery according to any one of claims 2-12, wherein the volumetric energy density of the battery cell is 390Wh/L-450Wh/L, and the thickness of the first busbar layer is less than or equal to 2.5mm; or, 所述电池单体的体积能量密度为450Wh/L-480Wh/L,所述第一汇流层的厚度小于或等于2.2mm。The volumetric energy density of the battery cell is 450Wh/L-480Wh/L, and the thickness of the first busbar is less than or equal to 2.2mm. 根据权利要求2-13任一项所述的电池,其中,所述负极活性材料中还包括硅基材料;The battery according to any one of claims 2-13, wherein the negative electrode active material further comprises a silicon-based material; 所述硅基材料中硅元素在所述负极活性材料中的质量含量为1%-6%;所述第一汇流层的厚度为1.2mm-2.2mm,所述第二汇流层的厚度为1.2mm-2.2mm。The silicon-based material contains 1%-6% silicon by mass in the negative electrode active material; the thickness of the first busbar layer is 1.2mm-2.2mm, and the thickness of the second busbar layer is 1.2mm-2.2mm. 根据权利要求2-14任一项所述的电池,其中,所述第一汇流层包括第一汇流部、第二汇流部以及连接所述第一汇流部和所述第二汇流部的第一缓冲部,所述第一汇流部和所述第二汇流部沿所述厚度方向设置并连接于不同的所述电池单体;The battery according to any one of claims 2-14, wherein the first busbar layer includes a first busbar portion, a second busbar portion, and a first buffer portion connecting the first busbar portion and the second busbar portion, the first busbar portion and the second busbar portion being disposed along the thickness direction and connected to different battery cells; 在所述第一汇流层和所述第二汇流层的层叠方向上,所述第一缓冲部凸出于所述第一汇流部和所述第二汇流部;In the stacking direction of the first busbar layer and the second busbar layer, the first buffer portion protrudes from the first busbar portion and the second busbar portion; 所述第一汇流层在与所述第一缓冲部对应的位置设有凹部。The first busbar layer has a recess at a position corresponding to the first buffer section. 根据权利要求15所述的电池,其中,The battery according to claim 15, wherein, 所述电池单体的体积能量密度为390Wh/L-450Wh/L,所述凹部的深度为1.2mm-2.5mm;或者,The volumetric energy density of the battery cell is 390Wh/L-450Wh/L, and the depth of the recess is 1.2mm-2.5mm; or, 所述电池单体的体积能量密度为450Wh/L-480Wh/L,所述凹部的深度为1mm-2.2mm。The volumetric energy density of the battery cell is 450Wh/L-480Wh/L, and the depth of the recess is 1mm-2.2mm. 根据权利要求1-16任一项所述的电池,其中,在所述多个电池单体中,沿所述厚度方向位于最外侧所述电池单体连接于所述第一汇流部件。The battery according to any one of claims 1-16, wherein, among the plurality of battery cells, the outermost battery cell located along the thickness direction is connected to the first busbar. 根据权利要求1-17任一项所述的电池,其中,所述电极组件包括两个第一表面和两个第二表面,两个所述第一表面沿所述厚度方向相对设置,两个所述第二表面沿与所述厚度方向垂直的方向相对设置,所述第二表面连接两个所述第一表面;The battery according to any one of claims 1-17, wherein the electrode assembly includes two first surfaces and two second surfaces, the two first surfaces are disposed opposite to each other along the thickness direction, the two second surfaces are disposed opposite to each other along a direction perpendicular to the thickness direction, and the second surfaces are connected to the two first surfaces; 所述第一表面的面积大于所述第二表面的面积。The area of the first surface is greater than the area of the second surface. 根据权利要求1-18任一项所述的电池,其中,所述电池单体在所述厚度方向上的膨胀压强为1.5MPa-2.0MPa。The battery according to any one of claims 1-18, wherein the expansion pressure of the battery cell in the thickness direction is 1.5 MPa-2.0 MPa. 根据权利要求1-19任一项所述的电池,其中,所述负极膜层的单面涂布重量为90mg/1540mm2至170mg/1540mm2,可选为110mg/1540mm2至150mg/1540mm2According to any one of claims 1-19, the single-sided coating weight of the negative electrode film layer is from 90 mg/1540 mm² to 170 mg/1540 mm² , and optionally from 110 mg/1540 mm² to 150 mg/1540 mm² . 根据权利要求1-20任一项所述的电池,其中,所述负极膜层于所述电池单体100%SOC下的压实密度为1.15g/cm3至1.36g/cm3,可选为1.25g/cm3至1.36g/cm3According to any one of claims 1-20, the negative electrode film layer has a compaction density of 1.15 g/ cm³ to 1.36 g/ cm³ at 100% SOC of the battery cell, and is optionally 1.25 g/ cm³ to 1.36 g/ cm³ . 根据权利要求1-21任一项所述的电池,其中,所述负极片的孔隙率为27%-40%。 The battery according to any one of claims 1-21, wherein the porosity of the negative electrode is 27%-40%. 根据权利要求1-22任一项所述的电池,其中,所述碳基材料包括人造石墨和天然石墨中的至少一种。The battery according to any one of claims 1-22, wherein the carbon-based material comprises at least one of artificial graphite and natural graphite. 根据权利要求1-23任一项所述的电池,其中,所述负极活性材料中还包括硅基材料,所述硅基材料中硅元素在所述负极活性材料中的质量含量为0.3%至10%,可选为1%至6%。The battery according to any one of claims 1-23, wherein the negative electrode active material further comprises a silicon-based material, wherein the silicon element in the silicon-based material has a mass content of 0.3% to 10%, optionally 1% to 6%. 根据权利要求24所述的电池,其中,所述硅基材料包括硅氧化合物和硅碳复合物中的至少一种。The battery according to claim 24, wherein the silicon-based material comprises at least one of silicon oxide and silicon-carbon composite. 根据权利要求1-25任一项所述的电池,其中,所述负极膜层包括第一负极膜层和第二负极膜层,所述第二负极膜层设置于所述第一负极膜层和所述负极集流体之间;The battery according to any one of claims 1-25, wherein the negative electrode film layer comprises a first negative electrode film layer and a second negative electrode film layer, and the second negative electrode film layer is disposed between the first negative electrode film layer and the negative electrode current collector; 所述负极活性材料包括设置于所述第一负极膜层的第一负极活性材料和设置于所述第二负极膜层的第二负极活性材料,所述第一负极活性材料包括人造石墨,所述第二负极活性材料包括人造石墨、天然石墨和硅基材料的一种或多种。The negative electrode active material includes a first negative electrode active material disposed on the first negative electrode film layer and a second negative electrode active material disposed on the second negative electrode film layer. The first negative electrode active material includes artificial graphite, and the second negative electrode active material includes one or more of artificial graphite, natural graphite, and silicon-based materials. 根据权利要求26所述的电池,其中,所述第一负极膜层的厚度和所述第二负极膜层的厚度比值为3:7至7:3,可选为4:6至6:4。According to the battery of claim 26, the ratio of the thickness of the first negative electrode film to the thickness of the second negative electrode film is 3:7 to 7:3, and optionally 4:6 to 6:4. 根据权利要求26或27所述的电池,其中,所述第一负极膜层的厚度小于或等于所述第二负极膜层的厚度。The battery according to claim 26 or 27, wherein the thickness of the first negative electrode film is less than or equal to the thickness of the second negative electrode film. 根据权利要求26-28任一项所述的电池,其中,所述第一负极活性材料的体积平均粒径Dv50小于或等于所述第二负极活性材料的体积平均粒径Dv50。The battery according to any one of claims 26-28, wherein the volume average particle size Dv50 of the first negative electrode active material is less than or equal to the volume average particle size Dv50 of the second negative electrode active material. 根据权利要求26-29任一项所述的电池,其中,所述第一负极活性材料的体积平均粒径Dv50为7.8μm-14.3μm,可选为7.8μm-11.3μm;According to any one of claims 26-29, the volume average particle size Dv50 of the first negative electrode active material is 7.8 μm-14.3 μm, and optionally 7.8 μm-11.3 μm; 所述第二负极活性材料的体积平均粒径Dv50为Dv50为9.5μm-18.5μm,可选为9.5μm-14.6μm。The volume average particle size Dv50 of the second negative electrode active material is 9.5μm-18.5μm, and can be selected as 9.5μm-14.6μm. 根据权利要求1-30任一项所述的电池,其中,所述负极活性材料的比表面积为0.5m2/g-3m2/g,可选为0.6m2/g-1.2m2/g。According to any one of claims 1-30, the specific surface area of the negative electrode active material is 0.5 /g-3 /g, optionally 0.6 /g-1.2 /g. 根据权利要求1-31任一项所述的电池,其中,所述正极膜层的单面涂布重量为200mg/1540mm2-370mg/1540/mm2;可选为240mg/1540mm2至330mg/1540mm2According to any one of claims 1-31, the single-sided coating weight of the positive electrode film is 200mg/1540mm² - 370mg/ 1540mm² ; optionally, it is 240mg/ 1540mm² to 330mg/ 1540mm² . 根据权利要求1-32任一项所述的电池,其中,所述正极膜层于所述电池单体100%SOC下的压实密度为2.50g/cm3至2.80g/cm3;可选为2.55g/cm3-2.70g/cm3According to any one of claims 1-32, the positive electrode film layer has a compaction density of 2.50 g/ cm³ to 2.80 g/ cm³ at 100% SOC of the battery cell; optionally, it is 2.55 g/ cm³ to 2.70 g/ cm³ . 根据权利要求1-33任一项所述的电池,其中,所述正极片的孔隙率为25%-32%。The battery according to any one of claims 1-33, wherein the porosity of the positive electrode is 25%-32%. 根据权利要求1-34任一项所述的电池,其中,所述正极片的厚度为0.13mm-0.2mm。The battery according to any one of claims 1-34, wherein the thickness of the positive electrode sheet is 0.13mm-0.2mm. 根据权利要求1-35任一项所述的电池,其中,所述正极集流体的厚度与所述正极膜层的厚度之比为0.05-0.3。According to any one of claims 1-35, the ratio of the thickness of the positive current collector to the thickness of the positive electrode film is 0.05-0.3. 根据权利要求1-36任一项所述的电池,其中,所述正极活性材料的体积平均粒径满足1μm≤Dv50≤2μm,0.4μm≤Dv10≤0.7μm。According to any one of claims 1-36, the volume average particle size of the positive electrode active material satisfies 1μm≤Dv50≤2μm and 0.4μm≤Dv10≤0.7μm. 根据权利要求1-37任一项所述的电池,其中,所述电池单体包括容纳于所述外壳内的电解液。The battery according to any one of claims 1-37, wherein the battery cell includes an electrolyte contained within the casing. 根据权利要求38所述的电池,其中,所述电解液于室温下的电导率为15mS/cm 至20mS/cm。According to claim 38, the electrolyte has a conductivity of 15 mS/cm at room temperature. Up to 20 mS/cm. 根据权利要求38或39所述的电池,其中,所述电解液包括有机溶剂,所述有机溶剂包括碳酸酯类溶剂和羧酸酯类溶剂中的一种或多种。The battery according to claim 38 or 39, wherein the electrolyte comprises an organic solvent, the organic solvent comprising one or more of carbonate solvents and carboxylic acid ester solvents. 根据权利要求40所述的电池,其中,所述碳酸酯类溶剂包括碳酸乙烯酯、碳酸丙烯酯、碳酸二甲酯、碳酸二乙酯和碳酸甲乙酯中的一种或多种。According to claim 40, the battery wherein the carbonate solvent includes one or more of ethylene carbonate, propylene carbonate, dimethyl carbonate, diethyl carbonate, and ethyl methyl carbonate. 根据权利要求40或41所述的电池,其中,所述羧酸酯包括R1-COO-R2,R1和R2分别独立地包括碳原子数为1-5的烷基或碳原子数为1-5的卤代烷基。According to claim 40 or 41, the carboxylic acid ester comprises R1- COO- R2 , wherein R1 and R2 each independently comprise an alkyl group having 1-5 carbon atoms or a haloalkyl group having 1-5 carbon atoms. 根据权利要求38-42任一项所述的电池,其中,所述电解液包括锂盐,所述锂盐包括双氟磺酰亚胺锂LiFSI和六氟磷酸锂LiPF6,所述双氟磺酰亚胺锂LiFSI的摩尔浓度为0.2mol/L至0.5mol/L,所述六氟磷酸锂LiPF6的摩尔浓度为0.5mol/L至1.0mol/L。The battery according to any one of claims 38-42, wherein the electrolyte comprises a lithium salt, the lithium salt comprising lithium bis(fluorosulfonyl)imide (LiFSI) and lithium hexafluorophosphate ( LiPF6) , the molar concentration of the lithium bis(fluorosulfonyl)imide (LiFSI) being from 0.2 mol/L to 0.5 mol/L, and the molar concentration of the lithium hexafluorophosphate (LiPF6 ) being from 0.5 mol/L to 1.0 mol/L. 根据权利要求38-43任一项所述的电池,其中,所述电解液于室温下的密度ρ满足:1.05g/mL≤ρ≤1.35g/mL。According to any one of claims 38-43, the electrolyte density ρ at room temperature satisfies: 1.05 g/mL ≤ ρ ≤ 1.35 g/mL. 根据权利要求1-44任一项所述的电池,其中,所述电极组件沿所述厚度方向上的尺寸为T,单层所述负极片的厚度为T1,所述负极片在所述厚度方向上层叠的层数为N;The battery according to any one of claims 1-44, wherein the dimension of the electrode assembly along the thickness direction is T, the thickness of a single layer of the negative electrode sheet is T1, and the number of layers of the negative electrode sheet stacked in the thickness direction is N; T、T1以及N满足:0.3≤(N×T1)/T≤0.5。T, T1, and N satisfy: 0.3≤(N×T1)/T≤0.5. 根据权利要求1-45任一项所述的电池,其中,所述电池单体从10%SOC充电至80%SOC的充电时间为5分钟至10.5分钟。According to any one of claims 1-45, the charging time for a single battery cell to charge from 10% SOC to 80% SOC is 5 minutes to 10.5 minutes. 一种用电装置,其特征在于,包括根据权利要求1-46任一项所述的电池,所述电池用于提供电能。 An electrical device, characterized in that it comprises a battery according to any one of claims 1-46, the battery being used to provide electrical energy.
PCT/CN2024/102665 2024-06-28 2024-06-28 Battery and electrical apparatus Pending WO2026000399A1 (en)

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