CN110212247A - Battery cell - Google Patents

Battery cell Download PDF

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Publication number
CN110212247A
CN110212247A CN201810168627.6A CN201810168627A CN110212247A CN 110212247 A CN110212247 A CN 110212247A CN 201810168627 A CN201810168627 A CN 201810168627A CN 110212247 A CN110212247 A CN 110212247A
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lithium
negative electrode
per unit
unit area
positive electrode
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CN110212247B (en
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王国宝
刘江
刘晓梅
谢斌
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Contemporary Amperex Technology Co Ltd
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Contemporary Amperex Technology Co Ltd
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Priority to CN202110083467.7A priority patent/CN112928334A/en
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    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M10/00Secondary cells; Manufacture thereof
    • H01M10/05Accumulators with non-aqueous electrolyte
    • H01M10/058Construction or manufacture
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M10/00Secondary cells; Manufacture thereof
    • H01M10/05Accumulators with non-aqueous electrolyte
    • H01M10/052Li-accumulators
    • H01M10/0525Rocking-chair batteries, i.e. batteries with lithium insertion or intercalation in both electrodes; Lithium-ion batteries
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M10/00Secondary cells; Manufacture thereof
    • H01M10/42Methods or arrangements for servicing or maintenance of secondary cells or secondary half-cells
    • H01M10/4235Safety or regulating additives or arrangements in electrodes, separators or electrolyte
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • 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
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/10Energy storage using batteries
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P70/00Climate change mitigation technologies in the production process for final industrial or consumer products
    • Y02P70/50Manufacturing or production processes characterised by the final manufactured product

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

Abstract

The invention provides a battery cell. The battery core comprises a negative plate, a positive plate and an isolating membrane, wherein the negative plate comprises a negative current collector and a negative diaphragm which is arranged on the surface of the negative current collector and contains a negative active substance, the positive plate comprises a positive current collector and a positive diaphragm which is arranged on the surface of the positive current collector and contains a positive active substance, and the isolating membrane is arranged between the adjacent negative plate and the positive plate. The surface of the negative electrode diaphragm is also provided with a metal lithium layer, the weight of the metal lithium layer is 0.5% -5% of the total weight of the negative electrode diaphragm, the negative electrode capacity per unit area/the positive electrode capacity per unit area is 1.2-2.1, and the negative electrode capacity per unit area/(the positive electrode capacity per unit area + the metal lithium layer capacity per unit area x 80%) is more than or equal to 1.10. The battery cell has better cycle performance and storage performance.

Description

电芯Batteries

技术领域technical field

本发明涉及电池领域,更具体而言涉及一种电芯。The present invention relates to the field of batteries, and more particularly to a battery cell.

背景技术Background technique

在二次电池中,锂离子二次电池相对于其它种类的二次电池来说,其较高的能量密度优势使其在市场上占据主流地位。其中,以磷酸铁锂为正极活性物质的锂离子二次电池以其高安全性、低成本、长寿命的特点广泛应用于电动大巴动力系统,并在大规模储能领域拥有广泛的应用前景。Among secondary batteries, lithium-ion secondary batteries have a higher energy density advantage compared to other types of secondary batteries, making them occupy a mainstream position in the market. Among them, lithium ion secondary batteries with lithium iron phosphate as the positive active material are widely used in electric bus power systems due to their high safety, low cost, and long life, and have broad application prospects in the field of large-scale energy storage.

近年来,基于度电成本考虑,对锂离子二次电池寿命的要求越来越高。虽然磷酸铁锂具有较高的结构稳定性,但是在石墨负极表面会发生固体-电解质液界面膜(SEI膜)的溶解-修复平衡,导致可用于正负极之间穿梭的活性锂离子不断减少,从而不可避免地发生容量损失。以钛酸锂为负极活性物质、以磷酸铁锂为正极活性物质的锂离子二次电池由于不生成SEI膜,可以避免由SEI膜的溶解-修复平衡引起的负极副反应导致的容量损失,但是钛酸锂较高的电压平台导致锂离子二次电池的放电电压平台较低,能量密度过低,且钛酸锂昂贵的单价导致单位Wh成本过高,因此,需要有效的技术解决锂离子二次电池的长寿命问题。In recent years, based on the consideration of the cost per kilowatt hour, the requirements for the life of lithium-ion secondary batteries are getting higher and higher. Although lithium iron phosphate has high structural stability, the dissolution-repair equilibrium of the solid-electrolyte interface film (SEI film) occurs on the surface of the graphite anode, resulting in the continuous reduction of active lithium ions that can be used for shuttle between the anode and cathode. , so that capacity loss inevitably occurs. The lithium ion secondary battery using lithium titanate as the negative electrode active material and lithium iron phosphate as the positive electrode active material can avoid the capacity loss caused by the negative electrode side reaction caused by the dissolution-repair balance of the SEI film because it does not generate an SEI film, but The higher voltage platform of lithium titanate leads to a lower discharge voltage platform of lithium ion secondary batteries, and the energy density is too low, and the expensive unit price of lithium titanate leads to high unit Wh cost. Therefore, effective technologies are needed to solve lithium ion secondary batteries. The long life of the secondary battery.

目前改善锂离子二次电池寿命的主要手段有:选择循环性能和存储性能好的磷酸铁锂种类和石墨种类、优化电解液配方(改变有机溶剂、添加剂)、优化正极膜片和负极膜片配方、优化SEI膜成膜条件等。这些手段均从抑制由SEI膜的溶解-修复平衡引起的负极副反应角度考虑,通过节流的方式延缓活性锂离子的减少,因此能起到的作用有限,锂离子二次电池的循环寿命最高可以做到5000~6000次左右,与长寿命电动大巴和大规模储能系统10000次以上循环寿命的目标尚有较大差距。At present, the main means to improve the life of lithium ion secondary batteries are: selecting lithium iron phosphate and graphite types with good cycle performance and storage performance, optimizing electrolyte formula (changing organic solvents, additives), optimizing positive electrode diaphragm and negative electrode diaphragm formula , optimize the SEI film forming conditions, etc. All of these measures are considered from the viewpoint of suppressing the negative side reactions caused by the dissolution-repair balance of the SEI film, and the reduction of active lithium ions is delayed by throttling, so they can play a limited role, and the cycle life of lithium ion secondary batteries is the highest. It can achieve about 5,000 to 6,000 cycles, which is still far from the target of more than 10,000 cycles of long-life electric buses and large-scale energy storage systems.

发明内容SUMMARY OF THE INVENTION

鉴于背景技术中存在的问题,本发明的目的在于提供一种电芯,所述电芯具有较好的循环性能和存储性能。In view of the problems existing in the background art, the purpose of the present invention is to provide a battery cell with better cycle performance and storage performance.

为了达到上述目的,本发明提供了一种电芯,其包括负极片、正极片以及隔离膜,所述负极片包括负极集流体以及设置在负极集流体的表面且含有负极活性物质的负极膜片,所述正极片包括正极集流体以及设置在正极集流体的表面且含有正极活性物质的正极膜片,所述隔离膜间隔于相邻负极片和正极片之间。所述负极膜片的表面还设置有金属锂层,所述金属锂层的重量为所述负极膜片的总重量的0.5%~5%,单位面积负极容量/单位面积正极容量=1.2~2.1,单位面积负极容量/(单位面积正极容量+单位面积金属锂层容量×80%)≥1.10。In order to achieve the above purpose, the present invention provides a battery cell, which includes a negative electrode sheet, a positive electrode sheet and a separator, the negative electrode sheet includes a negative electrode current collector and a negative electrode membrane sheet disposed on the surface of the negative electrode current collector and containing a negative electrode active material The positive electrode sheet includes a positive electrode current collector and a positive electrode membrane sheet disposed on the surface of the positive electrode current collector and containing a positive electrode active material, and the separator is spaced between adjacent negative electrode sheets and positive electrode sheets. The surface of the negative electrode membrane is also provided with a metal lithium layer, and the weight of the metal lithium layer is 0.5% to 5% of the total weight of the negative electrode membrane, and the capacity of the negative electrode per unit area/the capacity of the positive electrode per unit area=1.2 to 2.1 , the capacity of the negative electrode per unit area/(the capacity of the positive electrode per unit area + the capacity of the metal lithium layer per unit area×80%)≥1.10.

相对于现有技术,本发明的有益效果为:Compared with the prior art, the beneficial effects of the present invention are:

本发明的电芯具有较好的循环性能和存储性能。The battery cell of the invention has better cycle performance and storage performance.

附图说明Description of drawings

图1为实施例1和对比例1的常温循环性能曲线图,其中左侧的曲线表示对比例1,右侧的曲线表示实施例1。FIG. 1 is a graph of the normal temperature cycle performance of Example 1 and Comparative Example 1, wherein the curve on the left side represents Comparative Example 1, and the curve on the right side represents Example 1.

具体实施方式Detailed ways

下面详细说明根据本发明的电芯。The cell according to the present invention will be described in detail below.

根据本发明的电芯包括负极片、正极片以及隔离膜,所述负极片包括负极集流体以及设置在负极集流体的表面且含有负极活性物质的负极膜片,所述正极片包括正极集流体以及设置在正极集流体的表面且含有正极活性物质的正极膜片,所述隔离膜间隔于相邻负极片和正极片之间。所述负极膜片的表面还设置有金属锂层,所述金属锂层的重量为所述负极膜片的总重量的0.5%~5%,单位面积负极容量/单位面积正极容量=1.2~2.1,单位面积负极容量/(单位面积正极容量+单位面积金属锂层容量×80%)≥1.10。The battery cell according to the present invention includes a negative electrode sheet, a positive electrode sheet and a separator, the negative electrode sheet includes a negative electrode current collector and a negative electrode membrane sheet disposed on the surface of the negative electrode current collector and containing a negative electrode active material, the positive electrode sheet includes a positive electrode current collector and a positive electrode membrane that is disposed on the surface of the positive electrode current collector and contains a positive electrode active material, and the separator is spaced between adjacent negative electrode sheets and positive electrode sheets. The surface of the negative electrode membrane is also provided with a metal lithium layer, and the weight of the metal lithium layer is 0.5% to 5% of the total weight of the negative electrode membrane, and the capacity of the negative electrode per unit area/the capacity of the positive electrode per unit area=1.2 to 2.1 , the capacity of the negative electrode per unit area/(the capacity of the positive electrode per unit area + the capacity of the metal lithium layer per unit area×80%)≥1.10.

需要说明的是,本发明的电芯是指尚未经过电解液浸泡的电芯(即注入电解液之前的结构)。本发明的电芯在狭义上可仅包括正极片、隔离膜和负极片,但是本发明的电芯在广义上还可包括其它的结构,例如端子组件、保护壳组件等。It should be noted that the battery cell of the present invention refers to the battery cell that has not been soaked in the electrolyte solution (ie, the structure before the electrolyte solution is injected). In a narrow sense, the battery cell of the present invention may only include a positive electrode sheet, a separator and a negative electrode sheet, but in a broad sense, the battery cell of the present invention may also include other structures, such as terminal assemblies, protective shell assemblies, and the like.

在本发明所述的电芯中,在负极膜片表面设置有占负极膜片总重量的0.5%~5%的金属锂层,并控制单位面积负极容量与单位面积正极容量的比值在1.2~2.1范围内,同时保证单位面积负极容量与单位面积正极容量和单位面积金属锂层容量的80%的总和之比≥1.10,可以有效改善电芯的循环性能和存储性能。负极活性物质提供的空位需要在注液后容纳来自金属锂层中锂离子的嵌入,并在首次充电过程中接收来自正极活性物质的所有锂离子。如果金属锂层的含量过高、负极活性物质含量过少或者正极活性物质含量过多则均会导致无法满足上述关系,导致易在电芯满充过程中发生负极析锂,影响电芯的循环性能和存储性能。In the battery cell of the present invention, a metal lithium layer accounting for 0.5% to 5% of the total weight of the negative electrode film is arranged on the surface of the negative electrode film, and the ratio of the negative electrode capacity per unit area to the positive electrode capacity per unit area is controlled to be 1.2~5%. Within the range of 2.1, while ensuring that the ratio of the negative electrode capacity per unit area to the sum of the positive electrode capacity per unit area and 80% of the metal lithium layer capacity per unit area is greater than or equal to 1.10, the cycle performance and storage performance of the cell can be effectively improved. The vacancies provided by the negative active material are required to accommodate the intercalation of lithium ions from the metallic lithium layer after liquid injection and to receive all lithium ions from the positive active material during the first charging process. If the content of the metal lithium layer is too high, the content of the negative electrode active material is too small, or the positive electrode active material content is too large, the above relationship will not be satisfied, which will lead to the formation of lithium deposition in the negative electrode during the full charging process of the battery, which will affect the cycle of the battery cell. performance and storage performance.

在本发明所述的电芯中,由于负极膜片表面的金属锂层的容量难以被完全发挥出来,因此在进行电芯设计时,按金属锂层容量的80%设计不同的正负极容量,进而得到循环性能和存储性能均较优的电芯。In the battery cell according to the present invention, since the capacity of the metal lithium layer on the surface of the negative electrode membrane is difficult to fully exert, when designing the battery cell, different positive and negative electrode capacities are designed according to 80% of the capacity of the metal lithium layer. , and then a cell with better cycle performance and storage performance is obtained.

在本发明所述的电芯中,注液后电芯内部发生负极嵌锂,负极膜片表面的金属锂层均以嵌锂化合物的形式存在,注液后电芯的开路电压与首周充放电后的电压接近。满充后,负极活性物质有足够的空位接收来自正极活性物质的所有锂离子,并在满放后于负极储存过量的锂离子,因此,在放电截止后,负极依然有5%~97%(相对于正极容量)可在正负极之间穿梭的锂离子,换句话说,电芯首周充放电后的富锂状态为105%~197%(相对于正极容量),因此能有效降低容量损失,提高电芯的循环性能和存储性能。In the battery cell of the present invention, the negative electrode lithium intercalation occurs inside the battery cell after liquid injection, and the metal lithium layer on the surface of the negative electrode membrane exists in the form of a lithium intercalation compound. The voltage after discharge is close. After full charge, the negative electrode active material has enough vacancies to receive all the lithium ions from the positive electrode active material, and stores excess lithium ions in the negative electrode after full discharge. Therefore, after the discharge is terminated, the negative electrode still has 5% to 97% ( Lithium ions that can shuttle between the positive and negative electrodes relative to the positive electrode capacity. In other words, the lithium-rich state of the cell after the first cycle of charge and discharge is 105% to 197% (relative to the positive electrode capacity), so it can effectively reduce the capacity. loss, improve the cycle performance and storage performance of the cell.

在本发明所述的电芯中,负极膜片可设置在负极集流体的其中一个表面上,也可以设置在负极集流体的两个表面上。In the battery cell according to the present invention, the negative electrode membrane can be arranged on one surface of the negative electrode current collector, or can be arranged on both surfaces of the negative electrode current collector.

在本发明所述的电芯中,所述负极活性物质可选自能接受、脱出锂离子的材料。优选地,所述负极活性物质选自碳基材料、硅基材料、锡基材料、钛酸锂中的一种或几种。所述碳基材料可选自天然石墨、人造石墨、软碳、硬碳、中间相碳微球、纳米碳、碳纤维中的一种或几种,硅基材料可选自单质硅、硅氧化合物、硅碳复合物、硅合金中的一种或几种,锡基材料可选自单质锡、锡氧化合物、锡碳复合物、锡合金中的一种或几种。In the battery cell according to the present invention, the negative electrode active material can be selected from materials that can accept and extract lithium ions. Preferably, the negative electrode active material is selected from one or more of carbon-based materials, silicon-based materials, tin-based materials, and lithium titanate. The carbon-based material can be selected from one or more of natural graphite, artificial graphite, soft carbon, hard carbon, mesocarbon microspheres, nano-carbon, and carbon fiber, and the silicon-based material can be selected from elemental silicon, silicon oxide compounds. , one or more of silicon-carbon composites, and silicon alloys, and the tin-based material can be selected from one or more of elemental tin, tin oxide compounds, tin-carbon composites, and tin alloys.

在本发明所述的电芯中,所述负极膜片还包括粘结剂以及可选的导电剂,粘结剂以及导电剂的种类均不受到具体的限制,可根据实际需求进行选择。优选地,所述粘结剂可选自丁苯橡胶乳液(SBR)、羧甲基纤维素钠(CMC)中的一种或几种。所述导电剂可选自导电炭黑、超导炭黑、导电石墨、乙炔黑、科琴黑、石墨烯、碳纳米管中的一种或几种。In the battery cell of the present invention, the negative electrode film further includes a binder and an optional conductive agent, and the types of the binder and the conductive agent are not specifically limited and can be selected according to actual needs. Preferably, the binder can be selected from one or more of styrene-butadiene rubber emulsion (SBR) and sodium carboxymethyl cellulose (CMC). The conductive agent may be selected from one or more of conductive carbon black, superconducting carbon black, conductive graphite, acetylene black, Ketjen black, graphene, and carbon nanotubes.

在本发明所述的电芯中,正极膜片可设置在正极集流体的其中一个表面上,也可以设置在正极集流体的两个表面上。In the battery cell according to the present invention, the positive electrode membrane can be arranged on one surface of the positive electrode current collector, or can be arranged on both surfaces of the positive electrode current collector.

在本发明所述的电芯中,所述正极活性物质可选自能接受、脱出锂离子的材料。优选地,所述正极活性物质可选自锂过渡金属氧化物、锂过渡金属氧化物添加其它过渡金属或非过渡金属或非金属得到的化合物中的一种或几种。具体地,所述正极活性物质可选自锂钴氧化物、锂镍氧化物、锂锰氧化物、锂镍锰氧化物、锂镍钴锰氧化物、锂镍钴铝氧化物、橄榄石结构的含锂磷酸盐中的一种或几种,其中,橄榄石结构的含锂磷酸盐的通式可为LiFe1-x-yMnxM’yPO4,0≤x≤1,0≤y≤0.1,0≤x+y≤1,M’选自除Fe、Mn外的其它过渡金属元素或非过渡金属元素中的一种或几种,M’优选选自Cr、Mg、Ti、Al、Zn、W、Nb、Zr中一种或几种。优选地,橄榄石结构的含锂磷酸盐可为磷酸铁锂、磷酸锰锂以及磷酸锰铁锂。在所述正极活性物质中,橄榄石结构的含锂磷酸盐本身具有较高的结构稳定性,不会像其它正极活性物质在循环过程中出现结构变化而导致容量损失,因此使用橄榄石结构的含锂磷酸盐的电芯的容量衰减主要源自电池内部可穿梭于正负极之间的活性锂离子损失,而本发明的电芯在放电截止后依然有5%~97%(相对于正极容量)可在正负极之间穿梭的锂离子,由此,当正极活性物质包含橄榄石结构的含锂磷酸盐时,可以有效降低电芯的容量损失,大幅提高电芯的循环性能和存储性能。但本发明的正极活性物质不仅限于橄榄石结构的含锂磷酸盐。In the battery cell according to the present invention, the positive electrode active material can be selected from materials that can accept and extract lithium ions. Preferably, the positive active material can be selected from one or more of lithium transition metal oxides, and compounds obtained by adding other transition metals or non-transition metals or non-metals to lithium transition metal oxides. Specifically, the positive active material can be selected from lithium cobalt oxide, lithium nickel oxide, lithium manganese oxide, lithium nickel manganese oxide, lithium nickel cobalt manganese oxide, lithium nickel cobalt aluminum oxide, olivine structure One or more of lithium-containing phosphates, wherein the general formula of the olivine-structured lithium-containing phosphates can be LiFe 1-xy Mn x M' y PO 4 , 0≤x≤1, 0≤y≤0.1 , 0≤x+y≤1, M' is selected from one or more of other transition metal elements or non-transition metal elements except Fe, Mn, M' is preferably selected from Cr, Mg, Ti, Al, Zn , W, Nb, Zr one or more. Preferably, the olivine-structured lithium-containing phosphate may be lithium iron phosphate, lithium manganese phosphate and lithium iron manganese phosphate. Among the cathode active materials, the olivine-structured lithium-containing phosphate itself has high structural stability, and will not cause capacity loss due to structural changes during cycling like other cathode active materials. The capacity attenuation of the battery cell containing lithium phosphate is mainly due to the loss of active lithium ions inside the battery that can shuttle between the positive and negative electrodes, while the battery cell of the present invention still has 5% to 97% (relative to the positive electrode) after the discharge is terminated. capacity) lithium ions that can shuttle between the positive and negative electrodes, thus, when the positive electrode active material contains an olivine-structured lithium-containing phosphate, the capacity loss of the cell can be effectively reduced, and the cycle performance and storage of the cell can be greatly improved. performance. However, the positive electrode active material of the present invention is not limited to the olivine-structured lithium-containing phosphate.

在本发明所述的电芯中,所述正极膜片还包括导电剂以及粘结剂,粘结剂以及导电剂的种类均不受到具体的限制,可根据实际需求进行选择。优选地,所述粘结剂可选自聚偏氟乙烯(PVDF)、聚四氟乙烯、偏氟乙烯-四氟乙烯-丙烯三元共聚物、偏氟乙烯-六氟丙烯-四氟乙烯三元共聚物、四氟乙烯-六氟丙烯共聚物、含氟丙烯酸酯树脂中的一种或几种。所述导电剂可选自导电炭黑、超导炭黑、导电石墨、乙炔黑、科琴黑、石墨烯、碳纳米管中的一种或几种。In the battery cell of the present invention, the positive electrode film further includes a conductive agent and a binder, and the types of the binder and the conductive agent are not specifically limited, and can be selected according to actual needs. Preferably, the binder can be selected from polyvinylidene fluoride (PVDF), polytetrafluoroethylene, vinylidene fluoride-tetrafluoroethylene-propylene terpolymer, vinylidene fluoride-hexafluoropropylene-tetrafluoroethylene terpolymer One or more of tetrafluoroethylene-hexafluoropropylene copolymer and fluorine-containing acrylate resin. The conductive agent may be selected from one or more of conductive carbon black, superconducting carbon black, conductive graphite, acetylene black, Ketjen black, graphene, and carbon nanotubes.

在本发明所述的电芯中,优选地,单位面积负极容量/单位面积正极容量=1.3~2.1。In the battery cell according to the present invention, preferably, the capacity of the negative electrode per unit area/the capacity of the positive electrode per unit area=1.3˜2.1.

在本发明所述的电芯中,优选地,所述金属锂层的重量可为所述负极膜片的总重量的1%~5%。In the battery cell according to the present invention, preferably, the weight of the metal lithium layer may be 1% to 5% of the total weight of the negative electrode membrane.

在本发明所述的电芯中,所述金属锂层的来源及形式不受限制,所述金属锂层的来源可选自锂粉、锂锭、锂片形式中的一种或几种。负极膜片表面的金属锂层也不一定完全密集均匀分布在负极膜片表面。例如当金属锂层的来源是锂粉形式时,负极膜片表面的锂粉颗粒之间可以存在一定的间隙,间隙大小可控制在1μm~5000μm之间;当金属锂层的来源是锂锭或锂片形式时,也可以采用间隙设置的方式使多个锂片(或锂带)间断式的覆盖在负极膜片表面,各锂片(或锂带)之间的间距可控制在1μm~5000μm之间,注入电解液后,经过足够长时间的浸润扩散,富锂区(锂片位置)的锂会向贫锂区(间隙位置)扩散,最终负极膜片中的锂含量仍可达到均匀,实现均匀富锂。In the battery cell of the present invention, the source and form of the metal lithium layer are not limited, and the source of the metal lithium layer can be selected from one or more of the forms of lithium powder, lithium ingot, and lithium flake. The metallic lithium layer on the surface of the negative electrode membrane is not necessarily completely dense and uniformly distributed on the surface of the negative electrode membrane. For example, when the source of the metal lithium layer is in the form of lithium powder, there may be a certain gap between the lithium powder particles on the surface of the negative film, and the size of the gap can be controlled between 1 μm and 5000 μm; when the source of the metal lithium layer is lithium ingot or In the form of lithium sheets, a gap setting method can also be used to make multiple lithium sheets (or lithium strips) intermittently cover the surface of the negative electrode membrane, and the distance between each lithium sheet (or lithium strip) can be controlled within 1μm~5000μm After injecting the electrolyte, after a long enough time of infiltration and diffusion, the lithium in the lithium-rich area (lithium sheet position) will diffuse to the lithium-poor area (interstitial position), and finally the lithium content in the negative film can still reach uniformity. Achieving uniform lithium enrichment.

在本发明所述的电芯中,可采用辊压的方式在所述负极膜片的表面设置金属锂层,利用锂金属与负极活性物质(诸如石墨)的分子间作用力将使金属锂层稳定地固定在负极膜片的表面。In the battery cell of the present invention, a metal lithium layer can be provided on the surface of the negative electrode film by rolling, and the metal lithium layer can be formed by the intermolecular force between lithium metal and negative electrode active material (such as graphite). It is stably fixed on the surface of the negative electrode membrane.

在本发明所述的电芯中,单位面积负极容量=单位面积的负极涂布重量×负极活性物质重量比×负极活性物质的可逆克容量,单位面积正极容量=单位面积的正极涂布重量×正极活性物质重量比×正极活性物质的可逆克容量,金属锂层容量是指金属锂的理论容量。In the battery cell according to the present invention, capacity of negative electrode per unit area = coating weight of negative electrode per unit area × weight ratio of negative electrode active material × reversible gram capacity of negative electrode active material, capacity of positive electrode per unit area = coating weight of positive electrode per unit area × The weight ratio of the positive electrode active material×the reversible gram capacity of the positive electrode active material, and the capacity of the metal lithium layer refers to the theoretical capacity of the metal lithium.

在本发明所述的电芯中,隔离膜的具体种类并不受到具体的限制,可以是现有技术中使用的任何隔离膜材料,例如聚乙烯、聚丙烯、聚偏氟乙烯以及它们的多层复合膜,但不仅限于这些。In the battery core of the present invention, the specific type of the isolation film is not particularly limited, and can be any isolation film material used in the prior art, such as polyethylene, polypropylene, polyvinylidene fluoride and many of them. layer composite films, but not limited to these.

下面结合实施例,进一步阐述本申请。应理解,这些实施例仅用于说明本申请而不用于限制本申请的范围。The present application will be further described below with reference to the embodiments. It should be understood that these examples are only used to illustrate the present application and not to limit the scope of the present application.

实施例1Example 1

(1)正极片的制备(1) Preparation of positive electrode sheet

将正极活性物质磷酸铁锂(可逆克容量为139mAh/g)、导电剂乙炔黑、粘结剂PVDF按重量比94:4:2进行混合,加入溶剂N-甲基吡咯烷酮,充分搅拌混合均匀得到正极浆料,然后涂覆于正极集流体铝箔的两个表面上,其中,正极浆料的涂布重量为0.198g/1540.25mm2(以不包含溶剂的重量计),然后烘干、冷压,得到正极片。The positive active material lithium iron phosphate (reversible gram capacity is 139mAh/g), the conductive agent acetylene black, and the binder PVDF are mixed in a weight ratio of 94:4:2, the solvent N-methylpyrrolidone is added, and the mixture is fully stirred and mixed to obtain The positive electrode slurry is then coated on both surfaces of the positive electrode current collector aluminum foil, wherein the coating weight of the positive electrode slurry is 0.198g/1540.25mm 2 (calculated by weight without solvent), then dried, cold pressed , get the positive electrode.

(2)负极片的制备(2) Preparation of negative electrode sheet

将负极活性物质人造石墨(可逆克容量为340mAh/g)、导电剂乙炔黑、粘结剂SBR+CMC按照重量比95:1.5:3.1:0.4进行混合,加入溶剂去离子水,充分搅拌混合均匀得到负极浆料,然后涂覆于负极集流体铜箔的两个表面上,其中负极浆料的涂布重量为0.120g/1540.25mm2(以不包含溶剂的重量计),经烘干、冷压后得到负极膜片,然后将锂片(理论克容量为3861.3mAh/g)采用辊压的方式复合到负极膜片的表面,其中锂片的重量为3.05mg/1540.25mm2,得到负极片。Mix the negative active material artificial graphite (with a reversible gram capacity of 340mAh/g), the conductive agent acetylene black, and the binder SBR+CMC according to the weight ratio of 95:1.5:3.1:0.4, add the solvent deionized water, fully stir and mix evenly The negative electrode slurry was obtained, and then coated on the two surfaces of the negative electrode current collector copper foil, wherein the coating weight of the negative electrode slurry was 0.120g/1540.25mm 2 (in terms of the weight without solvent), after drying, cooling After pressing, a negative electrode film is obtained, and then the lithium sheet (theoretical gram capacity is 3861.3mAh/g) is compounded to the surface of the negative electrode film by rolling, wherein the weight of the lithium sheet is 3.05mg/1540.25mm 2 , to obtain a negative electrode sheet .

(3)电解液制备(3) Electrolyte preparation

在含水量<10ppm的氩气气氛手套箱中,将碳酸乙烯酯(EC)、碳酸丙烯酯(PC)、碳酸二甲酯(DMC)按照重量比为EC:PC:DMC=3:3:3进行混合后,得到混合有机溶剂,再将充分干燥的锂盐LiPF6溶解于上述混合有机溶剂中,搅拌均匀后,获得电解液,其中LiPF6的浓度为1mol/L。In an argon atmosphere glove box with a water content of <10ppm, ethylene carbonate (EC), propylene carbonate (PC), and dimethyl carbonate (DMC) in a weight ratio of EC:PC:DMC=3:3:3 After mixing, a mixed organic solvent is obtained, and the fully dried lithium salt LiPF 6 is dissolved in the above mixed organic solvent, and after stirring uniformly, an electrolyte solution is obtained, wherein the concentration of LiPF 6 is 1 mol/L.

(4)隔离膜的制备(4) Preparation of separator

以聚乙烯多孔膜作为隔离膜。A polyethylene porous membrane is used as the separator.

(5)锂离子二次电池的制备(5) Preparation of lithium ion secondary battery

将正极片、隔离膜、负极片按顺序叠好,使隔离膜处于正负极中间起到隔离的作用,并卷绕得到电芯。将电芯置于外包装中,注入配好的电解液并封装,获得锂离子二次电池。The positive electrode sheet, the separator and the negative electrode sheet are stacked in sequence, so that the separator is in the middle of the positive electrode and the negative electrode to play a role of isolation, and the battery core is obtained by winding. The battery cell is placed in an outer package, and the prepared electrolyte is injected and packaged to obtain a lithium ion secondary battery.

其中,in,

负极膜片表面的金属锂层的重量百分含量=(3.05mg/1540.25mm2)/(0.120g/1540.25mm2)×100%=2.54%。The weight percentage content of the metallic lithium layer on the surface of the negative electrode membrane=(3.05mg/1540.25mm 2 )/(0.120g/1540.25mm 2 )×100%=2.54%.

单位面积(以面积为1540.25mm2计,以下实施例类似)负极容量=0.120g×95%×340mAh/g=38.76mAh。Negative capacity per unit area (calculated as an area of 1540.25mm 2 , the following examples are similar)=0.120g×95%×340mAh/g=38.76mAh.

单位面积(以面积为1540.25mm2计,以下实施例类似)正极容量=0.198g×94%×139mAh/g=25.87mAh。Unit area (calculated as 1540.25mm 2 in area, similar to the following examples) positive electrode capacity=0.198g×94%×139mAh/g=25.87mAh.

CB值=单位面积负极容量/单位面积正极容量=38.76mAh/25.87mAh=1.50。CB value=negative electrode capacity per unit area/positive electrode capacity per unit area=38.76mAh/25.87mAh=1.50.

单位面积负极容量/(单位面积正极容量+单位面积金属锂层容量×80%)=38.76mAh/(25.87mAh+(3.05mg×3861.3mAh/g)×80%)=1.10。The capacity of negative electrode per unit area/(capacity of positive electrode per unit area+capacity of metal lithium layer per unit area×80%)=38.76mAh/(25.87mAh+(3.05mg×3861.3mAh/g)×80%)=1.10.

锂离子二次电池首周充放电后的富锂状态=[25.87mAh+(3.05mg×3861.3mAh/g)-38.76mAh×8%]/25.87mAh×100%=133.5%。The lithium-rich state of the lithium-ion secondary battery after the first cycle of charge and discharge=[25.87mAh+(3.05mg×3861.3mAh/g)-38.76mAh×8%]/25.87mAh×100%=133.5%.

实施例2Example 2

锂离子二次电池的制备过程同实施例1,区别在于:正极浆料的涂布重量为0.198g/1540.25mm2,负极浆料的涂布重量为0.104g/1540.25mm2,负极膜片表面的锂片的重量为1.52mg/1540.25mm2The preparation process of the lithium ion secondary battery is the same as that of Example 1, except that the coating weight of the positive electrode slurry is 0.198g/1540.25mm 2 , the coating weight of the negative electrode slurry is 0.104g/1540.25mm 2 , and the surface of the negative electrode membrane is 0.104g/1540.25mm 2 . The weight of the lithium sheet is 1.52mg/1540.25mm 2 .

负极膜片表面的金属锂层的重量百分含量=(1.52mg/1540.25mm2)/(0.104g/1540.25mm2)×100%=1.46%。The weight percentage content of the metal lithium layer on the surface of the negative electrode membrane=(1.52mg/1540.25mm 2 )/(0.104g/1540.25mm 2 )×100%=1.46%.

单位面积负极容量=0.104g×95%×340mAh/g=33.59mAh。Negative capacity per unit area=0.104g×95%×340mAh/g=33.59mAh.

单位面积正极容量=0.198g×94%×139mAh/g=25.87mAh。Positive electrode capacity per unit area=0.198g×94%×139mAh/g=25.87mAh.

CB值=单位面积负极容量/单位面积正极容量=33.59mAh/25.87mAh=1.30。CB value=negative electrode capacity per unit area/positive electrode capacity per unit area=33.59mAh/25.87mAh=1.30.

单位面积负极容量/(单位面积正极容量+单位面积金属锂层容量×80%)=33.59mAh/(25.87mAh+(1.52mg×3861.3mAh/g)×80%)=1.10。Negative capacity per unit area/(positive electrode capacity per unit area+capacity of metal lithium layer per unit area×80%)=33.59mAh/(25.87mAh+(1.52mg×3861.3mAh/g)×80%)=1.10.

锂离子二次电池首周充放电后的富锂状态=[25.87mAh+(1.52mg×3861.3mAh/g)-33.59mAh×8%]/25.87mAh×100%=112.3%。The lithium-rich state of the lithium-ion secondary battery after the first cycle of charge and discharge=[25.87mAh+(1.52mg×3861.3mAh/g)-33.59mAh×8%]/25.87mAh×100%=112.3%.

实施例3Example 3

锂离子二次电池的制备过程同实施例1,区别在于:正极浆料的涂布重量0.224g/1540.25mm2,负极浆料的涂布重量0.136g/1540.25mm2,负极膜片表面的锂片的重量为3.45mg/1540.25mm2The preparation process of the lithium ion secondary battery is the same as that of Example 1, except that the coating weight of the positive electrode slurry is 0.224g/1540.25mm 2 , the coating weight of the negative electrode slurry is 0.136g/1540.25mm 2 , the lithium ion on the surface of the negative electrode membrane The weight of the tablet was 3.45 mg/1540.25 mm 2 .

负极膜片表面的金属锂层的重量百分含量=(3.45mg/1540.25mm2)/(0.136g/1540.25mm2)×100%=2.54%。The weight percentage content of the metal lithium layer on the surface of the negative electrode membrane=(3.45mg/1540.25mm 2 )/(0.136g/1540.25mm 2 )×100%=2.54%.

单位面积负极容量=0.136g×95%×340mAh/g=43.93mAh。Negative capacity per unit area=0.136g×95%×340mAh/g=43.93mAh.

单位面积正极容量=0.224g×94%×139mAh/g=29.27mAh。Positive electrode capacity per unit area=0.224g×94%×139mAh/g=29.27mAh.

CB值=单位面积负极容量/单位面积正极容量=43.93mAh/29.27mAh=1.50。CB value=negative electrode capacity per unit area/positive electrode capacity per unit area=43.93mAh/29.27mAh=1.50.

单位面积负极容量/(单位面积正极容量+单位面积金属锂层容量×80%)=43.93mAh/(29.27mAh+(3.45mg×3861.3mAh/g)×80%)=1.10。Negative capacity per unit area/(positive electrode capacity per unit area+capacity of metal lithium layer per unit area×80%)=43.93mAh/(29.27mAh+(3.45mg×3861.3mAh/g)×80%)=1.10.

锂离子二次电池首周充放电后的富锂状态=[29.27mAh+(3.45mg×3861.3mAh/g)-43.93mAh×8%]/29.27mAh×100%=133.5%。The lithium-rich state of the lithium-ion secondary battery after the first cycle of charge and discharge=[29.27mAh+(3.45mg×3861.3mAh/g)-43.93mAh×8%]/29.27mAh×100%=133.5%.

实施例4Example 4

锂离子二次电池的制备过程同实施例1,区别在于:正极浆料的涂布重量为0.259g/1540.25mm2,负极浆料的涂布重量为0.136g/1540.25mm2,负极膜片表面的锂片的重量为1.99mg/1540.25mm2The preparation process of the lithium ion secondary battery is the same as that of Example 1, except that the coating weight of the positive electrode slurry is 0.259g/1540.25mm 2 , the coating weight of the negative electrode slurry is 0.136g/1540.25mm 2 , and the surface of the negative electrode membrane is 0.259g/1540.25mm 2 . The weight of the lithium sheet is 1.99 mg/1540.25 mm 2 .

负极膜片表面的金属锂层的重量百分含量=(1.99mg/1540.25mm2)/(0.136g/1540.25mm2)×100%=1.46%。The weight percentage content of the metallic lithium layer on the surface of the negative electrode membrane=(1.99mg/1540.25mm 2 )/(0.136g/1540.25mm 2 )×100%=1.46%.

单位面积负极容量=0.136g×95%×340mAh/g=43.93mAh。Negative capacity per unit area=0.136g×95%×340mAh/g=43.93mAh.

单位面积正极容量=0.259g×94%×139mAh/g=33.84mAh。Positive electrode capacity per unit area=0.259g×94%×139mAh/g=33.84mAh.

CB值=单位面积负极容量/单位面积正极容量=43.93mAh/33.84mAh=1.30。CB value=negative electrode capacity per unit area/positive electrode capacity per unit area=43.93mAh/33.84mAh=1.30.

单位面积负极容量/(单位面积正极容量+单位面积金属锂层容量×80%)=43.93mAh/(33.84mAh+(1.99mg×3861.3mAh/g)×80%)=1.10。Negative capacity per unit area/(positive capacity per unit area+capacity of metal lithium layer per unit area×80%)=43.93mAh/(33.84mAh+(1.99mg×3861.3mAh/g)×80%)=1.10.

锂离子二次电池首周充放电后的富锂状态=[33.84mAh+(1.99mg×3861.3mAh/g)-43.93mAh×8%]/33.84mAh×100%=112.3%。The lithium-rich state of the lithium-ion secondary battery after the first cycle of charge and discharge=[33.84mAh+(1.99mg×3861.3mAh/g)−43.93mAh×8%]/33.84mAh×100%=112.3%.

实施例5Example 5

锂离子二次电池的制备过程同实施例1,区别在于:正极浆料的涂布重量为0.177g/1540.25mm2,负极浆料的涂布重量0.136g/1540.25mm2,负极膜片表面的锂片的重量为5.44mg/1540.25mm2The preparation process of the lithium ion secondary battery is the same as that of Example 1, except that the coating weight of the positive electrode slurry is 0.177g/1540.25mm 2 , the coating weight of the negative electrode slurry is 0.136g/1540.25mm 2 , and the The weight of the lithium sheet was 5.44 mg/1540.25 mm 2 .

负极膜片表面的金属锂层的重量百分含量=(5.44mg/1540.25mm2)/(0.136g/1540.25mm2)×100%=4.0%。The weight percentage content of the metal lithium layer on the surface of the negative electrode membrane=(5.44mg/1540.25mm 2 )/(0.136g/1540.25mm 2 )×100%=4.0%.

单位面积负极容量=0.136g×95%×340mAh/g=43.93mAh。Negative capacity per unit area=0.136g×95%×340mAh/g=43.93mAh.

单位面积正极容量=0.177×94%×139mAh/g=23.13mAh。Positive electrode capacity per unit area=0.177×94%×139mAh/g=23.13mAh.

CB值=单位面积负极容量/单位面积正极容量=43.93mAh/23.13mAh=1.90。CB value=negative electrode capacity per unit area/positive electrode capacity per unit area=43.93mAh/23.13mAh=1.90.

单位面积负极容量/(单位面积正极容量+单位面积金属锂层容量×80%)=43.93mAh/(23.13mAh+(5.44mg×3861.3mAh/g)×80%)=1.10。Negative capacity per unit area/(positive capacity per unit area+capacity of metal lithium layer per unit area×80%)=43.93mAh/(23.13mAh+(5.44mg×3861.3mAh/g)×80%)=1.10.

锂离子二次电池首周充放电后的富锂状态=[23.13mAh+(5.44mg×3861.3mAh/g)-43.93mAh×8%]/23.13mAh×100%=175.6%。The lithium-rich state of the lithium-ion secondary battery after the first cycle of charge and discharge=[23.13mAh+(5.44mg×3861.3mAh/g)-43.93mAh×8%]/23.13mAh×100%=175.6%.

实施例6Example 6

锂离子二次电池的制备过程同实施例1,区别在于:正极浆料的涂布重量为0.160g/1540.25mm2,负极浆料的涂布重量0.136g/1540.25mm2,负极膜片表面的锂片的重量为6.16mg/1540.25mm2The preparation process of the lithium ion secondary battery is the same as that in Example 1, except that the coating weight of the positive electrode slurry is 0.160g/1540.25mm 2 , the coating weight of the negative electrode slurry is 0.136g/1540.25mm 2 , and the The weight of the lithium sheet was 6.16 mg/1540.25 mm 2 .

负极膜片表面的金属锂层的重量百分含量=(6.16mg/1540.25mm2)/(0.136g/1540.25mm2)×100%=4.53%。The weight percentage content of the metal lithium layer on the surface of the negative electrode membrane=(6.16mg/1540.25mm 2 )/(0.136g/1540.25mm 2 )×100%=4.53%.

单位面积负极容量=0.136g×95%×340mAh/g=43.93mAh。Negative capacity per unit area=0.136g×95%×340mAh/g=43.93mAh.

单位面积正极容量=0.160g×94%×139mAh/g=20.91mAh。Positive electrode capacity per unit area=0.160g×94%×139mAh/g=20.91mAh.

CB值=单位面积负极容量/单位面积正极容量=43.93mAh/20.91mAh=2.10。CB value=negative electrode capacity per unit area/positive electrode capacity per unit area=43.93mAh/20.91mAh=2.10.

单位面积负极容量/(单位面积正极容量+单位面积金属锂层容量×80%)=43.93mAh/(20.91mAh+(6.16mg×3861.3mAh/g)×80%)=1.10。Negative capacity per unit area/(positive capacity per unit area+capacity of metal lithium layer per unit area×80%)=43.93mAh/(20.91mAh+(6.16mg×3861.3mAh/g)×80%)=1.10.

锂离子二次电池首周充放电后的富锂状态=[20.91mAh+(6.16mg×3861.3mAh/g)-43.93mAh×8%]/20.91mAh×100%=197.0%。The lithium-rich state of the lithium-ion secondary battery after the first cycle of charge and discharge=[20.91mAh+(6.16mg×3861.3mAh/g)−43.93mAh×8%]/20.91mAh×100%=197.0%.

实施例7Example 7

锂离子二次电池的制备过程同实施例1,区别在于:正极浆料的涂布重量为0.280g/1540.25mm2,负极浆料的涂布重量为0.136g/1540.25mm2,负极膜片表面的锂片的重量为1.10mg/1540.25mm2The preparation process of the lithium ion secondary battery is the same as that in Example 1, except that the coating weight of the positive electrode slurry is 0.280g/1540.25mm 2 , the coating weight of the negative electrode slurry is 0.136g/1540.25mm 2 , and the surface of the negative electrode membrane is 0.280g/1540.25mm 2 . The weight of the lithium sheet is 1.10 mg/1540.25 mm 2 .

负极膜片表面的金属锂层的重量百分含量=(1.10mg/1540.25mm2)/(0.136g/1540.25mm2)×100%=0.81%。The weight percentage content of the metal lithium layer on the surface of the negative electrode membrane=(1.10mg/1540.25mm 2 )/(0.136g/1540.25mm 2 )×100%=0.81%.

单位面积负极容量=0.136g×95%×340mAh/g=43.93mAh。Negative capacity per unit area=0.136g×95%×340mAh/g=43.93mAh.

单位面积正极容量=0.280g×94%×139mAh/g=36.58mAh。Positive electrode capacity per unit area=0.280g×94%×139mAh/g=36.58mAh.

CB值=单位面积负极容量/单位面积正极容量=43.93mAh/36.58mAh=1.20。CB value=negative electrode capacity per unit area/positive electrode capacity per unit area=43.93mAh/36.58mAh=1.20.

单位面积负极容量/(单位面积正极容量+单位面积金属锂层容量×80%)=43.93mAh/(36.58mAh+(1.10mg×3861.3mAh/g)×80%)=1.10。The capacity of negative electrode per unit area/(capacity of positive electrode per unit area+capacity of metal lithium layer per unit area×80%)=43.93mAh/(36.58mAh+(1.10mg×3861.3mAh/g)×80%)=1.10.

锂离子二次电池首周充放电后的富锂状态=[36.58mAh+(1.10mg×3861.3mAh/g)-43.93mAh×8%]/36.58mAh×100%=102.0%。The lithium-rich state of the lithium-ion secondary battery after the first cycle of charge and discharge=[36.58mAh+(1.10mg×3861.3mAh/g)−43.93mAh×8%]/36.58mAh×100%=102.0%.

对比例1Comparative Example 1

锂离子二次电池的制备过程同实施例1,区别在于:正极浆料的涂布重量为0.198g/1540.25mm2,负极浆料的涂布重量为0.120g/1540.25mm2,负极膜片的表面不设置锂片。The preparation process of the lithium ion secondary battery is the same as that in Example 1, except that the coating weight of the positive electrode slurry is 0.198g/1540.25mm 2 , the coating weight of the negative electrode slurry is 0.120g/1540.25mm 2 , and the Lithium sheets are not provided on the surface.

单位面积负极容量=0.120g×95%×340mAh/g=38.76mAh。Negative capacity per unit area=0.120g×95%×340mAh/g=38.76mAh.

单位面积正极容量=0.198g×94%×139mAh/g=25.87mAh。Positive electrode capacity per unit area=0.198g×94%×139mAh/g=25.87mAh.

CB值=单位面积负极容量/单位面积正极容量=38.76mAh/25.87mAh=1.50。CB value=negative electrode capacity per unit area/positive electrode capacity per unit area=38.76mAh/25.87mAh=1.50.

锂离子二次电池首周充放电后的富锂状态=[25.87mAh-38.76mAh×8%]/25.87mAh×100%=88.0%。The lithium-rich state of the lithium-ion secondary battery after the first cycle of charge and discharge=[25.87mAh-38.76mAh×8%]/25.87mAh×100%=88.0%.

对比例2Comparative Example 2

锂离子二次电池的制备过程同实施例1,区别在于:正极浆料的涂布重量为0.198g/1540.25mm2,负极浆料的涂布重量为0.094g/1540.25mm2,负极膜片的表面不设置锂片。The preparation process of the lithium ion secondary battery is the same as that in Example 1, except that the coating weight of the positive electrode slurry is 0.198g/1540.25mm 2 , the coating weight of the negative electrode slurry is 0.094g/1540.25mm 2 , and the Lithium sheets are not provided on the surface.

单位面积负极容量=0.094g×95%×340mAh/g=30.36mAh。Negative capacity per unit area=0.094g×95%×340mAh/g=30.36mAh.

单位面积正极容量=0.198g×94%×139mAh/g=25.87mAh。Positive electrode capacity per unit area=0.198g×94%×139mAh/g=25.87mAh.

CB值=单位面积负极容量/单位面积正极容量=30.36mAh/25.87mAh=1.17。CB value=negative electrode capacity per unit area/positive electrode capacity per unit area=30.36mAh/25.87mAh=1.17.

锂离子二次电池首周充放电后的富锂状态=[25.87mAh-30.36mAh×8%]/25.87mAh×100%=90.6%。The lithium-rich state of the lithium-ion secondary battery after the first cycle of charge and discharge=[25.87mAh-30.36mAh×8%]/25.87mAh×100%=90.6%.

对比例3Comparative Example 3

锂离子二次电池的制备过程同实施例1,区别在于:正极浆料的涂布重量为0.224g/1540.25mm2,负极浆料的涂布重量为0.136g/1540.25mm2,负极膜片的表面不设置锂片。The preparation process of the lithium ion secondary battery is the same as that of Example 1, except that the coating weight of the positive electrode slurry is 0.224g/1540.25mm 2 , the coating weight of the negative electrode slurry is 0.136g/1540.25mm 2 , and the Lithium sheets are not provided on the surface.

单位面积负极容量=0.136g×95%×340mAh/g=43.93mAh。Negative capacity per unit area=0.136g×95%×340mAh/g=43.93mAh.

单位面积正极容量=0.224g×94%×139mAh/g=29.27mAh。Positive electrode capacity per unit area=0.224g×94%×139mAh/g=29.27mAh.

CB值=单位面积负极容量/单位面积正极容量=43.93mAh/29.27mAh=1.50。CB value=negative electrode capacity per unit area/positive electrode capacity per unit area=43.93mAh/29.27mAh=1.50.

锂离子二次电池首周充放电后的富锂状态=[29.27mAh-43.93mAh×8%]/29.27mAh×100%=88.0%。The lithium-rich state of the lithium-ion secondary battery after the first cycle of charge and discharge=[29.27mAh-43.93mAh×8%]/29.27mAh×100%=88.0%.

对比例4Comparative Example 4

锂离子二次电池的制备过程同实施例1,区别在于:正极浆料的涂布重量为0.287g/1540.25mm2,负极浆料的涂布重量为0.136g/1540.25mm2,负极膜片的表面不设置锂片。The preparation process of the lithium ion secondary battery is the same as that of Example 1, except that the coating weight of the positive electrode slurry is 0.287g/1540.25mm 2 , the coating weight of the negative electrode slurry is 0.136g/1540.25mm 2 , and the Lithium sheets are not provided on the surface.

单位面积负极容量=0.136g×95%×340mAh/g=43.93mAh。Negative capacity per unit area=0.136g×95%×340mAh/g=43.93mAh.

单位面积正极容量=0.287g×94%×139mAh/g=37.50mAh。Positive electrode capacity per unit area=0.287g×94%×139mAh/g=37.50mAh.

CB值=单位面积负极容量/单位面积正极容量=43.93mAh/37.50mAh=1.17。CB value=negative electrode capacity per unit area/positive electrode capacity per unit area=43.93mAh/37.50mAh=1.17.

锂离子二次电池首周充放电后的富锂状态=[37.50mAh-43.93mAh×8%]/37.50mAh×100%=90.6%。The lithium-rich state of the lithium-ion secondary battery after the first cycle of charge and discharge=[37.50mAh-43.93mAh×8%]/37.50mAh×100%=90.6%.

对比例5Comparative Example 5

锂离子二次电池的制备过程同实施例1,区别在于:正极浆料的涂布重量为0.280g/1540.25mm2,负极浆料的涂布重量为0.136g/1540.25mm2,负极膜片表面的锂片的重量为1.99mg/1540.25mm2The preparation process of the lithium ion secondary battery is the same as that in Example 1, except that the coating weight of the positive electrode slurry is 0.280g/1540.25mm 2 , the coating weight of the negative electrode slurry is 0.136g/1540.25mm 2 , and the surface of the negative electrode membrane is 0.280g/1540.25mm 2 . The weight of the lithium sheet is 1.99 mg/1540.25 mm 2 .

负极膜片表面的金属锂层的重量百分含量=(1.99mg/1540.25mm2)/(0.136g/1540.25mm2)×100%=1.46%。The weight percentage content of the metallic lithium layer on the surface of the negative electrode membrane=(1.99mg/1540.25mm 2 )/(0.136g/1540.25mm 2 )×100%=1.46%.

单位面积负极容量=0.136g×95%×340mAh/g=43.93mAh。Negative capacity per unit area=0.136g×95%×340mAh/g=43.93mAh.

单位面积正极容量=0.280g×94%×139mAh/g=36.58mAh。Positive electrode capacity per unit area=0.280g×94%×139mAh/g=36.58mAh.

CB值=单位面积负极容量/单位面积正极容量=43.93mAh/36.58mAh=1.20。CB value=negative electrode capacity per unit area/positive electrode capacity per unit area=43.93mAh/36.58mAh=1.20.

单位面积负极容量/(单位面积正极容量+单位面积金属锂层容量×80%)=43.93mAh/(36.58mAh+(1.99mg×3861.3mAh/g)×80%)=1.03。Negative electrode capacity per unit area/(positive electrode capacity per unit area + metal lithium layer capacity per unit area×80%)=43.93mAh/(36.58mAh+(1.99mg×3861.3mAh/g)×80%)=1.03.

锂离子二次电池首周充放电后的富锂状态=[36.58mAh+(1.99mg×3861.3mAh/g)-43.93mAh×8%]/36.58mAh×100%=111.4%。The lithium-rich state of the lithium-ion secondary battery after the first cycle of charge and discharge=[36.58mAh+(1.99mg×3861.3mAh/g)−43.93mAh×8%]/36.58mAh×100%=111.4%.

接下来说明锂离子二次电池的测试过程。Next, the test procedure of the lithium ion secondary battery will be described.

(1)锂离子二次电池的常温循环性能测试(1) Normal temperature cycle performance test of lithium ion secondary battery

在25℃下,将锂离子二次电池先以1C恒流充电至电压为3.65V,然后以3.65V恒压充电至电流为0.05C,静置5min之后,将锂离子二次电池以1C恒流放电至电压为2.5V,此为一个充放电循环过程,此次的放电容量为首次循环的放电容量。将锂离子二次电池按上述方法进行多次循环充放电测试,直至锂离子二次电池的放电容量衰减至80%,记录锂离子二次电池的循环次数。At 25°C, the lithium-ion secondary battery was first charged with a constant current of 1C to a voltage of 3.65V, and then charged with a constant voltage of 3.65V to a current of 0.05C. After standing for 5 minutes, the lithium-ion secondary battery was charged with a constant current of 1C. The current is discharged to a voltage of 2.5V, which is a charge-discharge cycle process, and the discharge capacity of this time is the discharge capacity of the first cycle. The lithium ion secondary battery is subjected to multiple cycle charge-discharge tests according to the above method, until the discharge capacity of the lithium ion secondary battery decays to 80%, and the cycle times of the lithium ion secondary battery are recorded.

(2)锂离子二次电池的高温循环性能测试(2) High temperature cycle performance test of lithium ion secondary battery

在60℃下,将锂离子二次电池先以1C恒流充电至电压为3.65V,然后以3.65V恒压充电至电流为0.05C,静置5min之后,将锂离子二次电池以1C恒流放电至电压为2.5V,此为一个充放电循环过程,此次的放电容量为首次循环的放电容量。将锂离子二次电池按上述方法进行多次循环充放电测试,检测得到第500次循环的放电容量。At 60°C, the lithium-ion secondary battery was first charged with a constant current of 1C to a voltage of 3.65V, and then charged with a constant voltage of 3.65V to a current of 0.05C. After standing for 5 minutes, the lithium-ion secondary battery was charged with a constant current of 1C. The current is discharged to a voltage of 2.5V, which is a charge-discharge cycle process, and the discharge capacity of this time is the discharge capacity of the first cycle. The lithium-ion secondary battery was subjected to multiple cycle charge-discharge tests according to the above method, and the discharge capacity of the 500th cycle was detected.

锂离子二次电池60℃循环500次后的容量保持率=(第500次循环的放电容量/首次循环的放电容量)×100%。The capacity retention rate of the lithium ion secondary battery after 500 cycles at 60° C.=(discharge capacity at the 500th cycle/discharge capacity at the first cycle)×100%.

(3)锂离子二次电池的存储性能测试(3) Storage performance test of lithium ion secondary battery

首先,在25℃下,将锂离子二次电池以0.5C恒流充电至电压为3.65V,然后以3.65V恒压充电至电流为0.05C,静置5min之后,将锂离子二次电池以0.5C恒流放电至电压为2.5V,此次的放电容量为存储前的放电容量;而后以0.5C的充电电流将锂离子二次电池满充,并于60℃下静置90天,之后取出并置于25℃下静置2小时,再以0.5C恒流放电至电压为2.5V,静置5min之后,以0.5C恒流充电至电压为3.65V,然后以3.65V恒压充电至电流为0.05C,静置5min之后,将锂离子二次电池以0.5C恒流放电至电压为2.5V,此时的放电容量为存储90天后的放电容量。First, at 25°C, the lithium-ion secondary battery was charged at a constant current of 0.5C to a voltage of 3.65V, and then charged at a constant voltage of 3.65V to a current of 0.05C. After standing for 5 minutes, the lithium-ion secondary battery was charged with 0.5C constant current discharge to a voltage of 2.5V, the discharge capacity this time is the discharge capacity before storage; then the lithium ion secondary battery is fully charged with a charging current of 0.5C, and left at 60 ℃ for 90 days, then Take it out and let it stand at 25°C for 2 hours, then discharge it with 0.5C constant current until the voltage is 2.5V, after standing for 5 minutes, charge it with 0.5C constant current until the voltage is 3.65V, and then charge it with 3.65V constant voltage until the voltage is 3.65V. The current was 0.05C, and after standing for 5 minutes, the lithium-ion secondary battery was discharged at a constant current of 0.5C to a voltage of 2.5V, and the discharge capacity at this time was the discharge capacity after 90 days of storage.

锂离子二次电池60℃存储90天后的容量保持率=(存储90天后的放电容量/存储前的放电容量)×100%。The capacity retention rate of the lithium ion secondary battery after storage at 60° C. for 90 days=(discharge capacity after storage for 90 days/discharge capacity before storage)×100%.

表1实施例1-7以及对比例1-5的性能测试结果Table 1 Performance test results of Examples 1-7 and Comparative Examples 1-5

注:表格中单位面积以面积为1540.25mm2计。Note: The unit area in the table is calculated as an area of 1540.25mm 2 .

图1为实施例1和对比例1的常温循环性能曲线图。从图1可以得知,对比例1的锂离子二次电池在常温环境下容量衰减至80%时预期最多可以循环约6000次,而实施例1的锂离子二次电池在循环6000次以后还有90%的可逆放电容量,且容量衰减至80%时预期可以循环约16000次,因此可以满足长寿命电动大巴和大规模储能系统的使用需求。FIG. 1 is a graph showing the normal temperature cycle performance of Example 1 and Comparative Example 1. FIG. It can be seen from Fig. 1 that the lithium ion secondary battery of Comparative Example 1 is expected to be cycled up to about 6000 times when the capacity decays to 80% in the normal temperature environment, while the lithium ion secondary battery of Example 1 can be cycled for 6000 times at most. It has a reversible discharge capacity of 90%, and is expected to be able to cycle about 16,000 times when the capacity decays to 80%, so it can meet the needs of long-life electric buses and large-scale energy storage systems.

从对比例1-2的比较可以得知,在正极容量一定的条件下,增加负极容量对锂离子二次电池循环寿命和存储寿命影响不大。从实施例1-2的比较可以得知,在负极膜片设置金属锂层后,增加负极容量,会显著提高锂离子二次电池的循环寿命和存储寿命,并且随着金属锂层含量的增加,锂离子二次电池的循环寿命和存储寿命得到进一步延长,因此通过调控负极容量和金属锂层的含量可以实现锂离子二次电池循环寿命和存储寿命的定制化。It can be seen from the comparison of Comparative Examples 1-2 that under the condition of a certain positive electrode capacity, increasing the negative electrode capacity has little effect on the cycle life and storage life of the lithium ion secondary battery. From the comparison of Examples 1-2, it can be known that after the negative electrode film is provided with a metal lithium layer, increasing the negative electrode capacity will significantly improve the cycle life and storage life of the lithium ion secondary battery, and with the increase of the metal lithium layer content , the cycle life and storage life of lithium ion secondary batteries are further extended, so by adjusting the negative electrode capacity and the content of the metal lithium layer, the customization of the cycle life and storage life of lithium ion secondary batteries can be realized.

从对比例3-4的比较可以得知,在负极容量一定的条件下,减少正极容量对锂离子二次电池的循环寿命和存储寿命影响不大。从实施例3-7的比较可以得知,在负极膜片设置金属锂层后,降低正极容量,会显著提高锂离子二次电池的循环寿命和存储寿命,并且随着金属锂层含量的增加,锂离子二次电池的循环寿命和存储寿命得到进一步延长,因此通过调控正极容量和金属锂层的含量可以实现锂离子二次电池循环寿命和存储寿命的定制化。From the comparison of Comparative Examples 3-4, it can be known that under the condition of a certain negative electrode capacity, reducing the positive electrode capacity has little effect on the cycle life and storage life of the lithium ion secondary battery. From the comparison of Examples 3-7, it can be known that after the negative electrode membrane is provided with a metal lithium layer, reducing the positive electrode capacity will significantly improve the cycle life and storage life of the lithium ion secondary battery, and with the increase of the metal lithium layer content , the cycle life and storage life of lithium-ion secondary batteries are further extended, so the customization of the cycle life and storage life of lithium-ion secondary batteries can be achieved by adjusting the cathode capacity and the content of the metal lithium layer.

在对比例5中,若单位面积负极容量与单位面积正极容量和单位面积金属锂层容量的80%之和的比值过低,锂离子二次电池的循环性能和存储性能均较差,这是由于该比值过低,会造成首次嵌锂时负极出现析锂,从而导致锂离子二次电池胀气漏液,使锂离子二次电池的循环性能及存储性能变差。In Comparative Example 5, if the ratio of the capacity of the negative electrode per unit area to the sum of the capacity of the positive electrode per unit area and the capacity of the metal lithium layer per unit area is too low, the cycle performance and storage performance of the lithium ion secondary battery are both poor. Because the ratio is too low, lithium precipitation occurs in the negative electrode when lithium is inserted for the first time, which leads to gas and liquid leakage of the lithium ion secondary battery, and deteriorates the cycle performance and storage performance of the lithium ion secondary battery.

Claims (10)

1.一种电芯,包括:1. A cell, comprising: 负极片,包括负极集流体以及设置在负极集流体的表面且含有负极活性物质的负极膜片;A negative electrode sheet, including a negative electrode current collector and a negative electrode membrane sheet disposed on the surface of the negative electrode current collector and containing a negative electrode active material; 正极片,包括正极集流体以及设置在正极集流体的表面且含有正极活性物质的正极膜片;以及A positive electrode sheet, including a positive electrode current collector and a positive electrode diaphragm provided on the surface of the positive electrode current collector and containing a positive electrode active material; and 隔离膜,间隔于相邻负极片和正极片之间;a separator, which is spaced between adjacent negative electrode sheets and positive electrode sheets; 其特征在于,It is characterized in that, 所述负极膜片的表面设置有金属锂层;The surface of the negative electrode membrane is provided with a metallic lithium layer; 所述金属锂层的重量为所述负极膜片的总重量的0.5%~5%;The weight of the metal lithium layer is 0.5% to 5% of the total weight of the negative electrode membrane; 单位面积负极容量/单位面积正极容量=1.2~2.1;Negative capacity per unit area/positive capacity per unit area=1.2~2.1; 单位面积负极容量/(单位面积正极容量+单位面积金属锂层容量×80%)≥1.10。The capacity of the negative electrode per unit area/(the capacity of the positive electrode per unit area + the capacity of the metal lithium layer per unit area×80%)≥1.10. 2.根据权利要求1所述的电芯,其特征在于,所述负极活性物质选自能接受、脱出锂离子的材料。2 . The battery cell according to claim 1 , wherein the negative electrode active material is selected from materials that can accept and extract lithium ions. 3 . 3.根据权利要求2所述的电芯,其特征在于,3. The battery according to claim 2, characterized in that, 所述负极活性物质选自天然石墨、人造石墨、软碳、硬碳、中间相碳微球、纳米碳、碳纤维、单质硅、硅氧化合物、硅碳复合物、硅合金、单质锡、锡氧化合物、锡碳复合物、锡合金、钛酸锂中的一种或几种。The negative active material is selected from natural graphite, artificial graphite, soft carbon, hard carbon, mesocarbon microspheres, nano carbon, carbon fiber, elemental silicon, silicon oxide compound, silicon carbon composite, silicon alloy, elemental tin, tin oxide One or more of compounds, tin-carbon composites, tin alloys, and lithium titanate. 4.根据权利要求1所述的电芯,其特征在于,所述正极活性物质选自能接受、脱出锂离子的材料。4 . The battery cell according to claim 1 , wherein the positive electrode active material is selected from materials that can accept and extract lithium ions. 5 . 5.根据权利要求4所述的电芯,其特征在于,所述正极活性物质选自锂过渡金属氧化物、锂过渡金属氧化物添加其它过渡金属或非过渡金属或非金属得到的化合物中的一种或几种。5. The battery according to claim 4, wherein the positive electrode active material is selected from the group consisting of lithium transition metal oxides, lithium transition metal oxides and compounds obtained by adding other transition metals or non-transition metals or non-metals. one or more. 6.根据权利要求5所述的电芯,其特征在于,所述正极活性物质选自锂钴氧化物、锂镍氧化物、锂锰氧化物、锂镍锰氧化物、锂镍钴锰氧化物、锂镍钴铝氧化物、橄榄石结构的含锂磷酸盐中的一种或几种。6. The battery cell according to claim 5, wherein the positive electrode active material is selected from the group consisting of lithium cobalt oxide, lithium nickel oxide, lithium manganese oxide, lithium nickel manganese oxide, lithium nickel cobalt manganese oxide , one or more of lithium nickel cobalt aluminum oxide and olivine structure lithium-containing phosphate. 7.根据权利要求1所述的电芯,其特征在于,所述金属锂层的重量为所述负极膜片的总重量的1%~5%。7 . The battery according to claim 1 , wherein the weight of the metal lithium layer is 1% to 5% of the total weight of the negative electrode membrane. 8 . 8.根据权利要求1所述的电芯,其特征在于,所述金属锂层的来源选自锂粉、锂锭、锂片形式中的一种或几种。8 . The battery cell according to claim 1 , wherein the source of the metal lithium layer is one or more selected from the group consisting of lithium powder, lithium ingot, and lithium sheet. 9 . 9.根据权利要求1所述的电芯,其特征在于,采用辊压的方式在所述负极膜片的表面设置金属锂层。9 . The battery cell according to claim 1 , wherein a metal lithium layer is provided on the surface of the negative electrode film by means of rolling. 10 . 10.根据权利要求1所述的电芯,其特征在于,10. The battery according to claim 1, characterized in that, 所述负极膜片还包括粘结剂以及可选的导电剂;The negative electrode film also includes a binder and an optional conductive agent; 所述正极膜片还包括导电剂以及粘结剂。The positive electrode film further includes a conductive agent and a binder.
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