WO2023134589A1 - Positive electrode lithium supplementing agent, and preparation method therefor and use thereof - Google Patents

Positive electrode lithium supplementing agent, and preparation method therefor and use thereof Download PDF

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WO2023134589A1
WO2023134589A1 PCT/CN2023/071097 CN2023071097W WO2023134589A1 WO 2023134589 A1 WO2023134589 A1 WO 2023134589A1 CN 2023071097 W CN2023071097 W CN 2023071097W WO 2023134589 A1 WO2023134589 A1 WO 2023134589A1
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positive electrode
lithium
battery
agent
transition metal
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杨阳宇尘
洪响
王玉轲
傅正文
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华为技术有限公司
中国科学院物理研究所
天目湖先进储能技术研究院有限公司
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    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/02Electrodes composed of, or comprising, active material
    • H01M4/62Selection of inactive substances as ingredients for active masses, e.g. binders, fillers
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01BNON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B19/00Selenium; Tellurium; Compounds thereof
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01BNON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B19/00Selenium; Tellurium; Compounds thereof
    • C01B19/002Compounds containing, besides selenium or tellurium, more than one other element, with -O- and -OH not being considered as anions
    • 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
    • H01M4/58Selection of substances as active materials, active masses, active liquids of inorganic compounds other than oxides or hydroxides, e.g. sulfides, selenides, tellurides, halogenides or LiCoFy; of polyanionic structures, e.g. phosphates, silicates or borates
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01PINDEXING SCHEME RELATING TO STRUCTURAL AND PHYSICAL ASPECTS OF SOLID INORGANIC COMPOUNDS
    • C01P2006/00Physical properties of inorganic compounds
    • C01P2006/40Electric properties
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/02Electrodes composed of, or comprising, active material
    • H01M2004/026Electrodes composed of, or comprising, active material characterised by the polarity
    • H01M2004/028Positive electrodes
    • 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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Abstract

The embodiments of the present application provide a positive electrode lithium supplementing agent, comprising a particle body, wherein the particle body comprises a lithium compound of a sulfoselenide of a transition metal, and the average chemical formula of the lithium compound of a sulfoselenide of a transition metal is LixMSySe2-y, where 1 < x ≤ 4, 0 < y < 2, and M represents the transition metal. When active lithium ions are de-intercalated from the positive electrode lithium supplementing agent, the decomposition voltage is low and no gas is produced, a high lithium supplementing capacity can be provided, and the delithiated product does not affect the performance of a positive electrode of a battery. The embodiments of the present application further provide a method for preparing the positive electrode lithium supplementing agent, a positive electrode sheet of a battery, an electrochemical battery, and an electronic device.

Description

正极补锂剂及其制备方法和应用Positive electrode lithium supplement and its preparation method and application
本申请要求于2022年1月12日提交至中国专利局、申请号为202210031227.7、申请名称为“正极补锂剂及其制备方法和应用”的中国专利申请的优先权,其全部内容通过引用结合在本申请中。This application claims the priority of the Chinese patent application with the application number 202210031227.7 and the application title "Positive electrode lithium supplement and its preparation method and application" submitted to the China Patent Office on January 12, 2022, the entire content of which is incorporated by reference in this application.
技术领域technical field
本申请实施例涉及电池技术领域,特别是涉及一种正极补锂剂及其制备方法和应用。The embodiment of the present application relates to the field of battery technology, in particular to a positive electrode lithium supplement and its preparation method and application.
背景技术Background technique
随着经济和科技的发展,便携式电子器件(手机、平板电脑、笔记本电脑等)、无人机、电动汽车等行业都迫切需要具有更高能量密度、更长循环寿命的储能器件。为使锂离子电池这一储能器件达到上述要求,业界通常采取的措施是向锂离子电池体系中预先加入能提供活性锂的补锂剂,以补偿电池首次充电过程中负极对活性锂的不可逆损耗。With the development of economy and technology, industries such as portable electronic devices (mobile phones, tablet computers, notebook computers, etc.), drones, and electric vehicles are in urgent need of energy storage devices with higher energy density and longer cycle life. In order to make lithium-ion batteries, an energy storage device, meet the above requirements, the industry usually takes measures to pre-add lithium-supplementing agents that can provide active lithium to the lithium-ion battery system to compensate for the irreversible effect of the negative electrode on the active lithium during the first charging process of the battery. loss.
目前,为电池补锂的方案主要可以分为正极补锂和负极补锂。负极补锂材料的本身安全隐患大,难以与负极片的制备工艺兼容,阻碍了其商业化应用。而常见的正极补锂材料虽然通常可与正极极片的制备工艺兼容,但仍无法兼顾高补锂容量、低产气、残留物低副作用等要求。At present, the solutions for replenishing lithium for batteries can be mainly divided into positive electrode lithium replenishment and negative electrode lithium replenishment. The negative electrode lithium supplement material itself has great safety hazards, and it is difficult to be compatible with the preparation process of the negative electrode sheet, which hinders its commercial application. Although the common positive electrode lithium supplement materials are usually compatible with the preparation process of the positive electrode sheet, they still cannot meet the requirements of high lithium supplement capacity, low gas production, and low residue side effects.
发明内容Contents of the invention
鉴于此,本申请实施例提供了一种正极补锂剂,其脱锂分解电压低、补锂容量高,且其脱出活性锂离子时不产气,脱锂产物的离子导电率高,不影响电池正极性能的发挥。In view of this, the embodiment of the present application provides a positive electrode lithium supplementing agent, which has a low delithiation decomposition voltage and high lithium supplementation capacity, and does not produce gas when it delithiates active lithium ions, and the ionic conductivity of the delithiated product is high, which does not affect The performance of the positive electrode of the battery.
具体地,本申请实施例第一方面提供了一种正极补锂剂,所述正极补锂剂包括颗粒本体,所述颗粒本体包括过渡金属的硫硒化物的锂化物,所述过渡金属的硫硒化物的锂化物的平均化学式为Li xMS ySe 2-y,其中,1<x≤4,0<y<2,M代表过渡金属。 Specifically, the first aspect of the embodiment of the present application provides a positive electrode lithium supplement agent, the positive electrode lithium supplement agent includes a particle body, the particle body includes a lithiated transition metal sulfur selenide, and the transition metal sulfur selenide The average chemical formula of lithium selenide is Li x MS y Se 2-y , wherein 1<x≤4, 0<y<2, and M represents a transition metal.
该正极补锂剂的导电性好,其脱锂分解电压较低,可在电芯化成阶段分解产生较多的活性锂离子较多(即,实际补锂容量高),能补足电池在首次充电过程中负极对活性锂的不可逆消耗,有利于提升电池的能量密度和循环性能;另外其脱锂时并不产气,脱锂后的固态残留物的离子电导率高,不会增加电芯阻抗,不影响电池的倍率性能发挥。因此,该正极补锂剂能在不影响电池其他性能的情况下,为电池补足活性锂损失,更好地提高电池的能量密度。The positive electrode lithium replenishing agent has good conductivity, its delithiation decomposition voltage is low, and it can be decomposed in the formation stage of the battery cell to produce more active lithium ions (that is, the actual lithium replenishment capacity is high), which can supplement the battery in the first charge. The irreversible consumption of active lithium by the negative electrode in the process is beneficial to improve the energy density and cycle performance of the battery; in addition, it does not produce gas during delithiation, and the solid residue after delithiation has high ion conductivity, which will not increase the cell impedance , does not affect the rate performance of the battery. Therefore, the positive electrode lithium replenishing agent can supplement the loss of active lithium for the battery without affecting other performances of the battery, and better improve the energy density of the battery.
本申请实施方式中,所述颗粒本体包括通式为Li xMS ySe 2-y的化合物,以及M、Li 2S和Li 2Se。其中,M、Li 2S和Li 2Se可通过化合物Li xMS ySe 2-y部分分解得到。不同于简单混合的M、Li 2S和Li 2Se,此时正极补锂剂中的这些物质是紧密结合的,如是纳米级别的接触,它们可在电芯化成阶段脱出锂离子而转变成过渡金属的硫硒化合物,避免像简单混合的M、Li 2S和Li 2Se混合物中Li 2S发生分解产气现象。 In the embodiment of the present application, the particle body includes a compound of the general formula Li x MS y Se 2-y , as well as M, Li 2 S and Li 2 Se. Among them, M, Li 2 S and Li 2 Se can be obtained by partial decomposition of the compound Li x MS y Se 2-y . Different from M, Li 2 S and Li 2 Se that are simply mixed, these substances in the positive lithium replenishing agent are closely combined at this time. If they are in nanometer-level contact, they can release lithium ions during the formation stage of the battery and transform into transition The metal sulfur selenium compound can avoid the decomposition and gas generation of Li 2 S in the simple mixture of M, Li 2 S and Li 2 Se.
本申请一些实施方式中,所述颗粒本体还包括通式为LiMS ySe 2-y的化合物。LiMS ySe 2-y的结构稳定性很高。 In some embodiments of the present application, the particle body further includes a compound having the general formula LiMS y Se 2-y . The structural stability of LiMS y Se 2-y is high.
本申请实施方式中,M可以包括Cr、Ti、V、Co、Fe、Ni、Mn、Nb的一种或多种。In the embodiments of the present application, M may include one or more of Cr, Ti, V, Co, Fe, Ni, Mn, and Nb.
本申请实施方式中,所述颗粒本体的表面还具有包覆层。包覆层的存在可赋予正极补锂剂良好的空气稳定性及加工性能。In the embodiment of the present application, the surface of the particle body also has a coating layer. The presence of the coating layer can endow the positive electrode lithium supplement with good air stability and processability.
本申请实施例第二方面还提供了一种正极补锂剂的制备方法,包括:The second aspect of the embodiment of the present application also provides a preparation method of a positive electrode lithium supplement, including:
将过渡金属源、硫源、硒源混合后进行球磨并烧结,制得过渡金属的硫硒化物;Mixing transition metal sources, sulfur sources, and selenium sources, ball milling and sintering to prepare transition metal sulfoselenides;
对所述过渡金属的硫硒化合物进行锂化,得到正极补锂剂;其中,所述正极补锂剂包括颗粒本体,所述颗粒本体包括过渡金属的硫硒化物的锂化物,所述过渡金属的硫硒化物的锂化物的平均化学式为Li xMS ySe 2-y,其中,1<x≤4,0<y<2,M代表过渡金属。 The sulfoselenide compound of the transition metal is lithiated to obtain a positive electrode lithium supplement; wherein, the positive electrode lithium supplement includes a particle body, and the particle body includes a lithium compound of a transition metal sulfur selenide, and the transition metal The average chemical formula of the lithiated sulfur selenide is Li x MS y Se 2-y , where 1<x≤4, 0<y<2, and M represents a transition metal.
本申请实施例第二方面提供的正极补锂剂的制备方法,工艺简单,高效环保,可大规模化生产。The preparation method of the positive electrode lithium supplement provided in the second aspect of the embodiment of the present application has a simple process, high efficiency and environmental protection, and can be produced on a large scale.
本申请实施例第三方面还提供了一种电池正极极片,所述电池正极极片中含有如本申请实施例第一方面所述的正极补锂剂。含有该正极补锂剂的电极极片可以用来提供能量密度高、循环寿命长的电化学电池。The third aspect of the embodiment of the present application also provides a battery positive pole piece, the battery positive pole piece contains the positive lithium replenishing agent as described in the first aspect of the embodiment of the present application. The electrode sheet containing the positive electrode lithium supplement can be used to provide an electrochemical battery with high energy density and long cycle life.
本申请一些实施方式中,所述电池正极极片包括集流体和设置在所述集流体上的正极材料层,所述正极材料层包括正极活性材料、如本申请实施例第一方面所述的正极补锂剂、以及粘结剂。在该电池正极极片的制作过程中,上述正极补锂剂的引入不会造成形成正极材料层的正极浆料发生果冻化现象,较易涂布得到平整度高的膜层。In some embodiments of the present application, the positive electrode sheet of the battery includes a current collector and a positive electrode material layer disposed on the current collector, and the positive electrode material layer includes a positive electrode active material, as described in the first aspect of the embodiment of the present application. Positive electrode lithium supplement, and binder. In the production process of the positive electrode sheet of the battery, the introduction of the above-mentioned positive electrode lithium supplementing agent will not cause the positive electrode slurry forming the positive electrode material layer to jelly, and it is easier to coat to obtain a film layer with high flatness.
本申请一些实施方式中,所述电池正极极片包括集流体及依次设置在所述集流体上的正极材料层和补锂剂层,其中,所述正极材料层含有正极活性材料、粘结剂和导电剂,所述补锂剂层含有所述正极补锂剂以及粘结剂和导电剂。In some embodiments of the present application, the positive electrode sheet of the battery includes a current collector, a positive electrode material layer and a lithium replenishing agent layer sequentially arranged on the current collector, wherein the positive electrode material layer contains a positive electrode active material, a binder and a conductive agent, the lithium supplementing agent layer contains the positive electrode lithium supplementing agent, a binder and a conductive agent.
本申请实施例第四方面还提供了一种电化学电池,包括正电极、负电极,以及位于所述正电极和所述负电极之间的隔膜和电解液,其中,所述正电极为本申请实施例第三方面所述的电池正极极片。该电化学电池具有高能量密度和长循环寿命。The fourth aspect of the embodiment of the present application also provides an electrochemical cell, including a positive electrode, a negative electrode, a separator and an electrolyte between the positive electrode and the negative electrode, wherein the positive electrode is the The positive electrode sheet of the battery described in the third aspect of the application embodiment. The electrochemical cell has high energy density and long cycle life.
本申请实施例第五方面还提供了一种电子设备,所述电子设备包括如本申请实施例第四方面所述的电化学电池。The fifth aspect of the embodiment of the present application further provides an electronic device, and the electronic device includes the electrochemical cell as described in the fourth aspect of the embodiment of the present application.
该电子设备可以是各种消费类电子产品,如手机、平板电脑、笔记本电脑、智能穿戴产品等,还可以是移动装置,如电动汽车。The electronic equipment may be various consumer electronic products, such as mobile phones, tablet computers, notebook computers, smart wearable products, etc., and may also be mobile devices, such as electric vehicles.
附图说明Description of drawings
图1为本申请实施例中提供的电化学电池的一种结构示意图。Fig. 1 is a schematic structural view of the electrochemical cell provided in the examples of the present application.
图2为本申请一实施方式中提供的电池正极极片的结构示意图。FIG. 2 is a schematic structural view of the positive electrode sheet of the battery provided in an embodiment of the present application.
图3为本申请另一实施方式中提供的电池正极极片的结构示意图。Fig. 3 is a schematic structural diagram of a positive electrode sheet of a battery provided in another embodiment of the present application.
图4为本申请实施例提供的电子设备的一种结构示意图。FIG. 4 is a schematic structural diagram of an electronic device provided by an embodiment of the present application.
图5为本申请实施例提供的电子设备的另一种结构示意图。FIG. 5 is another schematic structural diagram of an electronic device provided by an embodiment of the present application.
图6为本申请实施例1中正极补锂剂Li xCrSSe与其前驱物CrSSe的X射线衍射仪(X-ray diffraction,XRD)表征结果。 Fig. 6 shows the X-ray diffraction (XRD) characterization results of the positive lithium supplement Li x CrSSe and its precursor CrSSe in Example 1 of the present application.
图7为本申请实施例1半电池的首圈充放电曲线。FIG. 7 is the charge-discharge curve of the first cycle of the half-cell in Example 1 of the present application.
图8为对比例1半电池的首圈充放电曲线。Fig. 8 is the charge-discharge curve of the first cycle of the half-cell of Comparative Example 1.
图9为对比例2半电池(即,单纯的LiFePO 4扣式电池)的充放电曲线。 FIG. 9 is the charge-discharge curve of the half-cell of Comparative Example 2 (ie, a simple LiFePO 4 button cell).
图10为实施例2半电池(LiFePO 4与正极补锂剂混搭的扣式电池)的充放电曲线。 Fig. 10 is the charge and discharge curve of the half-cell of Example 2 (a button cell in which LiFePO 4 is mixed with a positive electrode lithium supplement).
具体实施方式Detailed ways
下面结合本申请实施例中的附图对本申请实施例进行描述。Embodiments of the present application are described below with reference to the drawings in the embodiments of the present application.
如图1所示,图1是本申请实施例提供的电化学电池100的结构示意图,该电化学电池100具体可以是锂二次电池。该锂二次电池包括正极101、负极102、隔膜103、电解液104,以及相应的连通辅件和回路。其中,正极101、负极102可以脱嵌活性金属离子(对于锂二次电池来说,活性金属离子为锂离子)而实现能量的存储和释放:在外加电路驱动下,活性金属离子从正极脱出,经过电解液104、隔膜103迁移至负极,实现电池充电;外接用电负载时,活性金属离子从负极脱出、迁移回正极,进行放电过程。As shown in FIG. 1 , FIG. 1 is a schematic structural diagram of an electrochemical cell 100 provided in an embodiment of the present application, and the electrochemical cell 100 may specifically be a lithium secondary battery. The lithium secondary battery includes a positive electrode 101, a negative electrode 102, a separator 103, an electrolyte 104, and corresponding communication accessories and circuits. Among them, the positive electrode 101 and the negative electrode 102 can deintercalate active metal ions (for lithium secondary batteries, the active metal ions are lithium ions) to realize energy storage and release: driven by an external circuit, the active metal ions are extracted from the positive electrode, Migrate to the negative electrode through the electrolyte 104 and the separator 103 to realize battery charging; when an external electrical load is connected, the active metal ions escape from the negative electrode and migrate back to the positive electrode to carry out the discharge process.
锂离子电池中的所有活性锂由正极材料提供。但是,在锂离子电池的首次充电过程中负极表面固态电解质膜(solid electrolyte interphase,SEI膜)的形成及后续充放电循环过程中的其他化学副反应均会消耗活性锂离子,造成电池的可逆容量的损失和能量密度的降低。为提高锂离子电池的能量密度,业界常用的解决方案是向电池正极中加入补锂剂,而常用的正极补锂剂一般包括二元含锂化合物、三元含锂化合物,或者有机锂盐等。其中,Li 2NiO 2、Li 6CoO 4等三元含锂化物的理论补锂容量低,且其补锂后残留物的离子和电子电导率较差,不利于电池倍率性能的发挥。而草酸锂(Li 2C 2O 4)、Li 2C 3O 5等有机锂盐的理论比容量适中,但其突出缺点是分解电压高,实际补锂能力有限。Li 2O、LiF、Li 2S、Li 3N等二元含锂化合物的理论比容量虽高,但由于其自身的电子导电性较差,其分解电压也很高,且它们分解产生的气体会影响电池的循环性能及安全性能。鉴于此,本申请实施例提供了一种能兼顾良好导电性、低分解电压、高补锂容量、脱锂时不产气等性质的正极补锂剂。 All the active lithium in a Li-ion battery is provided by the cathode material. However, during the first charging process of lithium-ion batteries, the formation of solid electrolyte interphase (SEI film) on the surface of the negative electrode and other chemical side reactions in the subsequent charge-discharge cycle will consume active lithium ions, resulting in the reversible capacity of the battery. loss and decrease in energy density. In order to improve the energy density of lithium-ion batteries, a common solution in the industry is to add lithium supplements to the positive electrode of the battery. Commonly used positive lithium supplements generally include binary lithium-containing compounds, ternary lithium-containing compounds, or organic lithium salts, etc. . Among them, Li 2 NiO 2 , Li 6 CoO 4 and other ternary lithium-containing compounds have low theoretical lithium supplement capacity, and the ion and electronic conductivity of the residue after lithium supplement is poor, which is not conducive to the performance of battery rate performance. Lithium oxalate (Li 2 C 2 O 4 ), Li 2 C 3 O 5 and other organolithium salts have moderate theoretical specific capacity, but their prominent disadvantages are high decomposition voltage and limited actual lithium supplementation capacity. Li 2 O, LiF, Li 2 S, Li 3 N and other binary lithium-containing compounds have high theoretical specific capacity, but due to their own poor electronic conductivity, their decomposition voltage is also high, and the gas produced by their decomposition It will affect the cycle performance and safety performance of the battery. In view of this, the embodiment of the present application provides a positive electrode lithium supplement that can take into account the properties of good conductivity, low decomposition voltage, high lithium supplement capacity, and no gas production during delithiation.
具体地,本申请实施例提供的正极补锂剂,该正极补锂剂包括颗粒本体,颗粒本体包括过渡金属的硫硒化物的锂化物,该过渡金属的硫硒化物的锂化物的平均化学式为Li xMS ySe 2-y,其中,1<x≤4,0<y<2,M代表过渡金属。 Specifically, the positive electrode lithium supplement agent provided in the embodiment of the present application, the positive electrode lithium supplement agent includes a particle body, the particle body includes a lithium compound of a transition metal sulfur selenide, and the average chemical formula of the transition metal sulfur selenide lithium compound is Li x MS y Se 2-y , wherein, 1<x≤4, 0<y<2, and M represents a transition metal.
该正极补锂剂的导电性好,其脱锂分解电压较低,可在电芯化成阶段分解产生较多的活性锂离子较多(即,实际补锂容量高),能补足电池在首次充电过程中负极对活性锂的不可逆消耗,有利于提升电池的能量密度和循环性能。另外,该正极补锂剂的脱锂反应式为:Li xMS ySe 2-y-e -→MS ySe 2-y+xLi +。该补锂剂在脱锂时并不产气,也就避免了各种产气问题(如不必增加电池制作过程的排气袋的体积,也避免了常见正极补锂剂脱锂产生的气体会部分溶解在电解液中溶解而增加电解液的副反应程度),且其脱去活性锂后的残留物主要为过渡金属的硫硒化合物MS ySe 2-y,其离子电导率高,不会增加电芯阻抗,不影响电池的倍率性能发挥,也不会增加电解液产气风险。因此,该正极补锂剂能在不影响电池其他性能的情况下,为电池补足活性锂损失,更好地提高电池的能量密度。 The positive electrode lithium replenishing agent has good conductivity, its delithiation decomposition voltage is low, and it can be decomposed in the formation stage of the battery cell to produce more active lithium ions (that is, the actual lithium replenishment capacity is high), which can supplement the battery in the first charge. The irreversible consumption of active lithium by the negative electrode in the process is conducive to improving the energy density and cycle performance of the battery. In addition, the delithiation reaction formula of the cathode lithium supplement is: Li x MS y Se 2-y -e - → MS y Se 2-y +xLi + . The lithium replenishing agent does not produce gas during delithiation, thus avoiding various gas production problems (for example, it is not necessary to increase the volume of the vent bag in the battery manufacturing process, and it also avoids the gas generated by the delithiation of common positive electrode lithium supplements. Partially dissolved in the electrolyte to increase the degree of side reactions in the electrolyte), and the residue after removing the active lithium is mainly the transition metal sulfur selenium compound MS y Se 2-y , which has high ion conductivity and will not Increasing the impedance of the cell will not affect the rate performance of the battery, nor will it increase the risk of electrolyte gas production. Therefore, the positive electrode lithium replenishing agent can supplement the loss of active lithium for the battery without affecting other performances of the battery, and better improve the energy density of the battery.
本申请中,所述颗粒本体中,Li元素和M元素的摩尔比在大于1至4的范围内。即,x的取值范围为:1<x≤4。此时,正极补锂剂的颗粒本体的补锂容量较高。在一些实施方式中,x可以是2、2.5、3、3.5或4等。本申请一些实施方中,y可以是0.2、0.5、1、1.5、1.8等。In the present application, in the particle body, the molar ratio of Li element to M element is in the range of greater than 1-4. That is, the value range of x is: 1<x≤4. At this time, the lithium supplementing capacity of the particle body of the positive electrode lithium supplementing agent is relatively high. In some embodiments, x can be 2, 2.5, 3, 3.5 or 4, etc. In some embodiments of the present application, y may be 0.2, 0.5, 1, 1.5, 1.8, etc.
本申请中,所述颗粒本体可通过对过渡金属的硫硒化物进行锂化得到。本申请一些实施方式中,所述颗粒本体包括通式为Li xMS ySe 2-y的化合物。 In the present application, the particle body can be obtained by lithiation of transition metal sulfoselenide. In some embodiments of the present application, the particle body includes a compound of the general formula Li x MS y Se 2-y .
本申请一些实施方式中,所述颗粒本体包括通式为Li xMS ySe 2-y的化合物,以及M、Li 2S和Li 2Se。其中,M、Li 2S和Li 2Se可通过Li xMS ySe 2-y部分分解得到。本申请中,不管Li xMS ySe 2-y部分分解或者未分解,所述颗粒本体的平均化学式均为Li xMS ySe 2-yIn some embodiments of the present application, the particle body includes a compound of the general formula Li x MS y Se 2-y , and M, Li 2 S and Li 2 Se. Among them, M, Li 2 S and Li 2 Se can be obtained by partial decomposition of Li x MS y Se 2-y . In the present application, regardless of whether Li x MS y Se 2-y is partially decomposed or not decomposed, the average chemical formula of the particle body is Li x MS y Se 2-y .
不同于简单混合的M、Li 2S和Li 2Se,此时正极补锂剂中的这些物质是紧密结合的,例如是纳米级别的接触,M、Li 2S和Li 2Se可在电芯化成阶段脱出锂离子而转变成过渡金属的硫硒化合物,脱锂反应式为:M+Li 2Se+Li 2S-4e -→MS ySe 2-y+4Li +。可见,即使Li xMS ySe 2-y发 生了一定分解,其分解产物仍能再共同经历脱锂反应,且不产气,避免了像Li 2S、或者简单物理混合的M、Li 2S和Li 2Se的混合物中Li 2S发生分解产气的现象,相应地也就避免了Li 2S分解产生的SO 2等气体影响电池的循环及安全性能的问题。 Different from M, Li 2 S and Li 2 Se that are simply mixed, these substances in the positive electrode lithium replenishing agent are closely combined at this time, such as nano-level contacts, M, Li 2 S and Li 2 Se can be used in the battery cell In the formation stage, lithium ions are removed and transformed into sulfur-selenium compounds of transition metals. The delithiation reaction formula is: M+Li 2 Se+Li 2 S-4e - →MS y Se 2-y +4Li + . It can be seen that even if Li x MS y Se 2-y is decomposed to a certain extent, its decomposition products can still undergo the delithiation reaction together without producing gas, avoiding the Li 2 S, or the simple physical mixture of M and Li 2 S In the mixture with Li 2 Se, Li 2 S decomposes to produce gas, and correspondingly avoids the problem that the SO 2 and other gases generated by the decomposition of Li 2 S affect the cycle and safety performance of the battery.
本申请一些实施方式中,所述颗粒本体还包括通式为LiMS ySe 2-y的化合物。化合物LiMS ySe 2-y的结构稳定性很高,也能贡献一定的补锂容量。此时,所述颗粒本体包括通式为Li xMS ySe 2-y的化合物(x≠1),以及M、Li 2S和Li 2Se,还有化合物LiMS ySe 2-y。其中,化合物LiMS ySe 2-y通过Li xMS ySe 2-y的化合物(x≠1)转化而来。 In some embodiments of the present application, the particle body further includes a compound having the general formula LiMS y Se 2-y . The compound LiMS y Se 2-y has high structural stability and can also contribute a certain lithium supplementary capacity. At this time, the particle body includes a compound of the general formula Li x MS y Se 2-y (x≠1), as well as M, Li 2 S and Li 2 Se, and the compound LiMS y Se 2-y . Wherein, the compound LiMS y Se 2-y is transformed by the compound (x≠1) of Li x MS y Se 2-y .
本申请中,M选自过渡金属元素。本申请实施方式中,M可以包括铬Cr、钛Ti、钒V、钴Co、铁Fe、镍Ni、锰Mn、铌Nb的一种或多种,但不限于此。本申请中涉及“多种”的表述时,“多种”是指两种或两种以上。In the present application, M is selected from transition metal elements. In the embodiment of the present application, M may include one or more of chromium Cr, titanium Ti, vanadium V, cobalt Co, iron Fe, nickel Ni, manganese Mn, and niobium Nb, but is not limited thereto. When the expression "multiple" is involved in the present application, "multiple" means two or more.
本申请一些实施方式中,所述颗粒本体的表面还具有掺杂层。该掺杂层可以包括所述颗粒本体的材料,只是在其中引入了掺杂元素。示例性的,该掺杂层可以含有含掺杂元素的Li xMS ySe 2-y化合物。其中,该掺杂元素可以是非金属元素,例如氮N、磷P、碳C、硼B中的一种或多种;还可以是不同于M的过渡金属元素/金属元素,例如钼Mo、钨W、锆Zr、银Ag、铜Cu、锡Sn、锑Sb、铝Al、镁Mg、钙Ca等中的一种或多种;当然还可以是上述两类元素的共掺杂等。掺杂元素的存在可进一步提升化合物Li xMS ySe 2-y的结构稳定性,保证其在空气中的良好稳定性,利于其顺利添加到正极体系中。在一些实施例中,掺杂元素以上述非金属元素为优。 In some embodiments of the present application, the surface of the particle body also has a doping layer. This doping layer may comprise the material of the particle body, but doping elements have been introduced therein. Exemplarily, the doped layer may contain a Li x MS y Se 2-y compound containing a doping element. Wherein, the doping element can be a non-metallic element, such as one or more of nitrogen N, phosphorus P, carbon C, boron B; it can also be a transition metal element/metal element different from M, such as molybdenum Mo, tungsten One or more of W, zirconium Zr, silver Ag, copper Cu, tin Sn, antimony Sb, aluminum Al, magnesium Mg, calcium Ca, etc.; of course, co-doping of the above two types of elements is also possible. The presence of doping elements can further improve the structural stability of the compound Li x MS y Se 2-y , ensure its good stability in air, and facilitate its smooth addition to the positive electrode system. In some embodiments, the doping elements are preferably the above-mentioned non-metallic elements.
本申请一些实施方式中,所述颗粒本体的表面还具有包覆层。其中,包覆层的材质可以是具有离子电导性的材料,这样不会影响后续颗粒本体中活性锂的释放。在一些实施例中,颗粒本体的表面外可依次包括上述掺杂层及包覆层。具体地,包覆层的材质可以包括无机碳材料、有机高分子、惰性氧化物等中的至少一种。包覆层材料在空气中稳定性好、不易再吸水或吸氧等,且碱性不高,具有包覆层的正极补锂剂可具有良好的空气稳定性和加工性能,且在该正极补锂剂的颗粒本体脱锂后,残留的包覆层材料不会增加电池电解液的产气风险。In some embodiments of the present application, the surface of the particle body also has a coating layer. Wherein, the material of the coating layer may be a material with ion conductivity, so that it will not affect the release of active lithium in the subsequent particle body. In some embodiments, the surface of the particle body may include the above-mentioned doped layer and cladding layer in sequence. Specifically, the material of the cladding layer may include at least one of inorganic carbon materials, organic polymers, inert oxides, and the like. The coating layer material has good stability in the air, is not easy to absorb water or oxygen, etc., and is not highly alkaline. The positive electrode lithium supplement agent with the coating layer can have good air stability and processability, and the positive electrode supplement After the particle body of the lithium agent is delithiated, the remaining coating layer material will not increase the risk of gas production in the battery electrolyte.
具体地,对于无机碳材料,可以列举石墨、石墨烯、碳纳米管,碳纤维、炭黑、热解碳等中的一种或多种,但不限于此。对于有机高分子,可以列举聚对二甲苯及其衍生物,聚甲基丙烯酸甲酯(PMMA)等聚丙烯酸酯,聚乙烯(PE)、聚苯乙烯等聚烯烃;对于惰性氧化物,可以列举二氧化硅,第一主族至第三主族金属元素的氧化物(如氧化铝、氧化镁、氧化钡等),非催化活性的过渡金属氧化物(如二氧化钛、氧化锌、氧化锆、氧化锡等)。其中,在包覆层为无机碳材料时,还可提升该正极补锂剂的导电性。绝大多数包覆层可以通过包覆层材料的原料与正极补锂剂混合后进行热处理形成。Specifically, for the inorganic carbon material, one or more of graphite, graphene, carbon nanotube, carbon fiber, carbon black, pyrolytic carbon, etc. can be cited, but not limited thereto. For organic polymers, examples include parylene and its derivatives, polyacrylates such as polymethyl methacrylate (PMMA), polyolefins such as polyethylene (PE), and polystyrene; for inert oxides, examples include Silica, oxides of metal elements from the first main group to the third main group (such as alumina, magnesia, barium oxide, etc.), non-catalytically active transition metal oxides (such as titanium dioxide, zinc oxide, zirconia, tin, etc.). Wherein, when the coating layer is an inorganic carbon material, the conductivity of the positive electrode lithium supplementing agent can also be improved. Most of the cladding layers can be formed by mixing the raw materials of the cladding layer materials with the positive electrode lithium replenishing agent and then performing heat treatment.
本申请实施方式中,包覆层的厚度可以在3nm-1000nm的范围内,例如可在5nm-500nm的范围。包覆层的厚度可根据正极补锂剂的大小来调整,合适的包覆层厚度,既可以保证正极补锂剂具有良好的加工性能,又可避免厚度过厚影响活性锂的及时释放、增加电池阻抗。In the embodiment of the present application, the thickness of the cladding layer may be in the range of 3 nm-1000 nm, for example, may be in the range of 5 nm-500 nm. The thickness of the coating layer can be adjusted according to the size of the positive electrode lithium supplement. The appropriate thickness of the coating layer can not only ensure that the positive electrode lithium supplement has good processing performance, but also avoid the influence of excessive thickness on the timely release and increase of active lithium. battery impedance.
本申请一些实施方式中,包覆层的质量可以占正极补锂剂质量的0.01wt%-10wt%。较低的质量占比使得该包覆层能在提高正极补锂剂具有较好的空气稳定性和加工性能,又不过多降低整体材料的补锂比容量。In some embodiments of the present application, the mass of the coating layer may account for 0.01wt%-10wt% of the mass of the positive electrode lithium supplement. The lower mass ratio enables the coating layer to have better air stability and processability in improving the positive electrode lithium supplementation agent, without reducing the lithium supplementation specific capacity of the overall material too much.
本申请实施例提供的上述正极补锂剂的实际补锂容量高,脱锂不产气,脱锂后残留物也不影响电池正极性能的发挥,能很好地提升电池的能量密度及循环性能等。The above-mentioned positive electrode lithium supplement agent provided in the examples of the present application has a high actual lithium supplement capacity, no gas is produced after delithiation, and the residue after delithiation does not affect the performance of the positive electrode of the battery, which can well improve the energy density and cycle performance of the battery wait.
相应地,本申请实施例还提供了上述正极补锂剂的一种制备方法,该制备方法工艺简单,易于操作,高效环保,可大规模化生产。该制备方法具体可以包括:Correspondingly, the embodiment of the present application also provides a preparation method of the above-mentioned positive electrode lithium supplementing agent, the preparation method is simple in process, easy to operate, efficient and environmentally friendly, and can be produced on a large scale. The preparation method may specifically include:
S01,将过渡金属源、硫源、硒源进行球磨,得到混合料,对所述混合料进行烧结,制得过渡金属的硫硒化物;S01, ball milling a transition metal source, a sulfur source, and a selenium source to obtain a mixture, and sintering the mixture to obtain a transition metal sulfur selenide;
S02,对所述过渡金属的硫硒化合物进行锂化,得到正极补锂剂;其中,所述正极补锂剂包括颗粒本体,所述颗粒本体包括过渡金属的硫硒化物的锂化物,所述过渡金属的硫硒化物的锂化物的平均化学式为Li xMS ySe 2-y,其中,1<x≤4,0<y<2,M代表过渡金属。 S02, performing lithiation on the sulfur selenide compound of the transition metal to obtain a positive electrode lithium supplement; wherein, the positive electrode lithium supplement includes a particle body, and the particle body includes a lithium compound of a transition metal sulfur selenide, and the The average chemical formula of the lithiated transition metal sulfoselenide is Li x MS y Se 2-y , wherein 1<x≤4, 0<y<2, and M represents a transition metal.
步骤S01中,过渡金属源可以是过渡金属的单质、氧化物、氢氧化物、盐等一种或多种;硫源可以是S及碱金属硫化物(如Li 2S、Na 2S、K 2S)中的一种或多种;硒源可以是Se、Li 2Se、Na 2Se、K 2Se中一种或多种。本申请一些实施方式中,所述硫源、硒源中的至少一种包括碱金属的相应化合物,这样可更容易得到补锂剂的前驱体。 In step S01, the transition metal source can be one or more of transition metal simple substance, oxide, hydroxide, salt, etc.; the sulfur source can be S and alkali metal sulfides (such as Li 2 S, Na 2 S, K 2 S); the selenium source can be one or more of Se, Li 2 Se, Na 2 Se, K 2 Se. In some embodiments of the present application, at least one of the sulfur source and the selenium source includes a corresponding compound of an alkali metal, which makes it easier to obtain the precursor of the lithium supplement agent.
所述混合料的配制可以通过将过渡金属源、硫源、硒源混合后进行球磨得到。其中,球磨的转速可以是400-1600r/min,具体可以是500、800、1000、1200或1500r/min。较高的球磨转速利于各原料之间进行晶格重构,便于经烧结得到用于形成补锂剂的前驱体-过渡金属的硫硒化合物。在一些实施方式中,球磨的转速可以是800-1500r/min。其中,球磨的时间可以是5min-300min,具体可以是20min、30min、60min、120min、180min、200min、240min等。另外,球磨过程中的球料比可以在(1-30):1的范围内。较高的球料比可以更好地实现晶格重构。The preparation of the mixture can be obtained by ball milling after mixing the transition metal source, the sulfur source and the selenium source. Wherein, the rotational speed of the ball mill may be 400-1600r/min, specifically 500, 800, 1000, 1200 or 1500r/min. A higher ball milling speed is conducive to the lattice reconstruction between the various raw materials, and facilitates the sintering to obtain the precursor-transition metal sulfur selenide compound for forming lithium supplementation agent. In some embodiments, the rotational speed of the ball mill may be 800-1500 r/min. Wherein, the time of ball milling may be 5 min-300 min, specifically 20 min, 30 min, 60 min, 120 min, 180 min, 200 min, 240 min, etc. In addition, the ball-to-material ratio in the ball milling process can be in the range of (1-30):1. Higher ball-to-material ratio can achieve better lattice reconstruction.
其中,烧结处理可以有助于球磨混合料重新长晶,消除晶格缺陷等。其中,烧结的温度可以是700-1000℃,具体可以是750、800、850、900或950℃等。烧结中的保温时长可以是8h-24h,具体可以是10、12、16、18或20h等。烧结处理可以在惰性气氛下进行,惰性气氛可以是氩气、氦气等。进一步地,由于升温速率过快会在各相之间的界面上产生较大的应力,本申请实施例在烧结处理过程中将升温速率控制在1-5℃/min。Among them, the sintering treatment can help the ball-milled mixture to re-grow crystals and eliminate lattice defects. Wherein, the sintering temperature may be 700-1000° C., specifically 750, 800, 850, 900 or 950° C. and the like. The holding time during sintering can be 8h-24h, specifically 10, 12, 16, 18 or 20h. The sintering treatment can be performed under an inert atmosphere, and the inert atmosphere can be argon, helium or the like. Further, since the temperature increase rate is too fast to generate greater stress on the interface between the phases, in the embodiment of the present application, the temperature increase rate is controlled at 1-5° C./min during the sintering process.
本申请一些实施方式中,上述混合料通过过渡金属单质、硫单质、碱金属硫化物、硒单质混合后球磨得到。进一步地,在碱金属硫化物中的碱金属不为锂(M’不为Li)时,在烧结之后还包括:采用碘单质进行置换反应,以得到过渡金属的硫硒化合物。所涉及到的反应方程式为:In some embodiments of the present application, the above-mentioned mixture is obtained by ball milling after mixing transition metal element, sulfur element, alkali metal sulfide, and selenium element. Further, when the alkali metal in the alkali metal sulfide is not lithium (M' is not Li), after sintering, it also includes: performing a displacement reaction with iodine simple substance to obtain a transition metal sulfur selenide compound. The reaction equations involved are:
1)M’ 2S+(2y-1)S+2(2-y)Se+2M==2M’MS ySe 2-y1) M' 2 S+(2y-1)S+2(2-y)Se+2M==2M'MS y Se 2-y ;
2)2M’MS ySe 2-y+I 2==2MS ySe 2-y+2M’I; 2) 2M'MS y Se 2-y + I 2 == 2MS y Se 2-y + 2M'I;
M’代表碱金属元素。未反应完的碘单质可以通过乙腈、丙酮等溶剂冲洗掉。M' represents an alkali metal element. The unreacted elemental iodine can be washed away by solvents such as acetonitrile and acetone.
步骤S02中,锂化方式包括电化学锂化、有机锂化试剂锂化、金属锂锂化等中的一种或多种。其中,电化学锂化通常是把待锂化的材料压片后与锂源置于电解液中,并通过隔膜隔开,且二者通过外电路进行电连接,在通电时可以实现对待锂化的材料的补锂。其中,锂源一般是自支撑的锂板、镀锂金属片或者附着在其他薄膜基材上的锂箔。而采用有机锂化试剂进行锂化具体可以是将待锂化的材料置于有机锂化试剂中,有机锂化试剂中的锂离子会脱出,并嵌入待锂化的材料中,实现其锂化。而有机锂化试剂一般是芳基锂化试剂,具体可以是萘锂、蒽锂、菲锂、联苯锂等中的一种或多种。而用来锂化的金属锂可以是锂粉、锂箔、熔融锂液等中一种或多种。其中,锂粉、锂箔一般是和待锂化的材料进行压合,熔融锂液一般是与待锂化的材料混合(例如浇铸到待锂化的材料),实现后者的锂化。其中,调节锂化过程的参数(如锂化时间等)可实现对补锂剂的颗粒本体中下标x的调控。In step S02, the lithiation method includes one or more of electrochemical lithiation, organic lithiation reagent lithiation, and metal lithium lithiation. Among them, electrochemical lithiation is usually to put the material to be lithiated into a tablet and place the lithium source in the electrolyte, and separate them through a diaphragm, and the two are electrically connected through an external circuit, and the lithiation to be lithiated can be realized when the power is turned on. Lithium supplementation of materials. Among them, the lithium source is generally a self-supporting lithium plate, a lithium-coated metal sheet, or a lithium foil attached to other thin film substrates. Lithiation using an organic lithiation reagent can specifically be to place the material to be lithiated in an organic lithiation reagent, and the lithium ions in the organic lithiation reagent will come out and be embedded in the material to be lithiated to realize its lithiation. . The organic lithiation reagent is generally an aryl lithiation reagent, specifically one or more of naphthalene lithium, anthracene lithium, phenanthrene lithium, biphenyl lithium, and the like. The metal lithium used for lithiation can be one or more of lithium powder, lithium foil, molten lithium liquid, and the like. Among them, lithium powder and lithium foil are generally pressed together with the material to be lithiated, and molten lithium liquid is generally mixed with the material to be lithiated (for example, cast into the material to be lithiated) to realize the lithiation of the latter. Among them, adjusting the parameters of the lithiation process (such as lithiation time, etc.) can realize the regulation of the subscript x in the particle body of the lithium supplementing agent.
本申请一些实施方式中,还可以对在上述锂化之后,对所得颗粒本体进行一些后处理,例如掺杂、表面包覆等。其中,掺杂、表面包覆通常涉及到热处理。下面以对该颗粒本体进行表面包覆进行示例。在上述步骤S02之后,包括以下步骤S03。In some embodiments of the present application, after the above-mentioned lithiation, some post-processing, such as doping, surface coating, etc., can also be performed on the obtained particle body. Among them, doping and surface coating usually involve heat treatment. The surface coating of the particle body is used as an example below. After the above step S02, the following step S03 is included.
S03,将颗粒本体与包覆层原料混合,以在颗粒本体的表面形成包覆层。S03, mixing the particle body and the raw material for the coating layer to form a coating layer on the surface of the particle body.
其中,包覆层原料可以直接选用包覆层材料,也可以选用合成包覆层材料的各原料。如果选用是合成包覆层材料的各原料,则一般是在正极补锂剂的颗粒本体表面形成包覆层材料的前驱体,还需进行进一步的热处理,以促使其前驱体转化成包覆层材料,及提高与颗粒本体之间的结合力。包覆层的形成方法包括球磨法、机械搅拌法、机械融合法、涂覆法、喷雾干燥法、气相沉积法、热分解法等中的一种或多种。其中,涂覆的方式可以具体包括滴涂、刷涂、喷涂、浸涂、刮涂、旋涂中的一种或多种方式的组合。气相沉积法包括物理气相沉积(如蒸镀沉积、磁控溅射、真空热沉积法等)、化学气相沉积法、原子层沉积法等。包覆层的构建方法可根据具体的材质进行选择。Wherein, the raw material of the cladding layer can be directly selected from the cladding layer material, and can also be selected from various raw materials of the synthetic cladding layer material. If the raw materials for the synthesis of the cladding layer material are selected, the precursor of the cladding layer material is generally formed on the surface of the particle body of the positive electrode lithium supplementing agent, and further heat treatment is required to promote the transformation of the precursor into the cladding layer material, and improve the bonding force with the particle body. The method for forming the coating layer includes one or more of ball milling, mechanical stirring, mechanical fusion, coating, spray drying, vapor deposition, and thermal decomposition. Wherein, the coating method may specifically include one or a combination of drip coating, brush coating, spray coating, dip coating, blade coating, and spin coating. Vapor deposition methods include physical vapor deposition (such as vapor deposition, magnetron sputtering, vacuum thermal deposition, etc.), chemical vapor deposition, atomic layer deposition, and the like. The construction method of the cladding layer can be selected according to the specific material.
包覆层材料如本申请前文所述。其中,石墨、碳纳米管、碳纤维等无机碳材料适合通过球磨法包覆上,在球磨后还可以进行适当的热处理。材质为热解碳的包覆层特别适用通过热分解法构建,具体可以将有机碳源与正极补锂剂混合后(例如是研磨,或者是通入气态碳源)进行热处理,以使有机碳源热分解成无机导电碳层。有机高分子可通过涂覆法、喷雾干燥法等包覆上,部分有机高分子(如聚对二甲苯及其衍生物)较适合通过化学气相沉积的方式构建致密性高、贴敷性好的包覆层。惰性氧化物可通过涂覆法、喷雾干燥法、气相沉积法等包覆上。The cladding material is as described earlier in this application. Among them, inorganic carbon materials such as graphite, carbon nanotubes, and carbon fibers are suitable for coating by ball milling, and appropriate heat treatment can also be performed after ball milling. The cladding layer made of pyrolytic carbon is especially suitable for construction by thermal decomposition. Specifically, the organic carbon source can be mixed with the positive electrode lithium supplement (for example, grinding, or a gaseous carbon source) for heat treatment to make the organic carbon The source heat decomposes into an inorganic conductive carbon layer. Organic polymers can be coated by coating method, spray drying method, etc. Some organic polymers (such as parylene and its derivatives) are more suitable to be constructed by chemical vapor deposition with high density and good adhesion cladding. The inert oxide can be coated by coating method, spray drying method, vapor deposition method, etc.
本申请实施例还提供了一种电池正极极片,该电池正极极片中含有本申请实施例上述的正极补锂剂。该电池正极极片可如图2或图3所示。The embodiment of the present application also provides a battery positive pole piece, the battery positive pole piece contains the above-mentioned positive electrode lithium replenishing agent in the embodiment of the present application. The positive pole piece of the battery may be as shown in FIG. 2 or FIG. 3 .
本申请一些实施方式中,参见图2,该电池正极极片101包括集流体1011和设置在集流体1011上的正极材料层1012’,该正极材料层1012’包括正极活性材料、本申请实施例上述的正极补锂剂,以及粘结剂。在一些实施例中,该正极材料层1012’中还包括导电剂。图2所示的正极极片可以通过将含上述正极补锂剂、正极活性材料、粘结剂及可选的导电剂的正极浆料涂覆在集流体1011上,再经干燥、压制形成。In some embodiments of the present application, referring to FIG. 2, the positive electrode sheet 101 of the battery includes a current collector 1011 and a positive electrode material layer 1012' disposed on the current collector 1011. The positive electrode material layer 1012' includes a positive electrode active material, an embodiment of the present application The above-mentioned positive electrode lithium replenishing agent, and a binder. In some embodiments, the anode material layer 1012' further includes a conductive agent. The positive electrode sheet shown in FIG. 2 can be formed by coating the positive electrode slurry containing the above-mentioned positive electrode lithium supplementing agent, positive electrode active material, binder and optional conductive agent on the current collector 1011, followed by drying and pressing.
其中,正极补锂剂的质量相对于正极补锂剂与正极活性材料的质量之和的质量占比可以为1%-10%。正极补锂剂的适量质量占比可在为正极极片提供足够的活性锂时,又不会降低正极极片的比容量,从而起到保证电池能量密度的有效提高。在一些实施例中,该质量占比具体可以是2%、3%、5%、7.5%、9%等。Wherein, the mass ratio of the mass of the positive lithium supplement to the sum of the mass of the positive lithium supplement and the positive active material may be 1%-10%. The appropriate mass proportion of the positive electrode lithium supplement can provide enough active lithium for the positive electrode sheet without reducing the specific capacity of the positive electrode sheet, thereby ensuring an effective increase in the energy density of the battery. In some embodiments, the mass proportion can be specifically 2%, 3%, 5%, 7.5%, 9% and so on.
图2所示的正极极片中,正极补锂剂的质量占正极材料层1012’的质量的0.5%-15%。该质量占比可以保证通过该电池正极极片101制得的电池在首次充放电及多次非首次充放电过程中均具有较高的容量,从而使该电池具有较高的能量密度和较长循环寿命。在一些实施方式中,该质量占比可以为2%-10%,进一步可以是5%-10%。其中,粘结剂的质量可以占正极材料层1012’的质量的0.5%-10%。导电剂的质量可以占正极材料层1012’的质量的0.5%-10%。In the positive electrode sheet shown in Fig. 2, the mass of the positive electrode lithium supplementing agent accounts for 0.5%-15% of the mass of the positive electrode material layer 1012'. This mass ratio can ensure that the battery made through the positive electrode sheet 101 of the battery has a higher capacity during the first charge and discharge and multiple non-first charge and discharge processes, so that the battery has a higher energy density and a longer battery life. cycle life. In some embodiments, the mass proportion may be 2%-10%, further may be 5%-10%. Wherein, the mass of the binder may account for 0.5%-10% of the mass of the positive electrode material layer 1012'. The mass of the conductive agent may account for 0.5%-10% of the mass of the positive electrode material layer 1012'.
本申请另一些实施方式中,参见图3,该电池正极极片101包括集流体1011及依次设置在集流体1011上的正极材料层1012和补锂剂层1013,其中,正极材料层1012含有正极活性材料及粘结剂和导电剂,补锂剂层1013含有本申请实施例上述的正极补锂剂以及粘结剂和导电剂。In other embodiments of the present application, referring to FIG. 3 , the positive electrode sheet 101 of the battery includes a current collector 1011 and a positive electrode material layer 1012 and a lithium replenishing agent layer 1013 sequentially arranged on the current collector 1011, wherein the positive electrode material layer 1012 contains a positive electrode Active materials, binders, and conductive agents, and the lithium-replenishing agent layer 1013 contain the above-mentioned positive electrode lithium-replenishing agent, binder, and conductive agent in the embodiment of the present application.
图3所示的正极极片可以通过如下步骤制得:先在集流体1011上涂覆常规的正极浆料,干燥后形成正极材料层1012,再在该正极材料层1012上涂覆含正极补锂剂、电剂和粘结剂的浆料干燥后得到补锂剂层1013。也可以理解成,此种实施方式提供的正极极片,相当于现有技术中的正极极片加上位于其表面的补锂剂层1013。如上所述,图3所示的正极极片中,正极补锂剂的质量相对于正极补锂剂与正极活性材料的质量之和的质量占比也可以为 1%-10%。The positive electrode sheet shown in FIG. 3 can be prepared by the following steps: firstly coat the conventional positive electrode slurry on the current collector 1011, dry it to form the positive electrode material layer 1012, and then coat the positive electrode material layer 1012 on the positive electrode material layer 1012. The lithium supplement layer 1013 is obtained after the slurry of the lithium agent, the battery agent and the binder is dried. It can also be understood that the positive electrode sheet provided by this embodiment is equivalent to the positive electrode sheet in the prior art plus the lithium-supplementing agent layer 1013 on its surface. As mentioned above, in the positive electrode sheet shown in FIG. 3 , the mass ratio of the mass of the positive lithium supplement to the sum of the mass of the positive lithium supplement and the positive active material can also be 1%-10%.
上述集流体1011可称为正极集流体,其包括但不仅限于金属箔材、合金箔材或镀金属膜,其表面可被蚀刻处理或粗化处理,以形成次级结构,便于和正极材料层形成有效接触。示例性的金属箔材可以为铝箔、涂炭铝箔或镀铝膜,示例性的合金箔材可以是不锈钢箔、铝合金箔或者涂炭不锈钢箔。The above-mentioned current collector 1011 can be referred to as a positive electrode current collector, which includes but is not limited to metal foil, alloy foil or metallized film, and its surface can be etched or roughened to form a secondary structure, which is convenient for the positive electrode material layer effective contact. Exemplary metal foil materials may be aluminum foil, carbon-coated aluminum foil, or aluminized film, and exemplary alloy foil materials may be stainless steel foil, aluminum alloy foil, or carbon-coated stainless steel foil.
上述正极活性材料、粘结剂、导电剂可以是电池领域的常规选择。其中,正极活性材料可以包括但不限于是磷酸铁锂、磷酸锰锂、磷酸锰铁锂、磷酸钒锂、磷酸钴锂、钴酸锂、锰酸锂、镍锰酸锂、镍钴锰(NCM)、镍钴铝(NCA)等中的至少一种。粘结剂可以具体包括但不限于聚四氟乙烯(PTFE)、聚偏氟乙烯(PVDF)、聚乙烯醇(PVA)、聚丙烯酸(PAA)、聚丙烯酸酯、丁苯橡胶(SBR)、羧甲基纤维素钠(CMC)和海藻酸钠等中的一种或多种。导电剂可以具体包括但不限于乙炔黑、科琴黑、Supper P导电炭黑、石墨、石墨烯、碳纳米管、碳纤维、无定形碳等中的一种或多种。The above-mentioned positive electrode active material, binder, and conductive agent can be conventional choices in the field of batteries. Among them, the positive electrode active material may include but not limited to lithium iron phosphate, lithium manganese phosphate, lithium manganese iron phosphate, lithium vanadium phosphate, lithium cobalt phosphate, lithium cobaltate, lithium manganate, lithium nickel manganate, nickel cobalt manganese (NCM ), nickel cobalt aluminum (NCA), etc. at least one. Binders may specifically include, but are not limited to, polytetrafluoroethylene (PTFE), polyvinylidene fluoride (PVDF), polyvinyl alcohol (PVA), polyacrylic acid (PAA), polyacrylate, styrene-butadiene rubber (SBR), carboxyl One or more of sodium methylcellulose (CMC) and sodium alginate, etc. The conductive agent may specifically include, but not limited to, one or more of acetylene black, Ketjen black, Supper P conductive carbon black, graphite, graphene, carbon nanotubes, carbon fibers, amorphous carbon, and the like.
本申请实施例提供的电池正极极片中,由于带有上述正极补锂剂,该正极极片可用来提供能量密度高、循环寿命长的电化学电池。In the positive pole piece of the battery provided in the embodiment of the present application, since the above-mentioned positive lithium replenishing agent is included, the positive pole piece can be used to provide an electrochemical battery with high energy density and long cycle life.
本申请实施例还提供了一种电化学电池,其包括前述电池正极极片。该电化学电池的结构可如前文图1所述。该电化学电池可以是二次电池,具有高循环性能和高安全性。具体地,该二次电池可以具体为锂二次电池。The embodiment of the present application also provides an electrochemical battery, which includes the above-mentioned positive electrode sheet of the battery. The structure of the electrochemical cell can be as described above in FIG. 1 . The electrochemical battery may be a secondary battery, which has high cycle performance and high safety. Specifically, the secondary battery may be specifically a lithium secondary battery.
其中,负极102可以包括负极集流体和设置在负极集流体上的负极材料层,负极材料层包括负极活性材料、粘结剂和可选的导电剂。其中,负极集流体包括但不仅限于金属箔材、合金箔材或镀金属膜,其表面可被蚀刻处理或粗化处理,以形成次级结构,便于和负极材料层形成有效接触。示例性的金属箔材可以为铜箔、涂炭铜箔或镀铜膜,示例性的合金箔材可以是不锈钢箔、铜合金箔等。负极活性材料包括但不限于钛酸锂、金属锂(锂单质或锂合金)、碳基材料、硅基材料、锡基材料等中的一种或多种。其中,碳基材料可包括石墨(如天然石墨、人造石墨)、非石墨化炭(软碳、硬碳等);硅基材料可包括单质硅、硅基合金、硅氧化物和硅碳复合材料等中的一种或多种;锡基材料可包括单质锡、锡合金等中的一种或多种。隔膜103可以是聚合物隔膜、无纺布等,包括但不限于单层PP(聚丙烯)、单层PE(聚乙烯)、双层PP/PE、双层PP/PP和三层PP/PE/PP等隔膜。电解液104包括锂盐和溶剂,溶剂可包括碳酸酯类溶剂、羧酸酯类溶剂、醚类溶剂中的一种或多种。Wherein, the negative electrode 102 may include a negative electrode current collector and a negative electrode material layer disposed on the negative electrode current collector. The negative electrode material layer includes a negative electrode active material, a binder and an optional conductive agent. Among them, the negative electrode current collector includes but not limited to metal foil, alloy foil or metallized film, and its surface can be etched or roughened to form a secondary structure to facilitate effective contact with the negative electrode material layer. Exemplary metal foil materials may be copper foil, carbon-coated copper foil, or copper-plated film, and exemplary alloy foil materials may be stainless steel foil, copper alloy foil, and the like. The negative electrode active material includes, but is not limited to, one or more of lithium titanate, lithium metal (lithium element or lithium alloy), carbon-based materials, silicon-based materials, tin-based materials, and the like. Among them, carbon-based materials can include graphite (such as natural graphite, artificial graphite), non-graphitized carbon (soft carbon, hard carbon, etc.); silicon-based materials can include elemental silicon, silicon-based alloys, silicon oxides, and silicon-carbon composite materials One or more of them; tin-based materials may include one or more of simple tin, tin alloys, etc. The separator 103 can be a polymer separator, non-woven fabric, etc., including but not limited to single-layer PP (polypropylene), single-layer PE (polyethylene), double-layer PP/PE, double-layer PP/PP and three-layer PP/PE /PP and other diaphragms. The electrolyte solution 104 includes a lithium salt and a solvent, and the solvent may include one or more of carbonate solvents, carboxylate solvents, and ether solvents.
本申请实施例的电化学电池可用于终端消费产品,如手机、平板电脑、移动电源、便携机、笔记本电脑、数码相机以及其它可穿戴电子设备或可移动的电子设备,如无人机、电动自行车、电动汽车等产品,以提高产品的性能。The electrochemical battery of the embodiment of the present application can be used in terminal consumer products, such as mobile phones, tablet computers, mobile power supplies, portable computers, notebook computers, digital cameras, and other wearable electronic devices or mobile electronic devices, such as drones, electric products such as bicycles and electric vehicles to improve the performance of the products.
本申请实施例还提供一种包含有上述电化学电池的电子设备。该电子设备可以是包括各种消费类电子产品,如手机、平板电脑、笔记本电脑、移动电源、便携机、以及其它可穿戴或可移动的电子设备、电视机、影碟机、录像机、摄录机、收音机、收录机、组合音响、电唱机、激光唱机、家庭办公设备、家用电子保健设备以及汽车等电子产品。需要说明的是,当上述电化学电池应用到电子设备中,其可以以电池包的形式容置在电子设备中,通常地,该电池包包括多个电池模组(单个电池模组可以包括多个上述电化学电池)及管控它们的电池管理系统等。The embodiment of the present application also provides an electronic device including the above electrochemical cell. The electronic equipment can include various consumer electronic products, such as mobile phones, tablet computers, notebook computers, mobile power supplies, portable computers, and other wearable or mobile electronic equipment, TV sets, DVD players, video recorders, camcorders , radios, tape recorders, stereos, record players, CD players, home office equipment, home electronic health care equipment and automobiles and other electronic products. It should be noted that when the above-mentioned electrochemical battery is applied to an electronic device, it can be accommodated in the electronic device in the form of a battery pack. Generally, the battery pack includes a plurality of battery modules (a single battery module can include multiple electrochemical cells mentioned above) and the battery management system that manages them.
一些实施方式中,参见图4,本申请实施例提供了一种电子设备200,其包括壳体201和容纳于壳体201内的电子元器件(图4中未示出)和电池202,电池202为电子设备200供电,电池202包括本申请实施例上述的电化学电池100。壳体201可包括组装在终端前侧的 前盖和组装在后侧的后壳,电池202可固定在后壳内侧。图4示出的电子设备通常为体积较小的便携式电子设备,如手机等。In some implementations, referring to FIG. 4 , the embodiment of the present application provides an electronic device 200, which includes a casing 201, electronic components (not shown in FIG. 4 ) contained in the casing 201, and a battery 202. The battery 202 provides power for the electronic device 200, and the battery 202 includes the electrochemical battery 100 described above in the embodiment of the present application. The housing 201 may include a front cover assembled on the front side of the terminal and a rear case assembled on the rear side, and the battery 202 may be fixed inside the rear case. The electronic device shown in FIG. 4 is usually a small portable electronic device, such as a mobile phone.
另一些实施方式中,参见图5,本申请实施例提供了一种电子设备300,其可以是各种用于装载、运输、组装、拆卸、安防等的可移动装置,可以是各种形式的车辆。具体地,该电子设备300可包括车体301、移动组件302、驱动组件,驱动组件包括电机303及电池304,电池304包括本申请实施例提供的上述电化学电池100。其中,移动组件302可以是车轮。电池304可以是包含上述电化学电池100的电池包,其容置在车辆的车体底部,并与电机303电连接,这样电化学电池100可以为电机303供电,电机303提供动力以驱动电子设备300的移动组件302移动。In other implementations, referring to FIG. 5, the embodiment of the present application provides an electronic device 300, which can be a variety of mobile devices for loading, transportation, assembly, disassembly, security, etc., and can be in various forms vehicle. Specifically, the electronic device 300 may include a car body 301 , a moving assembly 302 , and a driving assembly. The driving assembly includes a motor 303 and a battery 304 , and the battery 304 includes the above-mentioned electrochemical battery 100 provided in the embodiment of the present application. Wherein, the moving component 302 may be a wheel. The battery 304 can be a battery pack containing the above-mentioned electrochemical battery 100, which is accommodated at the bottom of the vehicle body and electrically connected to the motor 303, so that the electrochemical battery 100 can supply power to the motor 303, and the motor 303 provides power to drive electronic equipment The movement component 302 of 300 moves.
本申请实施例提供的电子设备通过采用本申请实施例提供的电化学电池为其供电,可以满足各类电子设备对电池高能量密度、长循环寿命的需求,提升电子设备的使用体验和市场竞争力。The electronic device provided in the embodiment of the present application uses the electrochemical battery provided in the embodiment of the present application to supply power for it, which can meet the requirements of various electronic devices for high energy density and long cycle life of the battery, and improve the use experience and market competition of electronic devices force.
下面分多个实施例对本申请实施例进行进一步的说明。The embodiments of the present application will be further described below in terms of multiple embodiments.
实施例1Example 1
一种正极补锂剂的制备,包括:A preparation of a positive electrode lithium supplement, comprising:
(1)补锂剂前驱物制备:(1) Preparation of lithium supplementation agent precursor:
将Na 2S和S、Se、Cr按照1:1:2:2的摩尔比混合,在氩气气氛下进行球磨,其中,球磨转速为600r/min,时间为30min,将球磨后得到的混合料在氩气气氛下进行烧结,其中,烧结温度为800℃,保温时间为10h,之后冷却至室温,得到产物为NaCrSSe; Mix Na 2 S, S, Se, and Cr at a molar ratio of 1:1:2:2, and perform ball milling under an argon atmosphere, wherein the ball milling speed is 600r/min, and the time is 30min. The material is sintered in an argon atmosphere, wherein the sintering temperature is 800°C, the holding time is 10h, and then cooled to room temperature to obtain the product NaCrSSe;
然后将NaCrSSe与I 2按照一定的摩尔比加入乙腈中,在氩气气氛下充分混合反应后,除去未反应的I 2的乙腈溶液,将反应产物用乙腈冲洗,洗去吸附的I 2单质,真空干燥后得到前驱物CrSSe。 Then add NaCrSSe and I2 into acetonitrile according to a certain molar ratio, and after fully mixing and reacting under an argon atmosphere, remove the unreacted I2 acetonitrile solution, rinse the reaction product with acetonitrile, and wash away the adsorbed I2 simple substance, The precursor CrSSe was obtained after vacuum drying.
上述涉及到的化学反应式为:Na 2S+S+2Se+2Cr=2NaCrSSe;2NaCrSSe+I 2=2CrSSe+2NaI。 The chemical reaction formula involved above is: Na 2 S+S+2Se+2Cr=2NaCrSSe; 2NaCrSSe+I 2 =2CrSSe+2NaI.
(2)锂化:(2) Lithiation:
将上述CrSSe粉体加入到浓度为0.1M的联苯锂的乙二醇二甲醚溶液中,进行锂化反应20min,得到锂化后的产物,之后离心分离出该锂化产物,并采用溶剂反复清洗,即可得到该正极补锂剂,该正极补锂剂的颗粒本体的平均化学式为Li 3.5CrSSe,具体包括以下物质:Li 3.5CrSSe及LiCrSSe、Li 2S、Li 2Se和Cr。 Add the above-mentioned CrSSe powder into the ethylene glycol dimethyl ether solution of biphenyllithium with a concentration of 0.1M, carry out the lithiation reaction for 20 minutes, and obtain the lithiated product, and then centrifuge the lithiated product, and use a solvent After repeated cleaning, the positive lithium supplement agent can be obtained. The average chemical formula of the particle body of the positive electrode lithium supplement agent is Li 3.5 CrSSe, which specifically includes the following substances: Li 3.5 CrSSe and LiCrSSe, Li 2 S, Li 2 Se and Cr.
一种锂离子半电池的制备,包括:A preparation of a lithium-ion half battery, comprising:
1)制备电池正极极片:1) Preparation of battery positive pole piece:
将上述正极补锂剂、粘结剂-聚偏氟乙烯(PVDF)、导电剂-乙炔黑按照8:1:1的重量比加入到N-甲基吡咯烷酮(NMP)中,搅拌均匀,得到正极浆料;将该正极浆料涂布在正极集流体铝箔上,经烘干、辊压、裁切后得到正极极片;Add the above-mentioned positive electrode lithium replenishing agent, binder-polyvinylidene fluoride (PVDF), conductive agent-acetylene black into N-methylpyrrolidone (NMP) according to the weight ratio of 8:1:1, and stir evenly to obtain the positive electrode Slurry: coating the positive electrode slurry on the aluminum foil of the positive electrode current collector, drying, rolling, and cutting to obtain the positive electrode sheet;
2)电池组装:以上述正极极片为正极,以金属锂片为负极、隔膜为celgard2400,电解液采用1mol/L LiPF 6的碳酸乙烯酯(EC)、碳酸甲乙酯(EMC)和碳酸二甲酯(DMC)的混合溶液;在充满氩气的手套箱中进行组装,得到锂离子半电池。 2) Battery assembly: use the above-mentioned positive pole piece as the positive pole, the lithium metal sheet as the negative pole, the diaphragm as celgard2400, and the electrolyte as ethylene carbonate (EC), ethyl methyl carbonate (EMC) and dicarbonate of 1mol/L LiPF 6 A mixed solution of methyl ester (DMC); assembled in an argon-filled glove box to obtain a lithium-ion half-cell.
对实施例1的半电池进行第一次充电的起始电压为开路电压(Open Circuit Voltage,OCV),约为1.3V,恒流充电(40mA/g),充电截止电压为4.2V;第一次放电的起始电压为4.2V,恒流充电(40mA/g),放电截止电压为2.5V。The half battery of embodiment 1 is carried out the starting voltage of charging for the first time to be open circuit voltage (Open Circuit Voltage, OCV), about 1.3V, constant current charging (40mA/g), charging cut-off voltage is 4.2V; The initial voltage of the first discharge is 4.2V, the constant current charge (40mA/g), the discharge cut-off voltage is 2.5V.
实施例2Example 2
一种锂离子半电池的制备,包括:A preparation of a lithium-ion half battery, comprising:
正极极片制作:将正极活性材料-磷酸铁锂(LiFePO 4)、实施例1制得的正极补锂剂、粘结剂-聚偏氟乙烯(PVDF)、导电剂-乙炔黑按照74:6:10:10的重量比加入到N-甲基吡咯烷酮(NMP)中,搅拌均匀,得到正极浆料;将该正极浆料涂布在正极集流体铝箔上,经烘干、辊压、裁切后得到正极极片; Positive electrode sheet production: the positive electrode active material-lithium iron phosphate (LiFePO 4 ), the positive electrode lithium supplement prepared in Example 1, the binder-polyvinylidene fluoride (PVDF), the conductive agent-acetylene black according to the ratio of 74:6 : Add the weight ratio of 10:10 into N-methylpyrrolidone (NMP), stir evenly to obtain the positive electrode slurry; coat the positive electrode slurry on the positive electrode current collector aluminum foil, dry, roll, and cut Afterwards, the positive electrode sheet is obtained;
根据实施例1记载的半电池制作方法,将上述正极极片组装成锂离子半电池。According to the half-cell fabrication method described in Example 1, the above-mentioned positive pole piece was assembled into a lithium-ion half-cell.
对实施例2的半电池进行充放电循环测试,其中,充电起始电压为OCV,约为2.3V,0.1C恒流充电,充电截止电压为4.2V;放电时的起始电压为4.2V,0.1C恒流充电,截止电压为2.7V。Carry out charge-discharge cycle test to the half-battery of embodiment 2, wherein, charging initial voltage is OCV, is about 2.3V, 0.1C constant current charging, charging cut-off voltage is 4.2V; The initial voltage when discharging is 4.2V, 0.1C constant current charging, the cut-off voltage is 2.7V.
为突出本申请的有益效果,设置对比例1和2。In order to highlight the beneficial effects of the present application, comparative examples 1 and 2 are provided.
对比例1Comparative example 1
将实施例1制备的补锂剂前驱物CrSSe代替正极补锂剂,根据实施例1记载的方法制作正极极片、半电池,并根据实施例1的测试条件对对比例1的半电池进行首次充电和放电。The precursor of the lithium-supplementing agent CrSSe prepared in Example 1 was used to replace the positive electrode lithium-supplementing agent, and the positive electrode sheet and the half-cell were fabricated according to the method described in Example 1, and the half-cell of Comparative Example 1 was tested for the first time according to the test conditions of Example 1. charging and discharging.
对比例2Comparative example 2
一种锂离子半电池,其与实施例2的区别在于:不引入正极补锂剂,且正极活性材料、粘结剂、导电剂的重量比为80:10:10。根据实施例2的测试条件对对比例2的半电池进行充放电循环测试。A lithium-ion half-battery, which differs from Example 2 in that no positive electrode lithium supplement is introduced, and the weight ratio of positive electrode active material, binder, and conductive agent is 80:10:10. According to the test conditions of Example 2, the half-cell of Comparative Example 2 was subjected to a charge-discharge cycle test.
图6为本申请实施例1中正极补锂剂的颗粒本体-Li 3.5CrSSe与其前驱物CrSSe的X射线衍射仪(X-ray diffraction,XRD)表征结果。从图6可以看出,前驱物CrSSe在锂化后,其晶体结构发生明显改变,CrSSe的特征峰消失,锂化后所得补锂剂中,能够观察到Cr、Li 2S、Li 2Se、LiCrSSe特征峰,说明部分Li 3.5CrSSe分解,该补锂剂含有Cr、Li 2S、Li 2Se及LiCrSSe。 Fig. 6 is an X-ray diffraction (XRD) characterization result of the particle body of the positive electrode lithium supplementing agent in Example 1 of the present application - Li 3.5 CrSSe and its precursor CrSSe. It can be seen from Figure 6 that the crystal structure of the precursor CrSSe changed significantly after lithiation, and the characteristic peaks of CrSSe disappeared. In the lithium supplementary agent obtained after lithiation, Cr, Li 2 S, Li 2 Se, The characteristic peak of LiCrSSe indicates that part of Li 3.5 CrSSe is decomposed, and the lithium supplement contains Cr, Li 2 S, Li 2 Se and LiCrSSe.
图7、图8分别是实施例1半电池、对比例1半电池的首圈充放电曲线。可以看出,实施例1平均化学式为Li 3.5CrSSe的补锂剂在4.2V的充电截止电压下表现出较高的脱锂容量(>460mAh/g),其嵌锂容量较低,小于40mAh/g,可忽略不计。由此可算得该补锂剂能提供的补锂容量(即,不可逆容量)>420mAh/g;而对比例1所用的锂化前的CrSSe,其脱锂容量可忽略(<15mAh/g),说明锂化后的Li 3.5CrSSe作为补锂添加剂能在电池的正常工作电位范围内具有较高的补锂容量。 Fig. 7 and Fig. 8 are the first cycle charge and discharge curves of the half-cell of Example 1 and the half-cell of Comparative Example 1, respectively. It can be seen that the lithium supplementing agent whose average chemical formula is Li 3.5 CrSSe in Example 1 shows a higher delithiation capacity (>460mAh/g) at a charge cut-off voltage of 4.2V, and its lithium intercalation capacity is lower, less than 40mAh/g. g, can be ignored. It can be calculated that the lithium supplementing agent can provide a lithium supplementation capacity (i.e., irreversible capacity)>420mAh/g; while the CrSSe before lithiation used in Comparative Example 1 has a negligible delithiation capacity (<15mAh/g), It shows that the lithiated Li 3.5 CrSSe as a lithium supplement additive can have a high lithium supplement capacity within the normal working potential range of the battery.
图9为对比例2半电池(即,单纯的LiFePO 4扣式电池)的充放电曲线,图10为实施例2半电池(LiFePO 4与正极补锂剂混搭的扣式电池)的充放电曲线,图9和图10中的虚线代表第一次充放电循环。从图9-图10可以获知,对比例2中LiFePO 4正极的首次充电比容量仅为160mAh/g,而添加一定补锂剂后的LiFePO 4正极的首次充电比容量高达199.6mAh/g,这表明实施例1的补锂剂实际发挥的补锂容量在450mAh/g以上。另外,在后续的充放电循环中,实施例2的半电池与对比例2半电池的充放电曲线基本一致,且实施例2电池的比容量更稳定些,这表明,本申请提供的正极补锂剂起到了良好的补锂作用,且对电池循环性能没有副作用。 Figure 9 is the charge-discharge curve of the half-cell of Comparative Example 2 (i.e., a simple LiFePO4 button cell), and Figure 10 is the charge-discharge curve of the half-cell of Example 2 (a coin cell in which LiFePO4 is mixed with positive lithium supplements) , The dotted line in Figure 9 and Figure 10 represents the first charge-discharge cycle. It can be seen from Figures 9-10 that the first charge specific capacity of the LiFePO 4 positive electrode in Comparative Example 2 is only 160mAh/g, while the first charge specific capacity of the LiFePO 4 positive electrode after adding a certain lithium supplement is as high as 199.6mAh/g, which is It shows that the actual lithium supplement capacity of the lithium supplement agent of Example 1 is above 450mAh/g. In addition, in the subsequent charge-discharge cycles, the charge-discharge curves of the half-battery of Example 2 and the half-cell of Comparative Example 2 are basically the same, and the specific capacity of the battery of Example 2 is more stable, which shows that the positive electrode supplement provided by the present application The lithium agent plays a good role in lithium supplementation, and has no side effects on the battery cycle performance.
实施例3Example 3
一种正极补锂剂的制备方法,包括:A preparation method of a positive electrode lithium supplement, comprising:
(1)补锂剂前驱物制备:(1) Preparation of lithium supplementation agent precursor:
将Li 2S和S、Se、Cr按照1:1:2:2的摩尔比混合,在氩气气氛下进行球磨,其中,球磨转速为800r/min,时间为30min,将球磨后得到的混合料真空密封后在氩气气氛下进行烧结,其中,烧结温度为900℃,保温时间为10h,之后冷却至室温,得到产物为LiCrSSe; Mix Li 2 S, S, Se, and Cr at a molar ratio of 1:1:2:2, and perform ball milling under an argon atmosphere. The ball milling speed is 800r/min, and the time is 30min. The material was vacuum-sealed and sintered under an argon atmosphere, wherein the sintering temperature was 900°C, the holding time was 10h, and then cooled to room temperature to obtain the product LiCrSSe;
(2)锂化:(2) Lithiation:
将上述LiCrSSe粉体加入到浓度为0.1M的萘锂的乙二醇二甲醚溶液中,进行锂化反应10min,得到锂化后的产物,之后离心分离出该产物,并采用溶剂反复清洗,即可得到该正极补锂剂,该正极补锂剂的平均化学式为Li 2.5CrSSe。 The above LiCrSSe powder was added to the ethylene glycol dimethyl ether solution of lithium naphthalene with a concentration of 0.1M, and the lithiation reaction was carried out for 10 minutes to obtain the lithiated product, which was then centrifuged and washed repeatedly with a solvent. The positive electrode lithium supplement can be obtained, and the average chemical formula of the positive electrode lithium supplement is Li 2.5 CrSSe.
实施例4Example 4
一种正极补锂剂的制备方法,包括:A preparation method of a positive electrode lithium supplement, comprising:
(1)补锂剂前驱物制备:(1) Preparation of lithium supplementation agent precursor:
将Na 2S和S、Se、Co按照1:1:2:2的摩尔比混合,在氩气气氛下进行球磨,其中,球磨转速为600r/min,时间为30min,将球磨后得到的混合料在氩气气氛下进行烧结,其中,烧结温度为800℃,保温时间为10h,之后冷却至室温,得到产物为NaCoSSe; Mix Na 2 S, S, Se, and Co in a molar ratio of 1:1:2:2, and perform ball milling under an argon atmosphere. The ball milling speed is 600r/min, and the time is 30min. The material is sintered in an argon atmosphere, wherein the sintering temperature is 800°C, the holding time is 10h, and then cooled to room temperature, and the obtained product is NaCoSSe;
然后将NaCoSSe与I 2按照一定的摩尔比加入乙腈中,在氩气气氛下充分混合反应后,除去未反应的I 2的乙腈溶液,将反应产物用乙腈冲洗,洗去吸附的I 2单质,真空干燥后得到前驱物CoSSe。 Then NaCoSSe and I2 were added into acetonitrile according to a certain molar ratio, and after fully mixing and reacting under an argon atmosphere, the unreacted I2 acetonitrile solution was removed, and the reaction product was washed with acetonitrile to wash away the adsorbed I2 simple substance, The precursor CoSSe was obtained after vacuum drying.
(2)锂化:(2) Lithiation:
将上述CoSSe粉体加入到浓度为0.1M的联苯锂的乙二醇二甲醚溶液中,进行锂化反应15min,得到锂化后的产物,之后离心分离出该产物,并采用溶剂反复清洗,即可得到正极补锂剂,其平均化学式为Li 3CoSSe。 Add the above CoSSe powder into the ethylene glycol dimethyl ether solution of biphenyllithium with a concentration of 0.1M, carry out the lithiation reaction for 15 minutes, and obtain the lithiated product, and then centrifuge the product, and wash it repeatedly with a solvent , the positive lithium supplement agent can be obtained, and its average chemical formula is Li 3 CoSSe.
实施例5Example 5
一种正极补锂剂的制备方法,包括:A preparation method of a positive electrode lithium supplement, comprising:
(1)补锂剂前驱物制备:(1) Preparation of lithium supplementation agent precursor:
将Na 2S和S、Se、Ti按照1:1:2:2的摩尔比混合,在氩气气氛下进行球磨,其中,球磨转速为600r/min,时间为30min,将球磨后得到的混合料在氩气气氛下进行烧结,其中,烧结温度为900℃,保温时间为10h,之后冷却至室温,得到产物为NaTiSSe; Mix Na 2 S, S, Se, and Ti in a molar ratio of 1:1:2:2, and perform ball milling under an argon atmosphere. The ball milling speed is 600r/min, and the time is 30min. The material is sintered in an argon atmosphere, wherein the sintering temperature is 900°C, the holding time is 10h, and then cooled to room temperature, and the obtained product is NaTiSSe;
然后将NaTiSSe与I 2按照一定的摩尔比加入乙腈中,在氩气气氛下充分混合反应后,除去未反应的I 2的乙腈溶液,将反应产物用乙腈冲洗,洗去吸附的I 2单质,真空干燥后得到前驱物TiSSe。 Then add NaTiSSe and I2 into acetonitrile according to a certain molar ratio, and after fully mixing and reacting under an argon atmosphere, remove unreacted I2 in acetonitrile solution, rinse the reaction product with acetonitrile, and wash away the adsorbed I2 simple substance, The precursor TiSSe was obtained after vacuum drying.
(2)锂化:(2) Lithiation:
将上述TiSSe粉体加入到浓度为0.1M的联苯锂的乙二醇二甲醚溶液中,进行锂化反应15min,得到锂化后的产物,之后离心分离出该产物,并采用溶剂反复清洗,得到正极补锂剂,其平均化学式为Li 3TiSSe。 Add the above TiSSe powder into the ethylene glycol dimethyl ether solution of biphenyllithium with a concentration of 0.1M, carry out the lithiation reaction for 15 minutes, and obtain the lithiated product, and then centrifuge the product, and wash it repeatedly with a solvent , to obtain a positive electrode lithium supplement, the average chemical formula of which is Li 3 TiSSe.
实施例6Example 6
一种正极补锂剂的制备方法,包括:A preparation method of a positive electrode lithium supplement, comprising:
(1)补锂剂前驱物制备:(1) Preparation of lithium supplementation agent precursor:
将Na 2S和S、Se、V按照1:1:2:2的摩尔比混合,在氩气气氛下进行球磨,其中,球磨 转速为600r/min,时间为30min,将球磨后得到的混合料在氩气气氛下进行烧结,其中,烧结温度为950℃,保温时间为8h,之后冷却至室温,得到产物为NaVSSe; Mix Na 2 S, S, Se, and V in a molar ratio of 1:1:2:2, and perform ball milling under an argon atmosphere, wherein the ball milling speed is 600r/min, and the time is 30min. The material is sintered in an argon atmosphere, wherein the sintering temperature is 950°C, the holding time is 8h, and then cooled to room temperature to obtain the product NaVSSe;
然后将NaVSSe与I 2按照一定的摩尔比加入乙腈中,在氩气气氛下充分混合反应后,除去未反应的I 2的乙腈溶液,将反应产物用乙腈冲洗,洗去吸附的I 2单质,真空干燥后得到前驱物VSSe。 Then add NaVSSe and I2 into acetonitrile according to a certain molar ratio, and after fully mixing and reacting under an argon atmosphere, remove unreacted I2 in acetonitrile solution, rinse the reaction product with acetonitrile, and wash away the adsorbed I2 simple substance, The precursor VSSe was obtained after vacuum drying.
(2)锂化:(2) Lithiation:
将上述VSSe粉体加入到浓度为0.1M的联苯锂的乙二醇二甲醚溶液中,进行锂化反应20min,得到锂化后的产物,之后离心分离出该产物,并采用溶剂反复清洗,得到正极补锂剂,其平均化学式为Li 3.5VSSe。 Add the above VSSe powder into the ethylene glycol dimethyl ether solution of biphenyllithium with a concentration of 0.1M, and carry out the lithiation reaction for 20 minutes to obtain the lithiated product, which is then centrifuged to separate the product and washed repeatedly with a solvent , to obtain a positive electrode lithium supplement, and its average chemical formula is Li 3.5 VSSe.
实施例7Example 7
一种正极补锂剂的制备方法,包括:A preparation method of a positive electrode lithium supplement, comprising:
(1)补锂剂前驱物制备:(1) Preparation of lithium supplementation agent precursor:
将Na 2S和S、Se、Mn按照1:1:2:2的摩尔比混合,在氩气气氛下进行球磨,其中,球磨转速为600r/min,时间为30min,将球磨后得到的混合料在氩气气氛下进行烧结,其中,烧结温度为800℃,保温时间为10h,之后冷却至室温,得到产物为NaMnSSe; Mix Na 2 S, S, Se, and Mn in a molar ratio of 1:1:2:2, and perform ball milling under an argon atmosphere, wherein the ball milling speed is 600r/min, and the time is 30min. The material is sintered in an argon atmosphere, wherein the sintering temperature is 800°C, the holding time is 10h, and then cooled to room temperature, and the obtained product is NaMnSSe;
然后将NaMnSSe与I 2按照一定的摩尔比加入乙腈中,在氩气气氛下充分混合反应后,除去未反应的I 2的乙腈溶液,将反应产物用乙腈冲洗,洗去吸附的I 2单质,真空干燥后得到前驱物MnSSe。 Then add NaMnSSe and I2 into acetonitrile according to a certain molar ratio, and after fully mixing and reacting under an argon atmosphere, remove the unreacted I2 acetonitrile solution, rinse the reaction product with acetonitrile, and wash away the adsorbed I2 simple substance, The precursor MnSSe was obtained after vacuum drying.
(2)锂化:(2) Lithiation:
将上述MnSSe粉体加入到浓度为0.1M的联苯锂的乙二醇二甲醚溶液中,进行锂化反应20min,得到锂化后的产物,之后离心分离出该产物,并采用溶剂反复清洗,得到正极补锂剂,其平均化学式为Li 3.5MnSSe。 Add the above MnSSe powder into the ethylene glycol dimethyl ether solution of biphenyllithium with a concentration of 0.1M, carry out the lithiation reaction for 20 minutes, and obtain the lithiated product, which is then centrifuged to separate the product and wash it repeatedly with a solvent , to obtain a positive electrode lithium supplement, and its average chemical formula is Li 3.5 MnSSe.
实施例8Example 8
一种正极补锂剂的制备方法,包括:A preparation method of a positive electrode lithium supplement, comprising:
(1)补锂剂前驱物制备:(1) Preparation of lithium supplementation agent precursor:
将Na 2S和S、Se、Cr按照1:1:2:2的摩尔比混合,在氩气气氛下进行球磨,其中,球磨转速为600r/min,时间为30min,将球磨后得到的混合料在氩气气氛下进行烧结,其中,烧结温度为800℃,保温时间为10h,之后冷却至室温,得到产物为NaCrSSe; Mix Na 2 S, S, Se, and Cr at a molar ratio of 1:1:2:2, and perform ball milling under an argon atmosphere, wherein the ball milling speed is 600r/min, and the time is 30min. The material is sintered in an argon atmosphere, wherein the sintering temperature is 800°C, the holding time is 10h, and then cooled to room temperature to obtain the product NaCrSSe;
然后将NaCrSSe与I 2按照一定的摩尔比加入乙腈中,在氩气气氛下充分混合反应后,除去未反应的I 2的乙腈溶液,将反应产物用乙腈冲洗,洗去吸附的I 2单质,真空干燥后得到前驱物CrSSe。 Then add NaCrSSe and I2 into acetonitrile according to a certain molar ratio, and after fully mixing and reacting under an argon atmosphere, remove the unreacted I2 acetonitrile solution, rinse the reaction product with acetonitrile, and wash away the adsorbed I2 simple substance, The precursor CrSSe was obtained after vacuum drying.
(2)锂化:(2) Lithiation:
将上述CrSSe粉体加入到浓度为0.1M的联苯锂的乙二醇二甲醚溶液中,进行锂化反应15min,得到锂化后的产物,之后离心分离出该产物,并采用溶剂反复清洗,得到该正极补锂剂,其平均化学式为Li 3CrSSe。 Add the above-mentioned CrSSe powder into the ethylene glycol dimethyl ether solution of biphenyllithium with a concentration of 0.1M, and carry out the lithiation reaction for 15 minutes to obtain the lithiated product, which is then centrifuged to separate the product and washed repeatedly with a solvent , to obtain the positive electrode lithium supplement, the average chemical formula of which is Li 3 CrSSe.
实施例9Example 9
一种正极补锂剂的制备方法,包括:A preparation method of a positive electrode lithium supplement, comprising:
(1)补锂剂前驱物制备:(1) Preparation of lithium supplementation agent precursor:
将Na 2S和S、Se、Cr按照1:2:1:2的摩尔比混合,在氩气气氛下进行球磨,其中,球磨转速为600r/min,时间为30min,将球磨后得到的混合料在氩气气氛下进行烧结,其中,烧结温度为800℃,保温时间为10h,之后冷却至室温,得到产物为NaCrS 1.5Se 0.5Mix Na 2 S, S, Se, and Cr at a molar ratio of 1:2:1:2, and perform ball milling under an argon atmosphere, wherein the ball milling speed is 600r/min, and the time is 30min. The material is sintered under an argon atmosphere, wherein the sintering temperature is 800°C, the holding time is 10h, and then cooled to room temperature to obtain the product NaCrS 1.5 Se 0.5 ;
然后将NaCrS 1.5Se 0.5与I 2按照一定的摩尔比加入乙腈中,在氩气气氛下充分混合反应后,除去未反应的I 2的乙腈溶液,将反应产物用乙腈冲洗,洗去吸附的I 2单质,真空干燥后得到前驱物CrS 1.5Se 0.5Then add NaCrS 1.5 Se 0.5 and I 2 into acetonitrile according to a certain molar ratio, and after fully mixing and reacting under an argon atmosphere, remove the unreacted I 2 in acetonitrile solution, rinse the reaction product with acetonitrile, and wash away the adsorbed I 2 simple substance, the precursor CrS 1.5 Se 0.5 was obtained after vacuum drying.
(2)锂化:(2) Lithiation:
将上述CrS 1.5Se 0.5粉体加入到浓度为0.1M的联苯锂的乙二醇二甲醚溶液中,进行锂化反应20min,得到锂化后的产物,之后离心分离出该产物,并采用溶剂反复清洗,得到该正极补锂剂,其平均化学式为Li 3.5CrS 1.5Se 0.5The above-mentioned CrS 1.5 Se 0.5 powder was added to the ethylene glycol dimethyl ether solution of biphenyllithium with a concentration of 0.1M, and the lithiation reaction was carried out for 20 minutes to obtain the lithiated product, which was then centrifuged and separated, and used The solvent is repeatedly washed to obtain the positive electrode lithium supplement, and its average chemical formula is Li 3.5 CrS 1.5 Se 0.5 .
实施例10Example 10
一种正极补锂剂的制备方法,包括:A preparation method of a positive electrode lithium supplement, comprising:
(1)补锂剂前驱物制备:(1) Preparation of lithium supplementation agent precursor:
将Na 2S和Se、Cr按照1:3:2的摩尔比混合,在氩气气氛下进行球磨,其中,球磨转速为600r/min,时间为30min,将球磨后得到的混合料在氩气气氛下进行烧结,其中,烧结温度为800℃,保温时间为10h,之后冷却至室温,得到产物为NaCrS 0.5Se 1.5Mix Na 2 S, Se, and Cr at a molar ratio of 1:3:2, and perform ball milling under an argon atmosphere. The ball milling speed is 600r/min, and the time is 30min. Carry out sintering under the atmosphere, wherein, the sintering temperature is 800°C, the holding time is 10h, and then cooled to room temperature, the obtained product is NaCrS 0.5 Se 1.5 ;
然后将NaCrS 0.5Se 1.5与I 2按照一定的摩尔比加入乙腈中,在氩气气氛下充分混合反应后,除去未反应的I 2的乙腈溶液,将反应产物用乙腈冲洗,洗去吸附的I 2单质,真空干燥后得到前驱物CrS 0.5Se 1.5Then add NaCrS 0.5 Se 1.5 and I 2 into acetonitrile according to a certain molar ratio, and after fully mixing and reacting under an argon atmosphere, remove the unreacted I 2 in acetonitrile solution, rinse the reaction product with acetonitrile, and wash away the adsorbed I 2 simple substance, the precursor CrS 0.5 Se 1.5 was obtained after vacuum drying.
(2)锂化:(2) Lithiation:
将上述CrS 0.5Se 1.5粉体加入到浓度为0.1M的联苯锂的乙二醇二甲醚溶液中,进行锂化反应20min,得到锂化后的产物,之后离心分离出该产物,并采用溶剂反复清洗,得到该正极补锂剂,其平均化学式为Li 3.5CrS 0.5Se 1.5The above-mentioned CrS 0.5 Se 1.5 powder was added to the ethylene glycol dimethyl ether solution of biphenyllithium with a concentration of 0.1M, and the lithiation reaction was carried out for 20 minutes to obtain the lithiated product, which was then centrifuged and separated, and used The solvent is washed repeatedly to obtain the positive electrode lithium supplement, and its average chemical formula is Li 3.5 CrS 0.5 Se 1.5 .
根据实施例2记载的方法,将实施例3-10的正极补锂剂分别制备成正极极片,并组装成扣式电池,并对各扣式电池进行充放电测试,电压范围为对应的OTC至4.2V,记录其充放电曲线,并结合仅含正极活性材料的对比例2半电池,并计算得到各补锂剂的脱锂比容量,结果如表1所示。According to the method described in Example 2, the positive electrode lithium supplements of Examples 3-10 were respectively prepared into positive electrode sheets, and assembled into button batteries, and each button battery was charged and discharged. The voltage range was the corresponding OTC To 4.2V, record the charge-discharge curve, and combine with the half-cell of Comparative Example 2 containing only the positive electrode active material, and calculate the lithium-removing specific capacity of each lithium-supplementing agent. The results are shown in Table 1.
此外,还将以上各实施例的正极补锂剂分别装配成全电池,并对装配好的各全电池进行化成后,以将电芯内部的正、负极活性材料激活,并在负极形成稳定的SEI膜,改善电池的自放电、充放电性能和储存性能等。其中,全电池的装配过程为:以石墨极片为负极、隔膜为celgard2400,电解液采用1mol/L LiPF 6的碳酸乙烯酯(EC)、碳酸甲乙酯(EMC)和碳酸二甲酯(DMC)的混合溶液;在充满氩气的手套箱中进行组装,得到锂离子全电池。 In addition, the positive electrode lithium supplements of the above embodiments were assembled into full batteries, and each assembled full battery was chemically formed to activate the positive and negative active materials inside the battery cell and form a stable SEI on the negative electrode. film, improve battery self-discharge, charge and discharge performance and storage performance. Among them, the assembly process of the full battery is as follows: the graphite pole piece is used as the negative electrode, the diaphragm is celgard2400, and the electrolyte is 1mol/L LiPF 6 ethylene carbonate (EC), ethyl methyl carbonate (EMC) and dimethyl carbonate (DMC). ) mixed solution; assembled in an argon-filled glove box to obtain a lithium-ion full battery.
化成的具体过程如下:全电池装配好后在25℃的温度下先静置4h,然后以0.05C的倍率恒流充电至4.2V,再以4.2V恒压充电至充电电流<0.005C。之后,将化成后的各全电池以0.2C进行充放电循环,电压范围:2.7V~4.2V,测试其首圈库伦效率、放电比容量、循环性能等。需要说明的是,这里的首次充电,是指化成时的充电,而非通常电池出厂后的首充(实际上应为第二次充电)。The specific process of the formation is as follows: After the full battery is assembled, it is left to stand at a temperature of 25°C for 4 hours, then charged at a constant current rate of 0.05C to 4.2V, and then charged at a constant voltage of 4.2V to a charging current <0.005C. Afterwards, each full battery after formation was subjected to a charge-discharge cycle at 0.2C, with a voltage range of 2.7V to 4.2V, to test its first-cycle Coulombic efficiency, discharge specific capacity, and cycle performance. It should be noted that the first charge here refers to the charge at the time of formation, not the usual first charge after the battery leaves the factory (actually it should be the second charge).
此外,本申请还提供了同等条件下未添加本申请实施例正极补锂剂的LiFePO 4全电池(对比例2)的性能测试结果。 In addition, the present application also provides the performance test results of the LiFePO 4 full battery (Comparative Example 2) under the same conditions without adding the positive electrode lithium replenishing agent of the embodiment of the present application.
表1各实施例和对比例的半电池的测试结果汇总Summary of the test results of the half-cells of each embodiment and comparative example in table 1
Figure PCTCN2023071097-appb-000001
Figure PCTCN2023071097-appb-000001
表2各实施例和对比例的全电池的测试结果汇总Summary of the test results of the full battery of each embodiment and comparative example in table 2
Figure PCTCN2023071097-appb-000002
Figure PCTCN2023071097-appb-000002
本申请上述实施例中平均化学式为Li xMS ySe 2-y的补锂剂,M可适用于多种过渡金属,y可取不同值,x也可取不同值,可通过调控锂化工艺进行控制。从表1的半电池数据可以获知,本申请实施例的补锂剂在首圈发生不可逆分解,脱锂比容量可超过450mAh/g,说明补锂剂的补锂容量高。所装半电池循环100圈后,容量保持率与对比例2(无补锂剂的半电池)接近,说明补锂剂对正极在循环中无明显副作用,兼容性良好。 In the above examples of the present application, the average chemical formula is Li x MS y Se 2-y lithium replenishing agent, M can be applied to a variety of transition metals, y can take different values, and x can also take different values, which can be controlled by adjusting the lithiation process . From the half-cell data in Table 1, it can be known that the lithium supplementation agent of the embodiment of the present application undergoes irreversible decomposition in the first cycle, and the delithiation specific capacity can exceed 450mAh/g, indicating that the lithium supplementation agent has a high lithium supplementation capacity. After 100 cycles of the installed half-battery, the capacity retention rate is close to that of Comparative Example 2 (half-cell without lithium-supplementing agent), indicating that the lithium-supplementing agent has no obvious side effects on the positive electrode during the cycle and has good compatibility.
从表2的全电池数据可以获知,本申请实施例的补锂剂在首圈发生不可逆分解,全电池的首次放电比容量由对比例的144mAh/g提高至155mAh/g以上,甚至可达160mAh/g,这说明其可弥补负极活性锂的损失,且在负极存有部分预存锂,从而提升电芯的循环性能与能量密度。循环100圈后,添加本申请补锂剂的全电池,其容量保持率明显优于无补锂剂的全电池,说明加入本申请补锂剂后的电池能量密度提升,循环性能明显改善,对正极无其他副作用,兼容性良好。From the data of the full battery in Table 2, it can be known that the lithium supplementing agent of the embodiment of the present application is irreversibly decomposed in the first cycle, and the first discharge specific capacity of the full battery is increased from 144mAh/g in the comparative example to more than 155mAh/g, and even up to 160mAh /g, which shows that it can make up for the loss of active lithium in the negative electrode, and there is a part of pre-stored lithium in the negative electrode, thereby improving the cycle performance and energy density of the battery. After 100 cycles, the capacity retention rate of the full battery added with the lithium-supplementing agent of the present application is significantly better than that of the full battery without the lithium-supplementing agent. No other side effects, good compatibility.
另外,表2中对比例2的全电池首圈库伦效率看着比实施例2-10高,这主要是由于表2中的首次充电是指化成时的充电,循环容量保持率的计算也是以化成数据为比较基准,未补锂的对比例2的首圈库伦效率为负极与正极消耗后的首效,即,其损耗部分是正极的不可逆活性锂,第2圈及以后的放电比容量低,循环性能差。而添加补锂剂的各实施例全电池,其首圈循环(化成时)消耗的是补锂剂提供的活性锂,并未消耗正极活性材料的,虽然看着首效低,但第2圈及以后的库伦效率并不低;且放电比容量高,循环性能好,电池的能量密度也相应较高。In addition, the first-cycle Coulombic efficiency of the full battery in Comparative Example 2 in Table 2 seems to be higher than that of Examples 2-10, which is mainly because the first charge in Table 2 refers to the charge during formation, and the calculation of the cycle capacity retention rate is also based on The formation data is used as a comparison basis. The first-cycle coulombic efficiency of Comparative Example 2 without lithium supplementation is the first effect after the negative electrode and positive electrode are consumed, that is, the loss part is the irreversible active lithium of the positive electrode, and the discharge specific capacity of the second cycle and later is low. , poor cycle performance. However, for the full battery of each embodiment with added lithium supplementing agent, the first cycle (during formation) consumes the active lithium provided by the lithium supplementing agent, and does not consume the positive electrode active material. Although the first effect is low, the second cycle The Coulombic efficiency in the future is not low; and the discharge specific capacity is high, the cycle performance is good, and the energy density of the battery is correspondingly high.

Claims (13)

  1. 一种正极补锂剂,其特征在于,所述正极补锂剂包括颗粒本体,所述颗粒本体包括过渡金属的硫硒化物的锂化物,所述过渡金属的硫硒化物的锂化物的平均化学式为Li xMS ySe 2-y,其中,1<x≤4,0<y<2,M代表过渡金属。 A positive electrode lithium replenishing agent, characterized in that the positive electrode lithium replenishing agent includes a particle body, the particle body includes a lithium compound of a transition metal sulfur selenide, and the average chemical formula of the lithium compound of the transition metal sulfur selenide is is Li x MS y Se 2-y , wherein, 1<x≤4, 0<y<2, and M represents a transition metal.
  2. 如权利要求1所述的正极补锂剂,其特征在于,所述颗粒本体包括通式为Li xMS ySe 2-y的化合物,以及M、Li 2S和Li 2Se。 The positive electrode lithium supplementing agent according to claim 1, wherein the particle body includes a compound of the general formula Li x MS y Se 2-y , and M, Li 2 S and Li 2 Se.
  3. 如权利要求2所述的正极补锂剂,其特征在于,所述颗粒本体还包括通式为LiMS ySe 2-y的化合物。 The positive electrode lithium supplement agent according to claim 2, characterized in that, the particle body also includes a compound with the general formula LiMSySe2 -y .
  4. 如权利要求1-3任一项所述的正极补锂剂,其特征在于,所述M包括Cr、Ti、V、Co、Fe、Ni、Mn、Nb的一种或多种。The positive electrode lithium replenishing agent according to any one of claims 1-3, wherein the M includes one or more of Cr, Ti, V, Co, Fe, Ni, Mn, and Nb.
  5. 如权利要求1-4任一项所述的正极补锂剂,其特征在于,所述颗粒本体的表面还具有包覆层。The positive electrode lithium supplement agent according to any one of claims 1-4, characterized in that, the surface of the particle body also has a coating layer.
  6. 一种正极补锂剂的制备方法,其特征在于,所述制备方法包括:A preparation method of a positive electrode lithium supplement, characterized in that the preparation method comprises:
    将过渡金属源、硫源、硒源混合后进行球磨并烧结,制得过渡金属的硫硒化物;Mixing transition metal sources, sulfur sources, and selenium sources, ball milling and sintering to prepare transition metal sulfoselenides;
    对所述过渡金属的硫硒化物进行锂化,得到正极补锂剂;其中,所述正极补锂剂包括颗粒本体,所述颗粒本体包括过渡金属的硫硒化物的锂化物,所述过渡金属的硫硒化物的锂化物的平均化学式为Li xMS ySe 2-y,其中,1<x≤4,0<y<2,M代表过渡金属。 The sulfoselenide of the transition metal is lithiated to obtain a positive electrode lithium supplement; wherein, the positive electrode lithium supplement includes a particle body, and the particle body includes a lithium compound of a transition metal sulfoselenide, and the transition metal The average chemical formula of the lithiated sulfur selenide is Li x MS y Se 2-y , where 1<x≤4, 0<y<2, and M represents a transition metal.
  7. 一种电池正极极片,其特征在于,所述电池正极极片中含有如权利要求1-5任一项所述的正极补锂剂。A positive pole piece of a battery, characterized in that the positive pole piece of the battery contains the positive lithium replenishing agent according to any one of claims 1-5.
  8. 如权利要求7所述的电池正极极片,其特征在于,所述电池正极极片包括集流体和设置在所述集流体上的正极材料层,所述正极材料层包括正极活性材料、所述正极补锂剂,以及粘结剂。The positive electrode sheet of the battery according to claim 7, wherein the positive electrode sheet of the battery comprises a current collector and a positive electrode material layer arranged on the current collector, and the positive electrode material layer includes a positive electrode active material, the Positive electrode lithium supplement, and binder.
  9. 如权利要求7所述的电池正极极片,其特征在于,所述电池正极极片包括集流体及依次设置在所述集流体上的正极材料层和补锂剂层,其中,所述正极材料层含有正极活性材料及粘结剂和导电剂,所述补锂剂层含有所述正极补锂剂及粘结剂和导电剂。The positive electrode sheet of the battery according to claim 7, wherein the positive electrode sheet of the battery comprises a current collector, a positive electrode material layer and a lithium replenishing agent layer sequentially arranged on the current collector, wherein the positive electrode material The layer contains positive electrode active material, binding agent and conductive agent, and the lithium supplementing agent layer contains the positive electrode lithium supplementing agent, binding agent and conductive agent.
  10. 如权利要求8或9所述的电池正极极片,其特征在于,所述正极补锂剂的质量相对于所述正极补锂剂与所述正极活性材料的质量之和的占比为1%-10%。The positive electrode sheet of the battery according to claim 8 or 9, wherein the mass of the positive lithium supplementing agent accounts for 1% of the sum of the mass of the positive lithium supplementing agent and the positive active material -10%.
  11. 如权利要求8所述的电池正极极片,其特征在于,所述正极补锂剂的质量占所述正极材料层的质量的0.5%-15%。The positive electrode sheet of the battery according to claim 8, wherein the mass of the positive electrode lithium supplementing agent accounts for 0.5%-15% of the mass of the positive electrode material layer.
  12. 一种电化学电池,其特征在于,包括正电极、负电极、以及位于所述正电极和所述负电极之间的隔膜和电解液,其中,所述正电极为如权利要求7-11任一项所述的电池正极极片。An electrochemical cell, characterized in that it comprises a positive electrode, a negative electrode, and a diaphragm and an electrolyte between the positive electrode and the negative electrode, wherein the positive electrode is as claimed in any one of claims 7-11. The battery positive pole piece described in one item.
  13. 一种电子设备,其特征在于,所述电子设备具有如权利要求12所述的电化学电池。An electronic device, characterized in that the electronic device has the electrochemical cell as claimed in claim 12.
PCT/CN2023/071097 2022-01-12 2023-01-06 Positive electrode lithium supplementing agent, and preparation method therefor and use thereof WO2023134589A1 (en)

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