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CN108736056B - A lithium metal interface protection structure and its preparation and application - Google Patents

A lithium metal interface protection structure and its preparation and application Download PDF

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CN108736056B
CN108736056B CN201710262306.8A CN201710262306A CN108736056B CN 108736056 B CN108736056 B CN 108736056B CN 201710262306 A CN201710262306 A CN 201710262306A CN 108736056 B CN108736056 B CN 108736056B
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battery
protection structure
lithium
interface protection
fluoride
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CN108736056A (en
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彭哲
张政刚
万浩
刘子萱
王德宇
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Ningbo Institute of Material Technology and Engineering of CAS
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    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M10/00Secondary cells; Manufacture thereof
    • H01M10/05Accumulators with non-aqueous electrolyte
    • H01M10/052Li-accumulators
    • 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
    • H01M4/134Electrodes based on metals, Si or alloys
    • 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
    • H01M4/628Inhibitors, e.g. gassing inhibitors, corrosion inhibitors
    • 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

本发明涉及一种锂金属界面保护结构及其制备和应用。具体地,本发明公开了一种界面保护结构。本发明还公开了所述界面保护结构的制备方法和应用。包含所述界面保护结构的电池具有优异的循环性能和使用寿命。所述制备方法具有工艺简单、成本低、原料易得等特点。The invention relates to a lithium metal interface protection structure and its preparation and application. Specifically, the present invention discloses an interface protection structure. The invention also discloses the preparation method and application of the interface protection structure. The battery including the interface protection structure has excellent cycle performance and service life. The preparation method has the characteristics of simple process, low cost, readily available raw materials and the like.

Description

一种锂金属界面保护结构及其制备和应用A lithium metal interface protection structure and its preparation and application

技术领域technical field

本发明涉及电化学领域,具体地涉及一种锂金属界面保护结构及其制备和应用。The invention relates to the field of electrochemistry, in particular to a lithium metal interface protection structure and its preparation and application.

背景技术Background technique

得益于石墨负极在循环过程中~10%的较小体积变化,以其为负极材料的锂离子电池可以获得稳定的循环性能和较长的使用寿命。然而石墨负极材料储锂容量相对较低(锂嵌入情况下为339mAh/g,锂脱出情况下为372mAh/g),在锂电池市场不断寻求更高能量密度体系的过程中,已无法满足行业需求。Benefiting from the small volume change of ~10% of the graphite anode during cycling, lithium-ion batteries using it as the anode material can achieve stable cycling performance and long service life. However, the lithium storage capacity of graphite anode materials is relatively low (339mAh/g in the case of lithium intercalation, 372mAh/g in the case of lithium extraction), and in the process of continuously seeking higher energy density systems in the lithium battery market, it has been unable to meet the needs of the industry .

锂金属作为一种高能量密度负极材料(锂金属理论容量为3860mAh/g,且具有最低电极电势)在锂空气、锂硫等新兴高储能电池体系中的应用前景被一致看好,然而循环效率较低安全性不良等问题一直阻碍着其在电池工业中的进一步推广和应用。通过大量的研究发现,在电池充电过程中,不论是在锂金属或其它金属集流体表面,都会产生不均匀的锂沉积。随着持续的充电过程,不均匀的锂沉积不可避免地导致锂金属表面的巨大体积膨胀和局部锂枝晶生长。体积膨胀和枝晶问题可以导致电极界面阻抗增加、电池容量损耗。持续的枝晶生长可以刺穿电解液隔膜导致电池短路,使得锂金属负极在使用过程中始终伴随着巨大的安全隐患,这也使其难以被应用于诸如电动车、随身电子设备等对安全系数要求较高的工作环境中。近年来通过业界提出的各种解决方案,锂金属负极的使用寿命和效率已得到明显改善,但改善强度依旧难以满足大规模商业化的需求。As a high energy density anode material (the theoretical capacity of lithium metal is 3860mAh/g and has the lowest electrode potential), the application prospects of lithium metal in emerging high energy storage battery systems such as lithium-air and lithium-sulfur are unanimously promising. However, the cycle efficiency Problems such as low safety and poor safety have always hindered its further promotion and application in the battery industry. Through a large number of studies, it has been found that in the process of battery charging, non-uniform lithium deposition will occur on the surface of lithium metal or other metal current collectors. With the continuous charging process, uneven Li deposition inevitably leads to huge volume expansion and local Li dendrite growth on the Li metal surface. Volume expansion and dendrite issues can lead to increased electrode interface impedance and battery capacity loss. The continuous dendrite growth can pierce the electrolyte separator and cause the battery to short-circuit, making the lithium metal negative electrode always accompanied by huge safety hazards during use, which also makes it difficult to be used in electric vehicles, portable electronic devices, etc. in a demanding work environment. In recent years, through various solutions proposed by the industry, the service life and efficiency of lithium metal anodes have been significantly improved, but the improved strength is still difficult to meet the needs of large-scale commercialization.

现有的保护方法对锂枝晶的防护作用过于单一。其中,使用固态电解质可以在一定程度上抑制枝晶生长,然而较低的离子导电性和较差的电极/电解质接触面都会导致电池内阻大幅度增加;另外,在电解液中加入促成膜型添加剂可以在电极表面加快形成具有保护作用的钝化层,然而该钝化层本身并不具备抑制枝晶生长的机械属性,最终电极表面依然会发生不均匀的枝晶生长,而且枝晶的过度生长可以刺穿钝化层,使得没有钝化层覆盖的锂金属部分直接与电解液接触并再度生成新的钝化层,如此地反复发生钝化层破裂和再生将不断消耗系统中的锂和电解液。The existing protection methods are too single in the protection of lithium dendrites. Among them, the use of solid electrolyte can inhibit dendrite growth to a certain extent, but the lower ionic conductivity and the poor electrode/electrolyte interface will lead to a large increase in the internal resistance of the battery; The additive can accelerate the formation of a protective passivation layer on the surface of the electrode, but the passivation layer itself does not have the mechanical properties to inhibit the growth of dendrites. In the end, uneven dendrite growth will still occur on the surface of the electrode, and excessive dendrite growth will occur. The growth can pierce the passivation layer, so that the part of the lithium metal that is not covered by the passivation layer directly contacts the electrolyte and generates a new passivation layer again. Repeated cracking and regeneration of the passivation layer will continuously consume the lithium and lithium in the system. Electrolyte.

综述所述,虽然本领域目前已存在可选的锂金属保护方法,但是现有锂金属负极的结构稳定性及循环效果均尚难以令人满意。In summary, although there are alternative lithium metal protection methods in the art, the structural stability and cycle effect of the existing lithium metal anodes are still unsatisfactory.

因此,本领域迫切需要开发一种可有效实现锂金属高循环效率的保护方法及其制备工艺。Therefore, there is an urgent need in the art to develop a protection method that can effectively achieve high cycle efficiency of lithium metal and a preparation process thereof.

发明内容SUMMARY OF THE INVENTION

本发明的目的在于提供一种可高效保护锂金属的界面保护结构及其制备和应用。The purpose of the present invention is to provide an interface protection structure capable of efficiently protecting lithium metal and its preparation and application.

本发明的第一方面,提供了一种界面保护结构前驱体材料,所述前驱体材料是如下制备的:In a first aspect of the present invention, an interface protection structure precursor material is provided, and the precursor material is prepared as follows:

1)提供一混合浆料,所述混合浆料包含:金属氟化物、碳材料、粘结剂和溶剂;1) Provide a mixed slurry, the mixed slurry includes: metal fluoride, carbon material, binder and solvent;

2)将所述混合浆料涂覆于金属基底表面,得到含第一涂层的金属基底;2) coating the mixed slurry on the surface of the metal substrate to obtain a metal substrate containing the first coating;

3)烘烤处理所述含第一涂层的金属基底,得到含第二涂层的金属基底,所述第二涂层即所述界面保护结构前驱体材料。3) Baking the metal substrate containing the first coating to obtain a metal substrate containing a second coating, where the second coating is the precursor material of the interface protection structure.

在另一优选例中,所述金属基底为不会与锂金属发生合金化的金属基底材料。In another preferred example, the metal base is a metal base material that does not alloy with lithium metal.

在另一优选例中,所述金属基底选自下组:铜箔、镍箔、不锈钢箔。In another preferred embodiment, the metal substrate is selected from the group consisting of copper foil, nickel foil, and stainless steel foil.

在另一优选例中,所述金属氟化物选自下组:氟化镍、氟化锰、氟化铁、氟化钛、氟化铜、氟化锡、或其组合;和/或In another preferred embodiment, the metal fluoride is selected from the group consisting of nickel fluoride, manganese fluoride, iron fluoride, titanium fluoride, copper fluoride, tin fluoride, or a combination thereof; and/or

所述碳材料选自下组:特密高导电碳黑、石墨烯、科琴黑、乙炔黑、碳纳米管、或其组合;和/或The carbon material is selected from the group consisting of ultra-conductive carbon black, graphene, Ketjen black, acetylene black, carbon nanotubes, or a combination thereof; and/or

所述粘结剂选自下组:聚偏氟乙烯、聚酰亚胺、叔苯丁基橡胶、聚丙烯腈、聚丙烯酸酯、海藻酸钠、或其组合。The binder is selected from the group consisting of polyvinylidene fluoride, polyimide, t-phenylbutyl rubber, polyacrylonitrile, polyacrylate, sodium alginate, or a combination thereof.

在另一优选例中,所述溶剂选自下组:水、N-甲基吡咯烷酮、N,N-二甲基甲酰胺、N,N-二甲基乙酰胺、二甲基亚砜、或其组合。In another preferred embodiment, the solvent is selected from the group consisting of water, N-methylpyrrolidone, N,N-dimethylformamide, N,N-dimethylacetamide, dimethylsulfoxide, or its combination.

在另一优选例中,所述混合浆料中,所述金属氟化物、所述碳材料和所述粘结剂的质量比为5-12:1-3:1-5,较佳地7-10:1-2:1-3。In another preferred example, in the mixed slurry, the mass ratio of the metal fluoride, the carbon material and the binder is 5-12:1-3:1-5, preferably 7 -10:1-2:1-3.

在另一优选例中,所述第一涂层的厚度为10-100微米,较佳地20-40微米。In another preferred embodiment, the thickness of the first coating is 10-100 microns, preferably 20-40 microns.

在另一优选例中,所述烘烤处理的处理温度为60-160℃,较佳地100-140℃;和/或In another preferred embodiment, the treatment temperature of the baking treatment is 60-160°C, preferably 100-140°C; and/or

所述烘烤处理在所述处理温度下的处理时间为1-20h,较佳地6-16h,更佳地8-14h。The treatment time of the baking treatment at the treatment temperature is 1-20h, preferably 6-16h, more preferably 8-14h.

在另一优选例中,所述烘烤处理在真空或惰性气体保护下进行。In another preferred embodiment, the baking process is carried out under the protection of vacuum or inert gas.

在另一优选例中,在步骤3)之后还任选地包括步骤:切割步骤3)所得产物,得到含所述界面保护结构前驱体材料的负极材料。In another preferred example, after step 3), the method further includes a step of: cutting the product obtained in step 3) to obtain a negative electrode material containing the interface protection structure precursor material.

本发明的第二方面,提供了一种界面保护结构,所述界面保护结构是如下制备的:In a second aspect of the present invention, an interface protection structure is provided, and the interface protection structure is prepared as follows:

i)提供含本发明第一方面所述界面保护结构前驱体材料的负极材料、电解液、隔膜、锂电极片;i) providing a negative electrode material, an electrolyte, a separator, and a lithium electrode sheet containing the precursor material of the interface protection structure according to the first aspect of the present invention;

ii)以所述负极材料、所述电解液、所述隔膜和所述锂电极片组装电池;ii) assembling a battery with the negative electrode material, the electrolyte, the separator and the lithium electrode sheet;

iii)电化学还原处理步骤ii)所得电池,拆解所得电池,即可从所得负极上剥离得到所述界面保护结构。iii) The battery obtained in the electrochemical reduction treatment step ii) is disassembled, and the interface protection structure can be obtained by peeling off the obtained negative electrode.

在另一优选例中,所述电解液、所述隔膜和所述锂电极片没有特别限制,可采用本领域常规的材料,或采用本领域常规的方法制备得到,或从市场购买得到。In another preferred example, the electrolyte, the separator and the lithium electrode sheet are not particularly limited, and can be prepared by using conventional materials in the art, or prepared by conventional methods in the art, or purchased from the market.

在另一优选例中,所述电解液选自下组:3011R(购自张家港市国泰华荣化工新材料有限公司)、自行调配的电解液(其中,锂盐选自下组:六氟磷酸锂、高氯酸锂、双三氟甲烷磺酰亚胺锂、双氟磺酰亚胺锂、或其组合;溶剂选自下组:碳酸二甲酯、碳酸甲乙酯、碳酸二乙酯、碳酸乙烯酯、碳酸丙烯酯、乙二醇二甲醚、1,3-二氧戊环、或其组合)。In another preferred example, the electrolyte is selected from the following group: 3011R (purchased from Zhangjiagang Guotai Huarong Chemical New Material Co., Ltd.), the electrolyte (wherein, the lithium salt is selected from the following group: lithium hexafluorophosphate, high Lithium chlorate, lithium bistrifluoromethanesulfonimide, lithium bisfluorosulfonimide, or a combination thereof; the solvent is selected from the group consisting of dimethyl carbonate, ethyl methyl carbonate, diethyl carbonate, ethylene carbonate , propylene carbonate, ethylene glycol dimethyl ether, 1,3-dioxolane, or a combination thereof).

在另一优选例中,所述隔膜选自下组:聚乙烯隔膜、聚丙烯隔膜、丙烯/乙烯共聚物隔膜、聚酯膜(PET,Polyethylene Terephthalate)、纤维素膜、聚酰亚胺膜(PI)、聚酰胺膜(PA)、氨纶或芳纶膜、或其组合。In another preferred embodiment, the separator is selected from the group consisting of polyethylene separator, polypropylene separator, propylene/ethylene copolymer separator, polyester film (PET, Polyethylene Terephthalate), cellulose film, polyimide film ( PI), polyamide film (PA), spandex or aramid film, or a combination thereof.

在另一优选例中,所述锂电极片的厚度为50-200微米,较佳地100-150微米。In another preferred embodiment, the thickness of the lithium electrode sheet is 50-200 microns, preferably 100-150 microns.

在另一优选例中,所述电化学还原处理是指:将所述电池放电至0V。In another preferred example, the electrochemical reduction treatment refers to: discharging the battery to 0V.

本发明的第三方面,提供了一种制品,所述制品包含本发明第一方面所述界面保护结构前驱体材料或本发明第二方面所述界面保护结构。According to a third aspect of the present invention, there is provided an article comprising the interface protection structure precursor material of the first aspect of the present invention or the interface protection structure of the second aspect of the present invention.

在另一优选例中,所述制品优选为电池。In another preferred embodiment, the product is preferably a battery.

本发明的第四方面,提供了一种电池,所述电池包含本发明第二方面所述界面保护结构。A fourth aspect of the present invention provides a battery, which includes the interface protection structure described in the second aspect of the present invention.

在另一优选例中,所述电池为锂金属电池,优选锂金属二次电池。In another preferred example, the battery is a lithium metal battery, preferably a lithium metal secondary battery.

在另一优选例中,所述电池还包含正极材料、负极材料、电解液和隔膜。In another preferred example, the battery further includes a positive electrode material, a negative electrode material, an electrolyte and a separator.

在另一优选例中,本发明第二方面所述界面保护结构与所述隔膜相邻布置。In another preferred embodiment, the interface protection structure in the second aspect of the present invention is arranged adjacent to the diaphragm.

在另一优选例中,本发明第二方面所述界面保护结构位于所述负极材料和所述隔膜材料之间。In another preferred embodiment, the interface protection structure in the second aspect of the present invention is located between the negative electrode material and the separator material.

在另一优选例中,所述负极材料为所述界面保护结构的支撑材料,优选地,所述负极材料选自下组:铜箔、铜网、锂箔、镍网、铝箔、铝网、或其组合。In another preferred example, the negative electrode material is the support material of the interface protection structure, preferably, the negative electrode material is selected from the following group: copper foil, copper mesh, lithium foil, nickel mesh, aluminum foil, aluminum mesh, or a combination thereof.

在另一优选例中,所述电池在锂金属沉积/分解循环100周后,其库伦效率≥60%,较佳地≥70%,更佳地≥80%,较佳地≥90%,最佳地≥95%。In another preferred embodiment, the coulombic efficiency of the battery after 100 cycles of lithium metal deposition/decomposition is greater than or equal to 60%, preferably greater than or equal to 70%, more preferably greater than or equal to 80%, preferably greater than or equal to 90%, and most preferably Good location ≥ 95%.

应理解,在本发明范围内中,本发明的上述各技术特征和在下文(如实施例)中具体描述的各技术特征之间都可以互相组合,从而构成新的或优选的技术方案。限于篇幅,在此不再一一累述。It should be understood that within the scope of the present invention, the above-mentioned technical features of the present invention and the technical features specifically described in the following (eg, the embodiments) can be combined with each other to form new or preferred technical solutions. Due to space limitations, it is not repeated here.

附图说明Description of drawings

图1示意了本发明所述界面保护结构的使用方法。FIG. 1 illustrates a method of using the interface protection structure of the present invention.

图2是实施例1-6制得的铜锂电池1-6和对比例1制得的铜锂电池C1在本发明测试条件下循环100周的库伦效率变化。FIG. 2 shows the change in coulombic efficiency of the copper-lithium batteries 1-6 prepared in Examples 1-6 and the copper-lithium battery C1 prepared in Comparative Example 1 under the test conditions of the present invention for 100 cycles.

具体实施方式Detailed ways

本发明人经过长期而深入的研究,意外地制备得到一种可高效保护锂金属的界面保护结构,包含所述界面保护结构的电池可获得优异的循环性能和使用寿命。所述界面保护结构的制备方法具有工艺简单、成本低、原料易得等特点。在此基础上,发明人完成了本发明。After long-term and in-depth research, the inventors have unexpectedly prepared an interface protection structure that can efficiently protect lithium metal, and a battery comprising the interface protection structure can obtain excellent cycle performance and service life. The preparation method of the interface protection structure has the characteristics of simple process, low cost, easy availability of raw materials and the like. On this basis, the inventors have completed the present invention.

界面保护结构及其制备方法Interface protection structure and preparation method thereof

在本发明中,应理解,经所述电化学还原处理所得界面保护结构具有氟化锂框架。In the present invention, it should be understood that the interface protection structure obtained by the electrochemical reduction treatment has a lithium fluoride framework.

在本发明中,所述界面保护结构前驱体材料包括金属氟化物/碳材料/粘结剂。In the present invention, the interface protection structure precursor material includes metal fluoride/carbon material/binder.

代表性地,所述金属氟化物包括(但并不限于):氟化镍、氟化钛、氟化铜、氟化铁、或氟化锰等常规金属氟化物或其组合,可以选用本领域常规的材料,或用常规方法制备,或从市场购买得到。Typically, the metal fluorides include (but are not limited to): conventional metal fluorides such as nickel fluoride, titanium fluoride, copper fluoride, iron fluoride, or manganese fluoride or combinations thereof, which can be selected in the art Conventional materials, either prepared by conventional methods, or purchased from the market.

代表性地,所述金属氟化物的颗粒粒径为10-100纳米。Typically, the particle size of the metal fluoride is 10-100 nanometers.

代表性地,所述碳材料包括(但并不限于):特密高导电碳黑(Super-P)、科琴黑、乙炔黑、石墨烯、碳纳米管、或其组合。Representatively, the carbon material includes (but is not limited to): Super-P, Ketjen black, acetylene black, graphene, carbon nanotube, or a combination thereof.

代表性地,所述粘结剂包括(但并不限于):叔苯丁基橡胶、聚酰亚胺、聚偏氟乙烯、聚丙烯腈、聚丙烯酸酯、海藻酸钠、或其组合。Typically, the binder includes (but is not limited to): tert-phenylene butyl rubber, polyimide, polyvinylidene fluoride, polyacrylonitrile, polyacrylate, sodium alginate, or a combination thereof.

在一优选例中,所述的金属氟化物:碳材料:粘结剂的重量比为65~89%:10~30%:1~5%。In a preferred example, the weight ratio of the metal fluoride: the carbon material: the binder is 65-89%: 10-30%: 1-5%.

在本发明中,所述金属氟化物负载量为1~5毫克/平方厘米。In the present invention, the loading amount of the metal fluoride is 1-5 mg/cm 2 .

典型地,所述界面保护结构是如下制备的:Typically, the interface protection structure is prepared as follows:

(1)将粘结剂搅拌预溶于有机溶剂中获得粘结剂溶液,粘结剂溶液浓度不超过质量比30%;(1) the binder is stirred and pre-dissolved in an organic solvent to obtain a binder solution, and the concentration of the binder solution does not exceed 30% by mass;

(2)将金属氟化物、碳材料和粘结剂溶液于有机溶剂中混合搅拌获得前驱体材料浆料;(2) mixing and stirring the metal fluoride, the carbon material and the binder solution in an organic solvent to obtain a precursor material slurry;

(3)将前驱体材料浆料涂覆于集流体一侧面,低温预热挥发有机溶剂之后再在惰性气氛或真空环境中烘烤;(3) Coating the precursor material slurry on one side of the current collector, preheating the volatilized organic solvent at a low temperature, and then baking in an inert atmosphere or a vacuum environment;

(4)将烘烤后的极片装入对电极为锂片的电池放电至0V进行还原,拆解电池,将电化学还原后的极片于空气环境中静置后,获得可剥离的自支撑界面保护结构。(4) Put the baked pole piece into the battery whose counter electrode is a lithium piece and discharge to 0V for reduction, disassemble the battery, and leave the electrochemically reduced pole piece in an air environment to obtain a peelable self-contained Support interface protection structure.

代表性地,所述有机溶剂根据粘结剂不同,包括(但并不限于):水、N-甲基吡咯烷酮、N,N-二甲基甲酰胺、N,N-二甲基乙酰胺、二甲基亚砜,或其组合。Typically, the organic solvent is different according to the binder, including (but not limited to): water, N-methylpyrrolidone, N,N-dimethylformamide, N,N-dimethylacetamide, dimethyl sulfoxide, or a combination thereof.

在另一优选例中,所述溶剂为N-甲基吡咯烷酮。In another preferred embodiment, the solvent is N-methylpyrrolidone.

在另一优选例中,所述搅拌为磁力搅拌。In another preferred embodiment, the stirring is magnetic stirring.

在另一优选例中,所述步骤(1)和/或(2)中搅拌的时间为1~5小时,优选地为2~3小时。In another preferred example, the stirring time in the step (1) and/or (2) is 1-5 hours, preferably 2-3 hours.

在另一优选例中,所述步骤(1)中粘结剂溶液浓度为5~30%,优选地为10%。In another preferred example, the concentration of the binder solution in the step (1) is 5-30%, preferably 10%.

在另一优选例中,所述低温预热温度为80~140℃,更佳地为100~120℃。在另一优选例中,所述的烘烤时间为1~20h,更佳地为3~15h。In another preferred embodiment, the low temperature preheating temperature is 80-140°C, more preferably 100-120°C. In another preferred example, the baking time is 1-20h, more preferably 3-15h.

在另一优选例中,所述烘烤在真空环境或惰性气体保护下进行。In another preferred embodiment, the baking is performed in a vacuum environment or under the protection of an inert gas.

如本发明所述的保护结构主要与支撑结构组成负极作用于锂二次电池中。所述支撑结构选自下组:铜箔、铜网、锂箔、镍网。The protection structure according to the present invention mainly forms a negative electrode with the support structure and acts in the lithium secondary battery. The support structure is selected from the group consisting of copper foil, copper mesh, lithium foil, nickel mesh.

更具体地,在本发明中,发明人通过在铜箔、镍箔或不锈钢箔及其它不与锂金属发生合金化的金属基底集流体表面涂覆由金属氟化物/碳材料/粘结剂组成的涂层,发现可以在其被锂离子电化学还原后形成具有氟化锂框架的自支撑结构。此种结构不但容易从金属基底集流体剥离,当其置于锂金属或其它负极集流体表面后,可在电池循环过程中有效保护沉积在保护结构下方、靠集流体一侧的锂金属,隔离其与电解液的直接接触,避免副反应发生,防止锂金属枝晶生长及钝化等一系列优化电极循环效率和使用寿命的特点(所述保护结构的使用方法如图1所示意)。在0.5毫安/平方厘米的电流密度和1毫安时/平方厘米的工作条件下包含所述界面保护结构的电池可达到~98%的库伦效率和超过100周的循环寿命。同时,本发明中所述界面保护结构的制备方法简洁实效,可大批量一次性处理,具有巨大的应用潜力。More specifically, in the present invention, the inventors consist of metal fluoride/carbon material/binder by coating the surface of copper foil, nickel foil or stainless steel foil and other metal base current collectors that do not alloy with lithium metal. coating, it was found that a self-supporting structure with a lithium fluoride framework could be formed after it was electrochemically reduced by lithium ions. This structure is not only easy to peel off from the metal base current collector, but when it is placed on the surface of lithium metal or other negative current collectors, it can effectively protect the lithium metal deposited under the protective structure and on the side of the current collector during battery cycling. Its direct contact with the electrolyte avoids the occurrence of side reactions, prevents lithium metal dendrite growth and passivation and a series of characteristics to optimize the electrode cycle efficiency and service life (the usage method of the protective structure is shown in Figure 1). Cells incorporating the interface protection structure can achieve ~98% coulombic efficiency and cycle life over 100 weeks at a current density of 0.5 mA/cm2 and operating conditions of 1 mAh/cm2. At the same time, the preparation method of the interface protection structure described in the present invention is simple and effective, can be processed in large batches at one time, and has huge application potential.

典型地,所述界面保护结构直接盖在铜集流体上方,对沉积在铜集流体和保护结构之间的锂金属进行保护,同时表征锂金属在受保护铜集流体上沉积/分解过程中的库伦效率。此体系中置于隔膜另外一侧的锂金属仅作为锂源提供沉积于铜箔测的锂金属,非受保护对象。Typically, the interfacial protection structure directly caps the copper current collector, protects the lithium metal deposited between the copper current collector and the protection structure, and characterizes the deposition/decomposition of lithium metal on the protected copper current collector. Coulomb efficiency. The lithium metal placed on the other side of the separator in this system only serves as the lithium source to provide the lithium metal deposited on the copper foil, not a protected object.

应理解,在实际应用中,此保护结构也可以盖在锂金属电池中的锂金属负极上,保护锂金属与保护结构之间的锂金属界面,如示意图1所示。It should be understood that in practical applications, the protection structure can also be covered on the lithium metal negative electrode in the lithium metal battery to protect the lithium metal interface between the lithium metal and the protection structure, as shown in schematic diagram 1 .

应用application

本发明还提供了一种电池,所述电池包含所述界面保护结构。The present invention also provides a battery including the interface protection structure.

在本发明中,所述电池在锂金属沉积/分解循环100周后,其库伦效率≥60%,较佳地≥70%,更佳地≥80%,较佳地≥90%,最佳地≥95%。In the present invention, the coulombic efficiency of the battery after 100 cycles of lithium metal deposition/decomposition is ≥ 60%, preferably ≥ 70%, more preferably ≥ 80%, preferably ≥ 90%, most preferably ≥95%.

与现有技术相比,本发明具有以下主要优点:Compared with the prior art, the present invention has the following main advantages:

(1)包含所述界面保护结构的电池中,在循环过程中,所述界面保护结构能有效保护锂金属,使锂金属在沉积过程中与电解液隔离,无副反应或者只有微量副反应发生;(1) In the battery comprising the interface protection structure, during the cycle process, the interface protection structure can effectively protect the lithium metal, so that the lithium metal is isolated from the electrolyte during the deposition process, and no side reactions or only a small amount of side reactions occur. ;

(2)包含所述界面保护结构的电池中,所述界面保护结构可有效防止锂金属枝晶生长及钝化;(2) In a battery including the interface protection structure, the interface protection structure can effectively prevent the growth and passivation of lithium metal dendrites;

(3)包含所述界面保护结构的电池具有极为优异的锂金属负极循环性能,在0.5毫安/平方厘米的电流密度和1毫安时/平方厘米的工作条件下可达到~98%的库伦效率和超过100周的循环寿命;(3) The battery including the interface protection structure has extremely excellent cycle performance of lithium metal anode, and can reach ~98% coulomb under the current density of 0.5 mA/cm2 and the working condition of 1 mAh/cm2 Efficiency and cycle life of over 100 weeks;

(4)所述界面保护结构的制备方法具有工艺简单、成本低、原料易得等特点;(4) the preparation method of the interface protection structure has the characteristics of simple process, low cost, easy availability of raw materials and the like;

(5)所述保护结构在制备完成后,可直接从金属基底剥离,并植入其它锂金属电池中对锂金属负极表面进行保护,应用性较强。(5) After the protection structure is prepared, it can be directly peeled off from the metal substrate and implanted into other lithium metal batteries to protect the surface of the lithium metal negative electrode, which has strong applicability.

下面结合具体实施例,进一步阐述本发明。应理解,这些实施例仅用于说明本发明而不用于限制本发明的范围。下列实施例中未注明具体条件的实验方法,通常按照常规条件或按照制造厂商所建议的条件。除非另外说明,否则百分比和份数按重量计算。The present invention will be further described below in conjunction with specific embodiments. It should be understood that these examples are only used to illustrate the present invention and not to limit the scope of the present invention. In the following examples, the experimental methods without specific conditions are usually in accordance with conventional conditions or in accordance with the conditions suggested by the manufacturer. Percentages and parts are by weight unless otherwise indicated.

除非另行定义,文中所使用的所有专业与科学用语与本领域熟练人员所熟悉的意义相同。此外,任何与所记载内容相似或均等的方法及材料皆可应用于本发明方法中。文中所述的较佳实施方法与材料仅作示范之用。Unless otherwise defined, all professional and scientific terms used herein have the same meanings as those familiar to those skilled in the art. In addition, any methods and materials similar or equivalent to those described can be used in the methods of the present invention. Methods and materials for preferred embodiments described herein are provided for illustrative purposes only.

实施例1具有界面保护结构1的铜锂电池1Example 1 Copper-lithium battery 1 with interface protection structure 1

a、将质量比为10%的聚偏氟乙烯(PVdF)预溶于N-甲基吡咯烷酮(NMP)溶剂中,在磁力搅拌器中混合搅拌3小时,获得均匀溶液;a. Pre-dissolve polyvinylidene fluoride (PVdF) with a mass ratio of 10% in N-methylpyrrolidone (NMP) solvent, and mix and stir in a magnetic stirrer for 3 hours to obtain a uniform solution;

b、按质量比7:1:2搅拌氟化镍、特密高导电碳黑(Super-P)、聚偏氟乙烯,在混合物中加入溶剂N-甲基吡咯烷酮(NMP)并置于磁力搅拌器中混合搅拌3小时,获得前驱体材料浆料;b. Stir nickel fluoride, super conductive carbon black (Super-P) and polyvinylidene fluoride in a mass ratio of 7:1:2, add solvent N-methylpyrrolidone (NMP) to the mixture and place it under magnetic stirring Mixing and stirring in the vessel for 3 hours to obtain the precursor material slurry;

c、将前驱体材料浆料涂覆在铜箔表面(涂层厚度约为20-60μm),在真空环境中以120℃烘烤12小时;c. Coat the precursor material slurry on the surface of the copper foil (the thickness of the coating is about 20-60 μm), and bake it at 120 ° C for 12 hours in a vacuum environment;

d、将步骤c中的烘烤后极片切成直径为16mm的圆片作为具有界面保护结构前驱体的负极极片;d, cutting the pole piece after baking in step c into a circular piece with a diameter of 16 mm as a negative pole piece having an interface protection structure precursor;

e、将电解液3011R按70μL的量滴入20微米厚的聚乙烯隔膜中,并和d中获得的负极极片以及对电极金属锂片一起装入CR2032型纽扣电池壳,放入含有惰性气体的手套箱内组装得到电池。e. Drop the electrolyte 3011R into a polyethylene separator with a thickness of 20 microns in an amount of 70 μL, and put it into a CR2032 button battery case together with the negative electrode piece and the counter electrode metal lithium piece obtained in d. The battery is assembled in the glove box.

f、将e中获得的电池放电至0V进行还原,拆解电池,将电化学还原后的负极极片于空气环境中静置后,获得可剥离的界面保护结构1。f. The battery obtained in e is discharged to 0V for reduction, the battery is disassembled, and the electrochemically reduced negative electrode is allowed to stand in an air environment to obtain a peelable interface protection structure 1 .

g、将f中获得的界面保护结构1置于铜箔表面,将电解液3011R按70μL的量滴入20微米厚的聚乙烯隔膜中,以金属锂片为对电极一起装入CR2032型纽扣电池壳,获得具有界面保护结构1的铜锂电池1。g. Place the interface protection structure 1 obtained in f on the surface of the copper foil, drop the electrolyte 3011R into a polyethylene separator with a thickness of 20 microns in an amount of 70 μL, and load the CR2032 button battery with the metal lithium sheet as the counter electrode. shell to obtain a copper-lithium battery 1 with an interface protection structure 1 .

实施例2具有界面保护结构2的铜锂电池2Example 2 Copper-lithium battery 2 with interface protection structure 2

同实施例1,区别在于:在步骤b中金属氟化物为氟化锰。Same as Example 1, the difference is: in step b, the metal fluoride is manganese fluoride.

实施例3具有界面保护结构3的铜锂电池3Embodiment 3 Copper-lithium battery 3 with interface protection structure 3

同实施例1,区别在于:在步骤b中金属氟化物为氟化铁。With Embodiment 1, the difference is: in step b, the metal fluoride is iron fluoride.

实施例4具有界面保护结构4的铜锂电池4Embodiment 4 Copper-lithium battery 4 with interface protection structure 4

同实施例1,区别在于:在步骤b中氟化镍:特密高导电碳黑(Super-P):聚偏氟乙烯比例为8:1:1。Same as Example 1, the difference is: in step b, the ratio of nickel fluoride: super conductive carbon black (Super-P): polyvinylidene fluoride is 8:1:1.

实施例5具有界面保护结构5的铜锂电池5Embodiment 5 Copper-lithium battery 5 with interface protection structure 5

同实施例1,区别在于:在步骤b中碳材料为石墨烯。Same as Example 1, the difference is: in step b, the carbon material is graphene.

实施例6具有界面保护结构6的铜锂电池6Embodiment 6 Copper-lithium battery 6 with interface protection structure 6

同实施例1,区别在于:在步骤b中粘结剂为聚酰亚胺。Same as Example 1, the difference is: in step b, the binder is polyimide.

对比例1不具有界面保护结构的铜锂电池C1Comparative Example 1 Copper-lithium battery C1 without interface protection structure

a、将电解液3011R按70μL的量滴入20微米厚的聚乙烯隔膜中,以铜箔为工作电极,金属锂片为对电极一起装入CR2032型纽扣电池壳,获得不具有界面保护结构的铜锂电池C1。a. Drop the electrolyte 3011R into a 20-micron-thick polyethylene separator in an amount of 70 μL, and use copper foil as the working electrode and metal lithium sheet as the counter electrode to put it into a CR2032 button battery case to obtain a CR2032 button battery case without an interface protection structure. Copper lithium battery C1.

电化学性能测试Electrochemical performance test

在0.5毫安/平方厘米的电流密度下,对实施例1-6制得的铜锂电池1-6和对比例1制得的铜锂电池C1分别进行锂金属沉积/分解循环。循环条件为每周往铜电极上沉积1毫安时/平方厘米的锂金属,然后再将其分解,分解截止电位为0.5V。以库伦效率,即分解量/沉积量,对铜电极一侧的锂金属保护效果进行表征。At a current density of 0.5 mA/cm 2 , lithium metal deposition/decomposition cycles were performed on copper-lithium batteries 1-6 prepared in Examples 1-6 and copper-lithium battery C1 prepared in Comparative Example 1, respectively. The cycling conditions were to deposit 1 mAh/cm2 of lithium metal on the copper electrode every week, and then decompose it with a decomposition cut-off potential of 0.5 V. The lithium metal protection effect on the copper electrode side was characterized by the Coulomb efficiency, that is, the amount of decomposition/deposition.

结果如表1和图2所示。The results are shown in Table 1 and Figure 2.

表1库伦效率结果Table 1 Coulomb efficiency results

第10周Week 10 第50周Week 50 第100周Week 100 实施例1Example 1 97.55%97.55% 97.60%97.60% 97.65%97.65% 实施例2Example 2 94.39%94.39% 97.19%97.19% 81.95%81.95% 实施例3Example 3 95.75%95.75% 97.25%97.25% 68.68%68.68% 实施例4Example 4 92.36%92.36% 95.25%95.25% 90.35%90.35% 实施例5Example 5 95.90%95.90% 97.65%97.65% 97.15%97.15% 实施例6Example 6 94.4%94.4% 96.7%96.7% 90.35%90.35% 对比例1Comparative Example 1 55.66%55.66% 25.22%25.22% ----

结合图2和表1可知:在循环100周过程中,具有本发明界面保护结构的铜锂电池1-6在前50周都能维持90%以上的库伦效率,而不具备本发明所述界面保护结构的铜锂电池C1在第10周库伦效率仅为55.66%,第50周衰减至25.22%,且无法循环至100周。It can be seen from Fig. 2 and Table 1 that during the 100-cycle cycle, the copper-lithium batteries 1-6 with the interface protection structure of the present invention can maintain a coulombic efficiency of more than 90% in the first 50 weeks, but do not have the interface of the present invention. The copper-lithium battery C1 with the protective structure was only 55.66% in the 10th week, attenuated to 25.22% in the 50th week, and could not be cycled to 100 weeks.

在本发明提及的所有文献都在本申请中引用作为参考,就如同每一篇文献被单独引用作为参考那样。此外应理解,在阅读了本发明的上述讲授内容之后,本领域技术人员可以对本发明作各种改动或修改,这些等价形式同样落于本申请所附权利要求书所限定的范围。All documents mentioned herein are incorporated by reference in this application as if each document were individually incorporated by reference. In addition, it should be understood that after reading the above teaching content of the present invention, those skilled in the art can make various changes or modifications to the present invention, and these equivalent forms also fall within the scope defined by the appended claims of the present application.

Claims (11)

1.一种锂金属电池,其特征在于,所述电池包含界面保护结构;1. A lithium metal battery, wherein the battery comprises an interface protection structure; 所述界面保护结构是如下制备的:The interface protection structure is prepared as follows: i)提供界面保护结构前驱体材料的负极材料、电解液、隔膜、锂电极片;i) Anode materials, electrolytes, separators, and lithium electrode sheets that provide interface protection structure precursor materials; ii)以所述负极材料、所述电解液、所述隔膜和所述锂电极片组装电池;ii) assembling a battery with the negative electrode material, the electrolyte, the separator and the lithium electrode sheet; iii)电化学还原处理步骤ii)所得电池,拆解所得电池,即可从所得负极上剥离得到所述界面保护结构;iii) The battery obtained in the electrochemical reduction treatment step ii) is disassembled, and the interface protection structure can be obtained by peeling off the obtained negative electrode; 所述界面保护结构前驱体材料是如下制备的:The interface protection structure precursor material is prepared as follows: 1)提供一混合浆料,所述混合浆料包含:金属氟化物、碳材料、粘结剂和溶剂;1) Provide a mixed slurry, the mixed slurry includes: metal fluoride, carbon material, binder and solvent; 2)将所述混合浆料涂覆于金属基底表面,得到含第一涂层的金属基底;2) coating the mixed slurry on the surface of the metal substrate to obtain a metal substrate containing the first coating; 3)烘烤处理所述含第一涂层的金属基底,得到含第二涂层的金属基底,所述第二涂层即所述界面保护结构前驱体材料;3) baking the metal substrate containing the first coating to obtain a metal substrate containing a second coating, where the second coating is the precursor material of the interface protection structure; 所述电化学还原处理是指:将所述电池放电至0V;The electrochemical reduction treatment refers to: discharging the battery to 0V; 经所述电化学还原处理所得界面保护结构具有氟化锂框架;The interface protection structure obtained by the electrochemical reduction treatment has a lithium fluoride framework; 所述电池还包含正极材料、负极材料、电解液和隔膜;The battery also includes a positive electrode material, a negative electrode material, an electrolyte and a separator; 所述界面保护结构位于所述负极材料和所述隔膜材料之间。The interface protection structure is located between the negative electrode material and the separator material. 2.如权利要求1所述电池,其特征在于,所述负极材料为所述界面保护结构的支撑材料。2 . The battery of claim 1 , wherein the negative electrode material is a support material of the interface protection structure. 3 . 3.如权利要求1所述电池,其特征在于,所述负极材料选自下组:铜箔、铜网、锂箔、镍网、铝箔、铝网、或其组合。3. The battery of claim 1, wherein the negative electrode material is selected from the group consisting of copper foil, copper mesh, lithium foil, nickel mesh, aluminum foil, aluminum mesh, or a combination thereof. 4.如权利要求1所述电池,其特征在于,所述金属氟化物选自下组:氟化镍、氟化锰、氟化铁、氟化钛、氟化铜、氟化锡、或其组合;和/或4. The battery of claim 1, wherein the metal fluoride is selected from the group consisting of nickel fluoride, manganese fluoride, iron fluoride, titanium fluoride, copper fluoride, tin fluoride, or its combination; and/or 所述碳材料选自下组:特密高导电碳黑、石墨烯、科琴黑、乙炔黑、碳纳米管、或其组合;和/或The carbon material is selected from the group consisting of ultra-conductive carbon black, graphene, Ketjen black, acetylene black, carbon nanotubes, or a combination thereof; and/or 所述粘结剂选自下组:聚偏氟乙烯、聚酰亚胺、叔苯丁基橡胶、聚丙烯腈、聚丙烯酸酯、海藻酸钠、或其组合。The binder is selected from the group consisting of polyvinylidene fluoride, polyimide, t-phenylbutyl rubber, polyacrylonitrile, polyacrylate, sodium alginate, or a combination thereof. 5.如权利要求1所述电池,其特征在于,所述混合浆料中,所述金属氟化物、所述碳材料和所述粘结剂的质量比为5-12:1-3:1-5。5 . The battery of claim 1 , wherein in the mixed slurry, the mass ratio of the metal fluoride, the carbon material and the binder is 5-12:1-3:1 5 . -5. 6.如权利要求1所述电池,其特征在于,所述烘烤处理的处理温度为60-160℃;和/或6 . The battery according to claim 1 , wherein the processing temperature of the baking treatment is 60-160° C.; and/or 所述烘烤处理在所述处理温度下的处理时间为1-20h。The treatment time of the baking treatment at the treatment temperature is 1-20 h. 7.如权利要求1所述电池,其特征在于,所述电池在锂金属沉积/分解循环100周后,其库伦效率≥60%。7. The battery of claim 1, wherein the battery has a coulombic efficiency of ≥60% after 100 cycles of lithium metal deposition/decomposition cycles. 8.如权利要求1所述电池,其特征在于,所述电池在锂金属沉积/分解循环100周后,其库伦效率≥70%。8. The battery of claim 1, wherein the battery has a coulombic efficiency of ≥70% after 100 cycles of lithium metal deposition/decomposition cycles. 9.如权利要求1所述电池,其特征在于,所述电池在锂金属沉积/分解循环100周后,其库伦效率≥80%。9 . The battery of claim 1 , wherein the battery has a coulombic efficiency of ≥80% after 100 cycles of lithium metal deposition/decomposition cycles. 10 . 10.如权利要求1所述电池,其特征在于,所述电池在锂金属沉积/分解循环100周后,其库伦效率≥90%。10. The battery of claim 1, wherein the battery has a coulombic efficiency of ≥90% after 100 cycles of lithium metal deposition/decomposition cycles. 11.如权利要求1所述电池,其特征在于,所述电池在锂金属沉积/分解循环100周后,其库伦效率≥95%。11. The battery of claim 1, wherein the battery has a coulombic efficiency > 95% after 100 cycles of lithium metal deposition/decomposition cycles.
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