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CN114242956B - Polymer negative electrode protective layer and preparation method and application thereof - Google Patents

Polymer negative electrode protective layer and preparation method and application thereof Download PDF

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CN114242956B
CN114242956B CN202111390102.5A CN202111390102A CN114242956B CN 114242956 B CN114242956 B CN 114242956B CN 202111390102 A CN202111390102 A CN 202111390102A CN 114242956 B CN114242956 B CN 114242956B
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lithium
negative electrode
protective layer
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stirring
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CN114242956A (en
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崔志明
罗飘
李威
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South China University of Technology SCUT
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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
    • H01M4/13Electrodes for accumulators with non-aqueous electrolyte, e.g. for lithium-accumulators; Processes of manufacture thereof
    • H01M4/139Processes of manufacture
    • H01M4/1395Processes of manufacture of electrodes 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
    • 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
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    • H01M12/06Hybrid cells; Manufacture thereof composed of a half-cell of the fuel-cell type and of a half-cell of the primary-cell type with one metallic and one gaseous electrode
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
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    • H01M4/13Electrodes for accumulators with non-aqueous electrolyte, e.g. for lithium-accumulators; Processes of manufacture thereof
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    • HELECTRICITY
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    • H01M4/02Electrodes composed of, or comprising, active material
    • H01M4/36Selection of substances as active materials, active masses, active liquids
    • H01M4/60Selection of substances as active materials, active masses, active liquids of organic compounds
    • H01M4/602Polymers
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    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
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    • H01M4/02Electrodes composed of, or comprising, active material
    • H01M2004/026Electrodes composed of, or comprising, active material characterised by the polarity
    • H01M2004/027Negative 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
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Abstract

The invention belongs to the technical field of electrochemical energy, and discloses a polymer negative electrode protective layer, a preparation method and application thereof; according to the invention, a lithium source and a polystyrene sulfonic acid solution are mixed and stirred to obtain a gel solution 1; adding N-methyl pyrrolidone into the gel solution 1, and stirring to obtain gel solution 2; adding poly (vinylidene fluoride-co-hexafluoropropylene) and solid thermoplastic polyurethane rubber into the gel solution 2, and uniformly stirring to obtain a gel solution 3; and (3) coating the gel liquid 3 on the pole piece, and drying the pole piece to obtain the polymer negative electrode protective layer. And carrying out lithium precipitation operation on the polymer negative electrode protective layer to obtain the metal lithium electrode. The preparation method of the polymer negative electrode protective layer has the advantages of simplicity, convenience in control, high yield, easiness in industrialization and the like. The prepared metallic lithium negative electrode plate with the high-toughness and fast ion conduction interface transmission layer has good electrochemical performance in the application aspect of lithium metal batteries.

Description

一种聚合物负极保护层及其制备方法与应用A kind of polymer negative electrode protection layer and its preparation method and application

技术领域technical field

本发明属于电化学能源技术领域,具体涉及一种聚合物负极保护层及其制备方法与应用。The invention belongs to the technical field of electrochemical energy, and in particular relates to a polymer negative electrode protection layer and a preparation method and application thereof.

背景技术Background technique

伴随着能源行业的不断发展,人类对于储能器件高能量密度的需求也在日渐增长。高效的能源存储和转换是科技发展的动力,电池的出现能够帮助我们可以更加高效和便捷地利用能源。自上世纪以来,多种电池形式已经实现了商业应用,如:铅酸电池、镍镉电池、镍氢电池以及锂离子电池等。锂离子电池的出现改变了人们的生活方式,促进了便携式摄像机、手机、笔记本电脑以及电动汽车等领域的快速发展。With the continuous development of the energy industry, the human demand for high energy density of energy storage devices is also increasing. Efficient energy storage and conversion is the driving force for the development of science and technology, and the emergence of batteries can help us use energy more efficiently and conveniently. Since the last century, various battery forms have achieved commercial applications, such as: lead-acid batteries, nickel-cadmium batteries, nickel-metal hydride batteries, and lithium-ion batteries. The emergence of lithium-ion batteries has changed people's lifestyles and promoted the rapid development of camcorders, mobile phones, notebook computers, and electric vehicles.

然而,尽管锂离子电池有着迅速的发展,但是这些商用电池的能量密度却增长缓慢。在过去的150年里,电池的能量密度仅从过去铅酸电池的40Wh·kg-1提高到目前锂离子电池的200Wh·kg-1。这样的增长速度远远无法满足人们对于能源的需求。随着锂离子电池中石墨负极的实际能量密度逐渐接近于其理论极限值,我们迫切需要更加高效的电极材料以满足新兴的高端储能器件发展的需求。However, despite the rapid development of lithium-ion batteries, the energy density of these commercial batteries has been increasing slowly. In the past 150 years, the energy density of batteries has only increased from 40Wh·kg -1 of lead-acid batteries in the past to 200Wh·kg -1 of lithium-ion batteries at present. This growth rate is far from meeting people's demand for energy. As the actual energy density of graphite anodes in lithium-ion batteries is gradually approaching its theoretical limit, we urgently need more efficient electrode materials to meet the needs of emerging high-end energy storage devices.

锂金属负极以其极高的理论容量(3860mAh·g-1)和最低(负)的电势(-3.04Vvs标准氢电极)而被广泛的认为是最有希望的锂离子负极材料,受到了研究人员的极大关注。目前,以金属锂作为负极的锂金属电池主要有:锂-硫电池、锂-空气电池和锂-氧化物电池,这些新型电池均表现出了很高的理论能量密度(锂-空气电池:3500Wh·kg-1,锂-硫电池:2600Wh·kg-1,锂-氧化物电池:1000-1500Wh·kg-1。因此,以金属锂为负极的锂金属电池很有可能成为下一代储能电池。但是,这些金属锂电池存在严重的安全问题(锂枝晶生长),难以稳定循环。锂枝晶生长会导致电池短路,进而可能造成热失控,引发着火、甚至爆炸的风险。这个问题直接导致锂金属二次电池无法实现商业应用。自从锂离子电池商业应用之后,大部分锂金属电池产品都被市场抛弃。然而,作为一种具有极高能量密度的负极材料,研究人员对金属锂的探索从来都没有停止过。近年来,人们开发出了多种新兴策略来抑制金属锂负极的锂枝晶生长,从而提高电池的安全性和使用寿命,以期待其最终的实际应用。Lithium metal anode is widely regarded as the most promising lithium ion anode material due to its extremely high theoretical capacity (3860mAh·g -1 ) and lowest (negative) potential (-3.04Vvs standard hydrogen electrode), and has been studied great attention from personnel. At present, lithium metal batteries using metal lithium as the negative electrode mainly include: lithium-sulfur batteries, lithium-air batteries and lithium-oxide batteries, and these new batteries have shown high theoretical energy densities (lithium-air batteries: 3500Wh kg -1 , lithium-sulfur battery: 2600Wh kg -1 , lithium-oxide battery: 1000-1500Wh kg -1 . Therefore, lithium metal batteries with metal lithium as the negative electrode are likely to become the next generation of energy storage batteries However, these metal lithium batteries have serious safety problems (lithium dendrite growth) and are difficult to cycle stably. The growth of lithium dendrites will cause short circuits in the battery, which may cause thermal runaway, triggering the risk of fire or even explosion. This problem directly leads to Lithium metal secondary batteries cannot be used commercially. Since the commercial application of lithium ion batteries, most lithium metal battery products have been abandoned by the market. However, as a negative electrode material with extremely high energy density, researchers have explored lithium metal It has never stopped. In recent years, various emerging strategies have been developed to suppress the lithium dendrite growth of metallic lithium anodes, thereby improving the safety and service life of batteries, in anticipation of their eventual practical applications.

利用界面传输层作为金属锂负极的保护层是一种非常有效的方法,能够减少金属锂沉积过程中与电解液所产生的副反应,并且能够有效地抑制锂枝晶的生长。(D.Luo,L.Zheng,Z.Zhang,M.Li,Z.Chen,R.Cui,Y.Shen,G.Li,R.Feng,S.Zhang,G.Jiang,L.Chen,A.Yu,X.Wang,Nat.Commun.2021,12,186.)然而,金属锂沉积过程中的离子传输速度及离子传输均匀性是金属锂沉积均匀的关键,同时由于金属锂沉积过程中会发生体积膨胀,并且易与电解液发生不可逆的副反应,目前对于金属锂界面传输层的研究并不充分。因此金属锂负极界面传输层材料需要更加深入的研究。Utilizing the interfacial transport layer as the protective layer of the metal lithium negative electrode is a very effective method, which can reduce the side reaction with the electrolyte during the metal lithium deposition process, and can effectively inhibit the growth of lithium dendrites. (D. Luo, L. Zheng, Z. Zhang, M. Li, Z. Chen, R. Cui, Y. Shen, G. Li, R. Feng, S. Zhang, G. Jiang, L. Chen, A. .Yu,X.Wang,Nat.Commun.2021,12,186.) However, the ion transport speed and uniformity of ion transport during metal lithium deposition are the key to the uniform deposition of metal lithium. Swelling, and easy to have irreversible side reactions with the electrolyte, the current research on the metal lithium interface transport layer is not sufficient. Therefore, the interfacial transport layer materials for lithium metal anode need more in-depth research.

发明内容Contents of the invention

为了克服现有技术存在的上述不足,本发明的目的是提供一种具有高韧性、快离子传导聚合物负极保护层制备方法,旨在调控其集流体表面的离子传输速度、限制金属锂生长范围、抑制金属锂枝晶的形成。In order to overcome the above-mentioned deficiencies in the prior art, the object of the present invention is to provide a method for preparing a high-toughness, fast ion-conducting polymer negative electrode protective layer, which aims to regulate the ion transmission speed on the surface of the current collector and limit the growth range of metal lithium , Inhibit the formation of metallic lithium dendrites.

本发明通过设计、构建快离子传输层的方法制备金属锂复合负极电极。The invention prepares the lithium metal composite negative electrode through the method of designing and constructing the fast ion transport layer.

本发明根据离子界面传输层的性质特点,首次通过利用含聚苯乙烯磺酸、偏二氟乙烯-co-六氟丙烯、热塑性聚氨酯材料制备出具有高韧性、快离子传导特点的聚合物负极保护层,并制备出复合金属锂负极电极。According to the properties and characteristics of the ion interface transport layer, the present invention for the first time prepares a polymer negative electrode protection with high toughness and fast ion conduction characteristics by using polystyrene sulfonic acid, vinylidene fluoride-co-hexafluoropropylene, and thermoplastic polyurethane materials. layer, and prepared a composite metal lithium negative electrode.

本发明的目的至少通过如下技术方案之一实现。The object of the present invention is achieved at least by one of the following technical solutions.

一种具有高韧性、快离子传导聚合物负极保护层的制备方法,包括如下步骤:A preparation method with high toughness and fast ion-conducting polymer negative electrode protective layer, comprising the steps of:

(1)将锂源和聚苯乙烯磺酸溶液混合,搅拌处理,得到凝胶液1凝胶状液体);(1) mix lithium source and polystyrene sulfonic acid solution, stir and process, obtain gel liquid 1 gel-like liquid);

(2)在步骤(1)所述凝胶液1中加入N-甲基吡咯烷酮(NMP),搅拌处理,得到凝胶液2;(2) Add N-methylpyrrolidone (NMP) into the gel solution 1 described in step (1), and stir to obtain the gel solution 2;

(3)将聚(偏二氟乙烯-co-六氟丙烯)(PVDF-HFP)和固体热塑性聚氨酯橡胶(TPU)加入步骤(2)所述凝胶液2中,搅拌均匀,得到凝胶液3;(3) Add poly(vinylidene fluoride-co-hexafluoropropylene) (PVDF-HFP) and solid thermoplastic polyurethane rubber (TPU) into the gel solution 2 described in step (2), and stir evenly to obtain the gel solution 3;

(4)将步骤(3)所述凝胶液3在极片上进行涂布处理,所得极片烘干处理,得到聚合物负极保护层。(4) Coating the gel solution 3 described in step (3) on the pole piece, and drying the obtained pole piece to obtain a polymer negative electrode protective layer.

优选的,步骤(1)所述聚苯乙烯磺酸溶液的质量百分比浓度为5%-40%;所述聚苯乙烯磺酸溶液是由聚苯乙烯磺酸和水混合均匀得到的溶液。Preferably, the mass percent concentration of the polystyrene sulfonic acid solution in step (1) is 5%-40%; the polystyrene sulfonic acid solution is a solution obtained by uniformly mixing polystyrene sulfonic acid and water.

进一步优选的,所述聚苯乙烯磺酸溶液的质量百分比浓度为30%;Further preferably, the mass percent concentration of the polystyrene sulfonic acid solution is 30%;

优选的,步骤(1)所述锂源与聚苯乙烯磺酸的摩尔比为(1:1)-(3:1);Preferably, the mol ratio of lithium source and polystyrenesulfonic acid described in step (1) is (1:1)-(3:1);

进一步优选的,所述锂源与聚苯乙烯磺酸的摩尔比为1:1;Further preferably, the molar ratio of the lithium source to polystyrene sulfonic acid is 1:1;

优选的,步骤(1)所述锂源为LiCl、LiOH、Li2CO3、LiF、LiNO3、LiTFSI及LiFSI中的一种以上;Preferably, the lithium source in step (1) is more than one of LiCl, LiOH, Li 2 CO 3 , LiF, LiNO 3 , LiTFSI and LiFSI;

进一步优选的,所述锂源为LiOH·H2O。Further preferably, the lithium source is LiOH·H 2 O.

优选的,步骤(1)所述搅拌处理的时间为30-90min,温度为常温。Preferably, the time for the stirring treatment in step (1) is 30-90 min, and the temperature is normal temperature.

进一步优选的,所述搅拌处理的时间为60min。Further preferably, the time for the stirring treatment is 60 minutes.

优选的,步骤(2)所述N-甲基吡咯烷酮与步骤(1)所述凝胶液1的体积比为(5:1)-(20:1);Preferably, the volume ratio of N-methylpyrrolidone in step (2) to gel solution 1 in step (1) is (5:1)-(20:1);

进一步优选的,所述N-甲基吡咯烷酮与步骤(1)所述凝胶液1的体积比为10:1;Further preferably, the volume ratio of the N-methylpyrrolidone to the gel solution 1 in step (1) is 10:1;

优选的,步骤(2)所述搅拌处理的时间为30-90min。Preferably, the stirring treatment time in step (2) is 30-90min.

进一步优选的,所述搅拌处理的时间为60min。Further preferably, the time for the stirring treatment is 60 minutes.

优选的,步骤(3)所述聚(偏二氟乙烯-co-六氟丙烯)与固体热塑性聚氨酯橡胶的质量比为(1:10)-(10:1);Preferably, the mass ratio of poly(vinylidene fluoride-co-hexafluoropropylene) to solid thermoplastic polyurethane rubber in step (3) is (1:10)-(10:1);

进一步优选的,所述聚(偏二氟乙烯-co-六氟丙烯)与固体热塑性聚氨酯橡胶的质量比为2:1;Further preferably, the mass ratio of poly(vinylidene fluoride-co-hexafluoropropylene) to solid thermoplastic polyurethane rubber is 2:1;

优选的,步骤(3)所述聚(偏二氟乙烯-co-六氟丙烯)与固体热塑性聚氨酯橡胶的总质量与步骤(1)所述的凝胶液1的质量比为(1:1)-(10:1)。Preferably, the mass ratio of the total mass of poly(vinylidene fluoride-co-hexafluoropropylene) and solid thermoplastic polyurethane rubber to the gel solution 1 described in step (1) in step (3) is (1:1 )-(10:1).

进一步优选的,所述聚(偏二氟乙烯-co-六氟丙烯)与固体热塑性聚氨酯橡胶的总质量与步骤(1)所述的凝胶液1的质量比为9:1。Further preferably, the mass ratio of the total mass of poly(vinylidene fluoride-co-hexafluoropropylene) and solid thermoplastic polyurethane rubber to the gel solution 1 described in step (1) is 9:1.

优选的,步骤(3)所述搅拌在常温状态下搅拌,搅拌的时间为6-20h。Preferably, the stirring in step (3) is carried out at room temperature, and the stirring time is 6-20 hours.

进一步优选的,所述搅拌的时间为12h。Further preferably, the stirring time is 12 hours.

优选的,步骤(4)所述的涂布处理是利用5-30μm的涂布器进行涂布;Preferably, the coating treatment described in step (4) utilizes a 5-30 μm coater for coating;

进一步优选的,所述的涂布处理是利用25μm的涂布器进行涂布;Further preferably, the coating process is performed using a 25 μm coater;

优选的,步骤(4)所述的烘干处理的温度为30-90℃,烘干时间为3-12h。Preferably, the temperature of the drying treatment in step (4) is 30-90° C., and the drying time is 3-12 hours.

进一步优选的,所述的烘干处理的温度为50℃,烘干时间为6h。Further preferably, the temperature of the drying treatment is 50° C., and the drying time is 6 hours.

上述的制备方法制备得到的聚合物负极保护层。The polymer negative electrode protective layer prepared by the above preparation method.

上述的聚合物负极保护层在制备金属锂电极中的应用。Application of the above-mentioned polymer negative electrode protective layer in the preparation of metal lithium electrodes.

优选的,将所述聚合物负极保护层沉锂操作,得到金属锂电极。Preferably, the polymer negative electrode protective layer is deposited into lithium to obtain a metal lithium electrode.

进一步优选的,所述沉锂操作是将聚合物负极保护层组装在扣式电池中进行的沉锂操作。Further preferably, the lithium sinking operation is a lithium sinking operation performed by assembling a polymer negative electrode protective layer in a button battery.

本发明提供的具有高韧性、快离子传导聚合物负极保护层的金属锂负极可以直接用作金属锂负极。The lithium metal negative electrode with high toughness and fast ion-conducting polymer negative electrode protective layer provided by the present invention can be directly used as the lithium metal negative electrode.

与现有技术相比,本发明具有如下优点和有益效果:Compared with the prior art, the present invention has the following advantages and beneficial effects:

本发明制备的具有高韧性、快离子传导聚合物负极保护层和金属锂负极,可以有效抑制金属枝晶生成,大幅减少金属锂与电解液的副反应。此方法易合成,重复性好,得到的电极材料可以直接用作无枝晶、高库伦效率的金属锂电池。The high-toughness, fast ion-conducting polymer negative electrode protective layer and metal lithium negative electrode prepared by the invention can effectively inhibit the formation of metal dendrites and greatly reduce the side reaction between metal lithium and electrolyte. This method is easy to synthesize and has good repeatability, and the obtained electrode material can be directly used as a metal lithium battery with no dendrites and high Coulombic efficiency.

附图说明Description of drawings

图1为实施例1制备的金属锂电极的极化曲线;Fig. 1 is the polarization curve of the metal lithium electrode prepared in embodiment 1;

图2为实施例1制备的金属锂电极极化前后的阻抗测试曲线;Fig. 2 is the impedance test curve before and after the polarization of the metal lithium electrode prepared in embodiment 1;

图3为实施例1制备的金属锂电极的锂对称电池循环图;Fig. 3 is the lithium symmetric cell cycle diagram of the metal lithium electrode prepared in embodiment 1;

图4为实施例1制备的金属锂电极的电极表面SEM测试图;Fig. 4 is the electrode surface SEM test figure of the metal lithium electrode prepared in embodiment 1;

图5为实施例2制备的金属锂电极的极化曲线;Fig. 5 is the polarization curve of the metal lithium electrode prepared in embodiment 2;

图6为实施例2制备的金属锂电极极化前后的阻抗测试曲线;Fig. 6 is the impedance test curve before and after the polarization of the metal lithium electrode prepared in embodiment 2;

图7为实施例2制备的金属锂电极的锂对称电池循环图;Fig. 7 is the lithium symmetric cell cycle diagram of the metal lithium electrode prepared in embodiment 2;

图8为实施例2制备的金属锂电极的电极表面SEM测试图;Fig. 8 is the electrode surface SEM test figure of the metal lithium electrode prepared in embodiment 2;

图9为实施例3制备的金属锂电极的极化曲线;Fig. 9 is the polarization curve of the metal lithium electrode prepared in embodiment 3;

图10为实施例3制备的金属锂电极极化前后的阻抗测试曲线;Fig. 10 is the impedance test curve before and after polarization of the metal lithium electrode prepared in embodiment 3;

图11为实施例3制备的金属锂电极的锂对称电池循环图;Fig. 11 is the lithium symmetric battery cycle diagram of the metal lithium electrode prepared in embodiment 3;

图12为实施例3制备的金属锂电极的电极表面SEM测试图;Fig. 12 is the electrode surface SEM test figure of the metal lithium electrode prepared in embodiment 3;

图13为实施例4制备的金属锂电极的极化曲线;Fig. 13 is the polarization curve of the metal lithium electrode prepared in embodiment 4;

图14为实施例4制备的金属锂电极极化前后的阻抗测试曲线;Fig. 14 is the impedance test curve before and after the polarization of the metal lithium electrode prepared in embodiment 4;

图15为实施例4制备的金属锂电极的锂对称电池循环图;Figure 15 is a lithium symmetric battery cycle diagram of the metal lithium electrode prepared in Example 4;

图16为实施例4制备的金属锂电极的电极表面SEM测试图。16 is an SEM test image of the electrode surface of the metal lithium electrode prepared in Example 4.

具体实施方式Detailed ways

以下结合实例对本发明的具体实施作进一步说明,但本发明的实施和保护不限于此。需指出的是,以下若有未特别详细说明之过程,均是本领域技术人员可参照现有技术实现或理解的。所用试剂或仪器未注明生产厂商者,视为可以通过市售购买得到的常规产品。The specific implementation of the present invention will be further described below in conjunction with examples, but the implementation and protection of the present invention are not limited thereto. It should be pointed out that, if there are any processes in the following that are not specifically described in detail, those skilled in the art can realize or understand with reference to the prior art. The reagents or instruments used were not indicated by the manufacturer, and they were regarded as conventional products that can be purchased from the market.

实施例1Example 1

一种具有高韧性、快离子传导聚合物负极保护层和金属锂电极的制备方法,包括如下步骤:A preparation method with high toughness, fast ion-conducting polymer negative electrode protective layer and metal lithium electrode, comprising the steps of:

称取1mol的30wt.%聚苯乙烯磺酸溶液和1mol的LiOH,在常温下搅拌1h待反应完全后加入3.5mL的NMP,继续在室温下搅拌,搅拌的时间为30min,至完全反应并形成水凝胶溶液。然后将6mol的PVDF-HFP加入上述溶液中并继续搅拌12h,搅拌均匀后,继续加入3mol的TPU搅拌6h。待处理完毕后,然后将得到的浆液在铜箔上进行涂布处理,涂布器的厚度设置为30μm,然后将涂布后的极片放置于烘箱中进行烘干处理,烘干条件为60℃,6h。然后将得到的极片组装在R2032型扣式电池中进行沉锂操作,最终,得到所述具有高韧性、快离子传导人工SEI(负极保护层)的金属锂电极。如图1,图2和图3所示,根据电化学测试得到的金属锂负极材料具有较低的电阻和较高的离子迁移数,在计量化锂对称电池中表现出优秀的金属锂可逆使用;SEM图显示极片边表面的离子传导层非常平整、均匀(如图4示)。Weigh 1 mol of 30wt.% polystyrene sulfonic acid solution and 1 mol of LiOH, stir at room temperature for 1 h, add 3.5 mL of NMP after the reaction is complete, and continue stirring at room temperature for 30 min until complete reaction and formation of Hydrogel solution. Then add 6 mol of PVDF-HFP into the above solution and continue to stir for 12 hours. After stirring evenly, continue to add 3 mol of TPU and stir for 6 hours. After the treatment is completed, the obtained slurry is then coated on the copper foil. The thickness of the coater is set to 30 μm, and then the coated pole piece is placed in an oven for drying treatment. The drying condition is 60 ℃, 6h. Then, the obtained pole piece was assembled in an R2032 type button battery for lithium sinking operation, and finally, the metal lithium electrode with high toughness and fast ion conduction artificial SEI (negative electrode protective layer) was obtained. As shown in Figure 1, Figure 2 and Figure 3, the metal lithium anode material obtained according to the electrochemical test has a lower resistance and a higher ion migration number, and shows excellent reversible use of metal lithium in metered lithium symmetric batteries ; The SEM image shows that the ion-conducting layer on the edge surface of the pole piece is very smooth and uniform (as shown in Figure 4).

实施例2Example 2

一种具有高韧性、快离子传导聚合物负极保护层和金属锂电极的制备方法,包括如下步骤:A preparation method with high toughness, fast ion-conducting polymer negative electrode protective layer and metal lithium electrode, comprising the steps of:

称取1mol的30wt.%聚苯乙烯磺酸溶液和1mol的LiOH,在常温下搅拌1h待反应完全后加入3.5mL的NMP,继续在室温下搅拌,搅拌的时间为30min,至完全反应并形成水凝胶溶液。然后将4.5mol的PVDF-HFP加入上述溶液中并继续搅拌6h,搅拌均匀后,继续加入4.5mol的TPU搅拌6h。待处理完毕后,然后将得到的浆液进行涂布处理,涂布器的厚度设置为30μm,然后将涂布后的极片放置于烘箱中进行烘干处理,烘干条件为60℃,6h。然后将得到的极片组装在R2032型扣式电池中进行沉锂操作,最终,得到所述具有高韧性、快离子传导界面传输层的金属锂电极。如图5,图6和图7所示,根据电化学测试得到的金属锂负极材料具有较低的电阻和较高的离子迁移数,在计量化锂对称电池中表现出优秀的金属锂可逆使用;SEM图显示极片边表面的离子传导层非常平整、均匀(如图8所示)。Weigh 1 mol of 30wt.% polystyrene sulfonic acid solution and 1 mol of LiOH, stir at room temperature for 1 h, add 3.5 mL of NMP after the reaction is complete, and continue stirring at room temperature for 30 min until complete reaction and formation of Hydrogel solution. Then add 4.5mol of PVDF-HFP into the above solution and continue to stir for 6h, after stirring evenly, continue to add 4.5mol of TPU and stir for 6h. After the treatment is completed, the obtained slurry is then coated. The thickness of the coater is set to 30 μm, and then the coated pole piece is placed in an oven for drying treatment. The drying condition is 60° C. for 6 hours. Then, the obtained pole piece was assembled in an R2032 type button battery for lithium sinking operation, and finally, the metal lithium electrode with high toughness and fast ion-conducting interfacial transport layer was obtained. As shown in Figure 5, Figure 6 and Figure 7, the metal lithium anode material obtained according to the electrochemical test has a lower resistance and a higher ion migration number, and shows excellent reversible use of metal lithium in metered lithium symmetric batteries ; The SEM image shows that the ion-conducting layer on the edge surface of the pole piece is very smooth and uniform (as shown in Figure 8).

实施例3Example 3

一种具有高韧性、快离子传导聚合物负极保护层和金属锂电极的制备方法,包括如下步骤:A preparation method with high toughness, fast ion-conducting polymer negative electrode protective layer and metal lithium electrode, comprising the steps of:

称取1mol的30wt.%聚苯乙烯磺酸溶液和1mol的LiOH,在常温下搅拌1h待反应完全后加入3.5mL的NMP,继续在室温下搅拌,搅拌的时间为30min,至完全反应并形成水凝胶溶液。然后将3mol的PVDF-HFP加入上述溶液中并继续搅拌6h,搅拌均匀后,继续加入6mol的TPU搅拌6h。待处理完毕后,然后将得到的浆液进行涂布处理,涂布器的厚度设置为30μm,然后将涂布后的极片放置于烘箱中进行烘干处理,烘干条件为60℃,6h。然后将得到的极片组装在R2032型扣式电池中进行沉锂操作,最终,得到所述具有高韧性、快离子传导界面传输层的金属锂电极。如图9,图10和图11所示,根据电化学测试得到的金属锂负极材料具有较低的电阻和较高的离子迁移数,在计量化锂对称电池中表现出优秀的金属锂可逆使用;SEM图显示极片边表面的离子传导层非常平整、均匀(如图12所示)。Weigh 1 mol of 30wt.% polystyrene sulfonic acid solution and 1 mol of LiOH, stir at room temperature for 1 h, add 3.5 mL of NMP after the reaction is complete, and continue stirring at room temperature for 30 min until complete reaction and formation of Hydrogel solution. Then add 3 mol of PVDF-HFP into the above solution and continue to stir for 6 hours. After stirring evenly, continue to add 6 mol of TPU and stir for 6 hours. After the treatment is completed, the obtained slurry is then coated. The thickness of the coater is set to 30 μm, and then the coated pole piece is placed in an oven for drying treatment. The drying condition is 60° C. for 6 hours. Then, the obtained pole piece was assembled in an R2032 type button battery for lithium sinking operation, and finally, the metal lithium electrode with high toughness and fast ion-conducting interfacial transport layer was obtained. As shown in Figure 9, Figure 10 and Figure 11, the metal lithium anode material obtained according to the electrochemical test has a lower resistance and a higher ion migration number, and exhibits excellent reversible use of metal lithium in metered lithium symmetric batteries ; The SEM image shows that the ion-conducting layer on the edge surface of the pole piece is very smooth and uniform (as shown in Figure 12).

实施例4Example 4

一种聚合物负极保护层和金属锂电极的制备方法,包括如下步骤:A preparation method of a polymer negative electrode protective layer and a lithium metal electrode, comprising the steps of:

将4.5mol的PVDF-HFP加入3.5mL的NMP,继续在室温下搅拌,搅拌的时间为30min,至完全反应并形成水凝胶溶液。然后,搅拌均匀后,继续加入4.5mol的TPU搅拌6h。待处理完毕后,然后将得到的浆液进行涂布处理,涂布器的厚度设置为30μm,然后将涂布后的极片放置于烘箱中进行烘干处理,烘干条件为60℃,6h。然后将得到的极片组装在R2032型扣式电池中进行沉锂操作,最终,得到所述具有高韧性、快离子传导界面传输层的金属锂电极。如图13,图14和图15所示,根据电化学测试得到的金属锂负极材料具有较高的电阻和较低的离子迁移数,在计量化锂对称电池中表现出较差的金属锂可逆使用;SEM图显示极片边表面的离子传导层不均匀(如图16所示)。Add 4.5 mol of PVDF-HFP to 3.5 mL of NMP, and continue to stir at room temperature for 30 min until the reaction is complete and a hydrogel solution is formed. Then, after stirring evenly, continue to add 4.5mol of TPU and stir for 6h. After the treatment is completed, the obtained slurry is then coated. The thickness of the coater is set to 30 μm, and then the coated pole piece is placed in an oven for drying treatment. The drying condition is 60° C. for 6 hours. Then, the obtained pole piece was assembled in an R2032 type button battery for lithium sinking operation, and finally, the metal lithium electrode with high toughness and fast ion-conducting interfacial transport layer was obtained. As shown in Fig. 13, Fig. 14 and Fig. 15, the metal lithium anode material obtained according to the electrochemical test has higher resistance and lower ion migration number, and shows poor metal lithium reversibility in metered lithium symmetric batteries. Use; The SEM image shows that the ion-conducting layer on the edge surface of the pole piece is uneven (as shown in Figure 16).

上述实施例为本发明较佳的实施方式,但本发明的实施方式并不受上述实施例的限制,其它的任何未背离本发明的精神实质与原理下所作的改变、修饰、替代、组合、简化,均应为等效的置换方式,都包含在本发明的保护范围之内。The above-mentioned embodiment is a preferred embodiment of the present invention, but the embodiment of the present invention is not limited by the above-mentioned embodiment, and any other changes, modifications, substitutions, combinations, Simplifications should be equivalent replacement methods, and all are included in the protection scope of the present invention.

Claims (9)

1. The preparation method of the polymer negative electrode protective layer is characterized by comprising the following steps of:
(1) Mixing a lithium source with a polystyrene sulfonic acid solution, and stirring to obtain a gel solution 1; the mass percentage concentration of the polystyrene sulfonic acid solution is 5% -40%;
(2) Adding N-methyl pyrrolidone into the gel liquid 1 in the step (1), and stirring to obtain gel liquid 2;
(3) Adding poly (vinylidene fluoride-co-hexafluoropropylene) and solid thermoplastic polyurethane rubber into the gel liquid 2 obtained in the step (2), and uniformly stirring to obtain gel liquid 3; the mass ratio of the poly (vinylidene fluoride-co-hexafluoropropylene) to the solid thermoplastic polyurethane rubber is (1:10) - (10:1); the mass ratio of the total mass of the poly (vinylidene fluoride-co-hexafluoropropylene) to the solid thermoplastic polyurethane rubber to the gel solution 1 in the step (1) is (1:1) - (10:1);
(4) And (3) coating the gel liquid 3 in the step (3) on a pole piece, and drying the pole piece to obtain the polymer negative electrode protective layer.
2. The method of claim 1, wherein the molar ratio of lithium source to polystyrene sulfonic acid in step (1) is (1:1) - (3:1);
the lithium source is LiCl, liOH, li 2 CO 3 、LiF、LiNO 3 More than one of LiTFSI and LiFSI;
the stirring treatment time in the step (1) is 30-90min, and the temperature is normal temperature.
3. The method according to claim 1, wherein the volume ratio of the N-methylpyrrolidone in step (2) to the gel liquid 1 in step (1) is (5:1) - (20:1);
the stirring treatment time in the step (2) is 30-90min.
4. The method according to claim 1, wherein the stirring in the step (3) is performed at room temperature for 6 to 20 hours.
5. The method according to claim 1, wherein the coating treatment in the step (4) is coating with a coater of 5 to 30 μm;
the temperature of the drying treatment in the step (4) is 30-90 ℃, and the drying time is 3-12h.
6. The polymer negative electrode protective layer prepared by the preparation method of any one of claims 1 to 5.
7. Use of the polymer negative electrode protection layer of claim 6 for the preparation of a metallic lithium electrode.
8. The use according to claim 7, wherein the polymer negative electrode protection layer is subjected to a lithium precipitation operation to obtain a metallic lithium electrode.
9. The use according to claim 8, wherein the lithium sinking operation is a lithium sinking operation performed by assembling a polymer negative electrode protection layer in a button cell.
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Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6444343B1 (en) * 1996-11-18 2002-09-03 University Of Southern California Polymer electrolyte membranes for use in fuel cells
WO2020151357A1 (en) * 2019-01-25 2020-07-30 深圳锂硫科技有限公司 Lithium battery separator and preparation method therefor
CN112952192A (en) * 2021-03-12 2021-06-11 上海交通大学 Preparation method and application of polyamino azulene-doped organic polymer electrolyte film

Family Cites Families (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR101566789B1 (en) * 2009-12-04 2015-11-09 현대자동차 주식회사 Sulfonated polyarylene ether copolymer process of manufacturing the same and polymer electrolyte membrane for fuel cell using the copolymer
US10347904B2 (en) * 2015-06-19 2019-07-09 Solidenergy Systems, Llc Multi-layer polymer coated Li anode for high density Li metal battery
CN105126648B (en) * 2015-09-21 2018-03-09 江苏凯米膜科技股份有限公司 A kind of method that network hole polyvinylidene fluoride film is prepared based on polyvinyl alcohol gel
EP3264500B1 (en) * 2015-12-17 2023-07-12 LG Energy Solution, Ltd. Lithium secondary battery anode and lithium secondary battery including same
US20200365902A1 (en) * 2019-05-14 2020-11-19 Nanotek Instruments, Inc. Conducting polymer network-based cathode-protecting layer for lithium metal secondary battery
CN110808358B (en) * 2019-11-03 2022-11-18 中国科学院青岛生物能源与过程研究所 Polyurethane-protected metal cathode with rigid framework confinement function and preparation method thereof
CN111180673B (en) * 2020-01-21 2023-06-23 天齐锂业股份有限公司 Preparation process of metal lithium negative electrode with surface protection layer
CN113540401B (en) * 2020-04-21 2023-03-24 华为技术有限公司 Metal negative electrode, preparation method thereof and secondary battery
CN112574659B (en) * 2020-12-11 2022-11-18 中国科学院青岛生物能源与过程研究所 A lithium secondary battery electrode sheet protective layer and preparation method thereof

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6444343B1 (en) * 1996-11-18 2002-09-03 University Of Southern California Polymer electrolyte membranes for use in fuel cells
WO2020151357A1 (en) * 2019-01-25 2020-07-30 深圳锂硫科技有限公司 Lithium battery separator and preparation method therefor
CN112952192A (en) * 2021-03-12 2021-06-11 上海交通大学 Preparation method and application of polyamino azulene-doped organic polymer electrolyte film

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
刘冬冬等.锂金属负极人造保护膜的研究进展.《物理化学学报》.2021,第37卷(第2期),第2008078 (2 of 15) 页. *

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