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CN113540697B - Composite diaphragm and preparation method thereof - Google Patents

Composite diaphragm and preparation method thereof Download PDF

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CN113540697B
CN113540697B CN202110721031.6A CN202110721031A CN113540697B CN 113540697 B CN113540697 B CN 113540697B CN 202110721031 A CN202110721031 A CN 202110721031A CN 113540697 B CN113540697 B CN 113540697B
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solid electrolyte
composite
monomer
lithium
methacrylate
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CN113540697A (en
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张志勇
牛亚如
李洋
朱冠楠
王义飞
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Gotion High Tech Co Ltd
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    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M50/00Constructional details or processes of manufacture of the non-active parts of electrochemical cells other than fuel cells, e.g. hybrid cells
    • H01M50/40Separators; Membranes; Diaphragms; Spacing elements inside cells
    • H01M50/409Separators, membranes or diaphragms characterised by the material
    • H01M50/449Separators, membranes or diaphragms characterised by the material having a layered structure
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M10/00Secondary cells; Manufacture thereof
    • H01M10/05Accumulators with non-aqueous electrolyte
    • H01M10/052Li-accumulators
    • H01M10/0525Rocking-chair batteries, i.e. batteries with lithium insertion or intercalation in both electrodes; Lithium-ion batteries
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M10/00Secondary cells; Manufacture thereof
    • H01M10/42Methods or arrangements for servicing or maintenance of secondary cells or secondary half-cells
    • H01M10/4235Safety or regulating additives or arrangements in electrodes, separators or electrolyte
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M50/00Constructional details or processes of manufacture of the non-active parts of electrochemical cells other than fuel cells, e.g. hybrid cells
    • H01M50/40Separators; Membranes; Diaphragms; Spacing elements inside cells
    • H01M50/403Manufacturing processes of separators, membranes or diaphragms
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M50/00Constructional details or processes of manufacture of the non-active parts of electrochemical cells other than fuel cells, e.g. hybrid cells
    • H01M50/40Separators; Membranes; Diaphragms; Spacing elements inside cells
    • H01M50/409Separators, membranes or diaphragms characterised by the material
    • H01M50/411Organic material
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M50/00Constructional details or processes of manufacture of the non-active parts of electrochemical cells other than fuel cells, e.g. hybrid cells
    • H01M50/40Separators; Membranes; Diaphragms; Spacing elements inside cells
    • H01M50/409Separators, membranes or diaphragms characterised by the material
    • H01M50/411Organic material
    • H01M50/414Synthetic resins, e.g. thermoplastics or thermosetting resins
    • H01M50/417Polyolefins
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M50/00Constructional details or processes of manufacture of the non-active parts of electrochemical cells other than fuel cells, e.g. hybrid cells
    • H01M50/40Separators; Membranes; Diaphragms; Spacing elements inside cells
    • H01M50/409Separators, membranes or diaphragms characterised by the material
    • H01M50/431Inorganic material
    • 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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  • Manufacturing & Machinery (AREA)
  • Inorganic Chemistry (AREA)
  • Materials Engineering (AREA)
  • Cell Separators (AREA)

Abstract

The invention discloses a composite diaphragm and a preparation method thereof, wherein the composite diaphragm comprises a base membrane, and the surface of the base membrane is coated with a LICION type composite solid electrolyte coating; the LISICON type composite solid electrolyte coating contains a LISICON type composite solid electrolyte, and the electrolyte is obtained by in-situ polymerization of a hydrophobic monomer and an ionic conductor monomer on the surface of the LISICON type solid electrolyte. On one hand, the organic polymer polymerized by the hydrophobic monomer can better improve the wettability between the diaphragm and the electrolyte; on the other hand, the ion conductor polymer polymerized by the ion conductor monomer can construct an ion transmission passage between non-compact LISICON type solid electrolyte particles, so that the ion transmission rate is improved; in addition, the LISICON type solid electrolyte belongs to an inorganic material, has high thermal stability, can stabilize a low-melting-point basement membrane at high temperature, and reduces the thermal shrinkage and the short circuit risk of the cell at high temperature.

Description

一种复合隔膜及其制备方法A kind of composite diaphragm and preparation method thereof

技术领域technical field

本发明属于锂离子电池技术领域,具体涉及一种复合隔膜及其制备方法。The invention belongs to the technical field of lithium ion batteries, and in particular relates to a composite diaphragm and a preparation method thereof.

背景技术Background technique

由于具有高功率密度、低自放电率,无记忆效应和放电电压稳定等优点,锂电池成为动力电池的主要选择。隔膜是锂离子电池的关键部件,在电池中起着阻隔正负极电子电导,允许电解液离子自由通过的重要作用。Due to the advantages of high power density, low self-discharge rate, no memory effect and stable discharge voltage, lithium batteries have become the main choice for power batteries. The separator is a key component of lithium-ion batteries, which plays an important role in blocking the electrical conductivity of positive and negative electrodes and allowing the free passage of electrolyte ions.

动力电池的安全问题是极为复杂的,隔膜在电池安全中扮演着至关重要的作用,在使用过程中,由于锂枝晶刺穿隔膜或电芯内部温度升高隔膜收缩导致内短路,造成正负极直接接触,短时间放出大量的热,最终导致电池发生热失控。The safety issues of power batteries are extremely complex, and the separator plays a crucial role in battery safety. During use, due to the puncture of the separator by lithium dendrites or the increase of the internal temperature of the cell, the shrinkage of the separator leads to an internal short circuit, resulting in positive The negative electrode is in direct contact, and a large amount of heat is released in a short time, which eventually leads to thermal runaway of the battery.

目前,采用具有高热稳定性和高离子电导率的无机陶瓷电解质作为涂覆层成为研究的热点,采用无机陶瓷固态电解质作为涂层的隔膜具有吸液性好、耐高温、离子电导率高、抑制锂枝晶等优点,可以用于液态、半固态、准固态、全固态锂电池以及金属锂电池中。但目前,在无机固态电解质涂覆隔膜的制备过程中,涂覆层极易吸水,导致隔膜水分增加,在后续使用过程需长时间烘烤去除隔膜中的水分,降低生产效率。At present, the use of inorganic ceramic electrolytes with high thermal stability and high ionic conductivity as the coating layer has become a research hotspot. Lithium dendrites and other advantages can be used in liquid, semi-solid, quasi-solid, all-solid-state lithium batteries and metal lithium batteries. However, at present, during the preparation of inorganic solid electrolyte-coated separators, the coating layer is very easy to absorb water, which leads to an increase in the moisture content of the separator. In the subsequent use process, it takes a long time to bake to remove the moisture in the separator, which reduces the production efficiency.

发明内容SUMMARY OF THE INVENTION

本发明的目的是提供一种复合隔膜及其制备方法,该复合隔膜能够减少隔膜烘烤的时间,降低隔膜的热收缩率,提升离子传输速率。The purpose of the present invention is to provide a composite diaphragm and a preparation method thereof, which can reduce the baking time of the diaphragm, reduce the thermal shrinkage rate of the diaphragm, and improve the ion transmission rate.

为实现上述目的,本发明采用的技术方案为:To achieve the above object, the technical scheme adopted in the present invention is:

一种复合隔膜,包括基膜,所述基膜的表面涂覆有LISICON型复合固态电解质涂层;所述LISICON型复合固态电解质涂层中包括LISICON型复合固态电解质,所述LISICON型复合固态电解质由LISICON型固态电解质、疏水单体、离子导体单体通过原位聚合制备所得。进一步的,所述基膜的材质为聚乙烯或聚丙烯;所述LISICON型复合固态电解质涂层的厚度为0.2~20 μm。A composite diaphragm, comprising a base membrane, the surface of the base membrane is coated with a LISICON type composite solid electrolyte coating; the LISICON type composite solid electrolyte coating includes a LISICON type composite solid electrolyte, and the LISICON type composite solid electrolyte coating It is prepared by in-situ polymerization of LISICON-type solid electrolyte, hydrophobic monomer and ionic conductor monomer. Further, the material of the base film is polyethylene or polypropylene; the thickness of the LISICON type composite solid electrolyte coating is 0.2-20 μm.

作为优选的技术方案,LISICON型复合固态电解质是通过以下步骤制备得到的:As a preferred technical solution, the LISICON type composite solid electrolyte is prepared through the following steps:

S1.将疏水单体和离子导体单体溶解在溶剂中得到反应液;进一步优选的,所述疏水单体为甲基丙烯酸甲酯、乙烯基三甲基硅烷、烷基类硅烷偶联剂、丙烯酸六氟丁酯、甲基丙烯酸六氟丁酯、甲基丙烯酸2,2,2-三氟乙酯、甲基丙烯酸十二氟庚酯、丙烯酸十二氟庚酯、甲基丙烯酸十三氟辛酯、丙烯酸十三氟辛酯中至少一种;所述离子导体单体为丙烯酸锂、甲基丙烯酸锂,马来酸锂、(甲基乙烯基醚共聚马来酸)锂、富马酸锂中至少一种;所述疏水单体和离子导体单体的物质的量比为0.01~1;所述溶剂为去离子水、DMF、DMSO、N-甲基吡咯烷酮、甲醇、乙醇、甲苯或四氢呋喃中的至少一种。S1. Dissolve the hydrophobic monomer and the ionic conductor monomer in a solvent to obtain a reaction solution; further preferably, the hydrophobic monomer is methyl methacrylate, vinyltrimethylsilane, an alkyl silane coupling agent, Hexafluorobutyl acrylate, hexafluorobutyl methacrylate, 2,2,2-trifluoroethyl methacrylate, dodecafluoroheptyl methacrylate, dodecafluoroheptyl acrylate, tridecafluoromethacrylate At least one of octyl ester and tridecafluorooctyl acrylate; the ion conductor monomer is lithium acrylate, lithium methacrylate, lithium maleate, (methyl vinyl ether copolymer maleate) lithium, fumaric acid At least one of lithium; the material ratio of the hydrophobic monomer and the ionic conductor monomer is 0.01 to 1; the solvent is deionized water, DMF, DMSO, N-methylpyrrolidone, methanol, ethanol, toluene or at least one of tetrahydrofuran.

S2.将LISICON型固态电解质加入到S1中的反应液中,加入引发剂后进行原位聚合反应;进一步的,所述疏水单体和离子导体单体的总质量与LISICON型固态电解质的质量比为0.001~0.02。S2. The LISICON type solid electrolyte is added to the reaction solution in S1, and an initiator is added to carry out an in-situ polymerization reaction; further, the total mass of the hydrophobic monomer and ion conductor monomer is compared with the mass ratio of the LISICON type solid electrolyte is 0.001~0.02.

S3.对原位聚合反应制得的产物进行抽滤、洗涤、真空烘干,最终得到被疏水聚合物和离子导体聚合物共同包覆的LISICON型固态电解质,即LISICON型复合固态电解质。S3. Perform suction filtration, washing and vacuum drying on the product obtained by the in-situ polymerization reaction, and finally obtain a LISICON type solid electrolyte which is co-coated by a hydrophobic polymer and an ion conductor polymer, that is, a LISICON type composite solid electrolyte.

作为优选的技术方案,所述LISICON型固态电解质的粒径分布为:D50≥200 nm,离散度

Figure 999593DEST_PATH_IMAGE001
;所述LISICON型固态电解质的化学式为Li1+xMxN2-x(PO4)3;其中:0≤x≤0.5;M选自Al、Y、Ga、Cr、Fe中的一种;N选自Ti、Ge、Ta、Zr、Sn、V中的一种。As a preferred technical solution, the particle size distribution of the LISICON type solid electrolyte is: D 50 ≥200 nm, and the dispersion degree is
Figure 999593DEST_PATH_IMAGE001
; The chemical formula of the LISICON type solid electrolyte is Li 1+x M x N 2-x (PO 4 ) 3 ; wherein: 0≤x≤0.5; M is selected from one of Al, Y, Ga, Cr, Fe ; N is selected from one of Ti, Ge, Ta, Zr, Sn, and V.

本发明还提供了上述所述的复合隔膜的制备方法,其包括以下步骤:The present invention also provides the preparation method of the above-mentioned composite membrane, which comprises the following steps:

将粘结剂、稳定剂、有机溶剂、LISICON型复合固态电解质混合均匀后得到稳定的悬浮液;将悬浮液涂覆在基膜的表面,烘干去除有机溶剂后即得到复合隔膜。进一步的,所述粘结剂为聚偏二氟乙烯;所述稳定剂为羧甲基纤维素、海藻酸钠、聚丙烯酸钠、聚酰胺中的至少一种;所述有机溶剂为N-甲基吡咯烷酮、乙腈、四氢呋喃中的至少一种。The binder, the stabilizer, the organic solvent and the LISICON type composite solid electrolyte are mixed uniformly to obtain a stable suspension; the suspension is coated on the surface of the base film, and the composite diaphragm is obtained after drying to remove the organic solvent. Further, the binder is polyvinylidene fluoride; the stabilizer is at least one of carboxymethyl cellulose, sodium alginate, sodium polyacrylate, and polyamide; the organic solvent is N-methyl cellulose At least one of pyrrolidone, acetonitrile, and tetrahydrofuran.

本发明的有益效果为:The beneficial effects of the present invention are:

本发明通过在基膜表面涂覆的LISICON型复合固态电解质涂层以改善其性能,其中LISICON型复合固态电解质涂层中含有LISICON型复合固态电解质,该LISICON型复合固态电解质是疏水单体和离子导体单体在LISICON型固态电解质的表面通过原位聚合所得。一方面,疏水单体聚合而成的有机聚合物可以更好地改善隔膜与电解液之间的润湿性;另一方面,离子导体单体聚合而成的离子导体聚合物能够在非致密LISICON型固态电解质颗粒之间构建离子传输通路,提升离子传输速率;此外,LISICON型固态电解质属无机材料,具有高的热稳定性,高温下可以稳定低熔点基膜,降低其热收缩和电芯高温下的短路风险。The present invention improves its performance by coating the LISICON type composite solid electrolyte coating on the surface of the base film, wherein the LISICON type composite solid electrolyte coating contains LISICON type composite solid electrolyte, and the LISICON type composite solid electrolyte is a hydrophobic monomer and ion The conductor monomer is obtained by in-situ polymerization on the surface of the LISICON-type solid electrolyte. On the one hand, the organic polymer formed by the polymerization of hydrophobic monomers can better improve the wettability between the separator and the electrolyte; LISICON type solid electrolyte particles build ion transport paths between the particles to improve the ion transport rate; in addition, LISICON type solid electrolyte is an inorganic material with high thermal stability. It can stabilize the low melting point base film at high temperature and reduce its thermal shrinkage and cell high temperature. risk of short circuit.

本发明提供的复合隔膜疏水性好、离子电导率高、电解液润湿性好、热收缩率低。应用在锂离子电芯生产中,可以节省隔膜烘烤成本,保证电芯的充放电倍率性能,减少电芯因隔膜收缩导致的短路风险。The composite membrane provided by the invention has good hydrophobicity, high ionic conductivity, good wettability of electrolyte and low thermal shrinkage rate. Applied in the production of lithium-ion cells, it can save the cost of separator baking, ensure the charge and discharge rate performance of the cell, and reduce the risk of short circuit caused by the shrinkage of the separator.

附图说明Description of drawings

图1为实施例1中复合的Li1.4Al0.4Ti1.6(PO4)3固态电解质压片接触角测试图片;Fig. 1 is the Li 1.4 Al 0.4 Ti 1.6 (PO 4 ) 3 solid electrolyte pressed sheet contact angle test picture of the composite in Example 1;

图2为对比例1中 Li1.4Al0.4Ti1.6(PO4)3固态电解质压片接触角测试图片。FIG. 2 is a test picture of the contact angle of Li 1.4 Al 0.4 Ti 1.6 (PO 4 ) 3 solid-state electrolyte in Comparative Example 1.

具体实施方式Detailed ways

下面将结合本发明实施例中的技术方案进行清楚、完整地描述,显然,所描述的实施例仅仅是本发明一部分实施例,而不是全部的实施例。基于本发明中的实施例,本领域普通技术人员在没有做出创造性劳动前提下所获得的所有其他实施例,都属于本发明保护的范围。The following will clearly and completely describe the technical solutions in the embodiments of the present invention. Obviously, the described embodiments are only a part of the embodiments of the present invention, rather than all the embodiments. Based on the embodiments of the present invention, all other embodiments obtained by those of ordinary skill in the art without creative efforts shall fall within the protection scope of the present invention.

实施例1Example 1

一种复合隔膜的制备方法,具体包括有以下步骤:A preparation method of a composite diaphragm, specifically comprising the following steps:

(1)将丙烯酸六氟丁酯:丙烯酸锂=1:1(物质的量比)置于甲苯/甲醇中搅拌溶解,再加入D50=500 nm的Li1.4Al0.4Ti1.6(PO4)3粉末(Li1.4Al0.4Ti1.6(PO4)3粉末的质量:丙烯酸六氟丁酯和甲基丙烯酸锂的总质量=99:1),搅拌1h后加入偶氮二异丁腈(AIBN)引发剂,在70℃水浴条件下进行原位聚合反应,3小时后,反应结束,将产物抽滤、无水乙醇洗涤、120℃真空烘干12h。最后得到复合的Li1.4Al0.4Ti1.6(PO4)3固态电解质,并对其压片进行接触角测试(对水)。具体数据见表1。(1) Put hexafluorobutyl acrylate:lithium acrylate=1:1 (material ratio) in toluene/methanol and stir to dissolve, then add Li 1.4 Al 0.4 Ti 1.6 (PO 4 ) 3 with D 50 =500 nm Powder (mass of Li 1.4 Al 0.4 Ti 1.6 (PO 4 ) 3 powder: total mass of hexafluorobutyl acrylate and lithium methacrylate=99:1), stir for 1 h and add azobisisobutyronitrile (AIBN) to initiate The in-situ polymerization reaction was carried out under the condition of a water bath at 70°C. After 3 hours, the reaction was completed, and the product was suction filtered, washed with absolute ethanol, and dried in vacuum at 120°C for 12 hours. Finally, the composite Li 1.4 Al 0.4 Ti 1.6 (PO 4 ) 3 solid electrolyte was obtained, and the contact angle test (to water) was carried out on the tablet. The specific data are shown in Table 1.

(2)取上述复合的Li1.4Al0.4Ti1.6(PO4)3固态电解质、聚偏二氟乙烯(PVDF)、聚酰胺、N-甲基吡咯烷酮(NMP),它们的质量比为9:0.5:0.5:25,四者用行星球磨机分散3h后得到稳定的浆料。(2) Take the above composite Li 1.4 Al 0.4 Ti 1.6 (PO 4 ) 3 solid electrolyte, polyvinylidene fluoride (PVDF), polyamide, N-methylpyrrolidone (NMP), and their mass ratio is 9:0.5 : 0.5: 25, and the four were dispersed with a planetary ball mill for 3 hours to obtain a stable slurry.

(3)将稳定的浆料通过微凹辊涂覆在聚乙烯基膜上,涂覆厚度为3微米,80℃烘干后即得到复合隔膜。(3) Coat the stable slurry on the polyethylene base film through a gravure roll with a coating thickness of 3 microns, and obtain a composite membrane after drying at 80°C.

将得到的复合隔膜进行水分含量测试、130℃下1 h的热收缩率。具体数据见表2。The obtained composite membrane was tested for moisture content and thermal shrinkage at 130 °C for 1 h. The specific data are shown in Table 2.

实施例2Example 2

一种复合隔膜的制备方法,具体包括有以下步骤:A preparation method of a composite diaphragm, specifically comprising the following steps:

(1)将乙烯基三甲基硅烷:甲基丙烯酸锂=1:1(物质的量比)置于甲醇中中搅拌溶解,再加入D50=500 nm的Li1.4Al0.4Ti1.6(PO4)3粉末(Li1.4Al0.4Ti1.6(PO4)3粉末质量:乙烯基三甲基硅烷和甲基丙烯酸锂的总质量=99:1),搅拌1h后加入偶氮二异丁腈(AIBN),70℃水浴条件下进行原位聚合反应,3小时后反应结束,将产物抽滤、无水乙醇洗涤、120℃真空烘干12h。最后得到复合的Li1.4Al0.4Ti1.6(PO4)3固态电解质,并对其压片进行接触角测试(对水)。具体数据见表1。(1) Put vinyltrimethylsilane:lithium methacrylate=1:1 (material ratio) in methanol and stir to dissolve, then add Li 1.4 Al 0.4 Ti 1.6 (PO 4 D 50 =500 nm) ) 3 powder (Li 1.4 Al 0.4 Ti 1.6 (PO 4 ) 3 powder mass: total mass of vinyltrimethylsilane and lithium methacrylate=99:1), stir for 1 h and add azobisisobutyronitrile (AIBN ), in-situ polymerization was carried out in a water bath at 70°C, the reaction was completed after 3 hours, and the product was suction filtered, washed with anhydrous ethanol, and dried in vacuum at 120°C for 12 hours. Finally, the composite Li 1.4 Al 0.4 Ti 1.6 (PO 4 ) 3 solid electrolyte was obtained, and the contact angle test (to water) was carried out on the tablet. The specific data are shown in Table 1.

(2)取上述复合的Li1.4Al0.4Ti1.6(PO4)3固态电解质、聚偏二氟乙烯(PVDF)、海藻酸钠、N-甲基吡咯烷酮(NMP),它们的质量比为9:0.5:0.5:25,四者用行星球磨机分散3h后得到稳定的浆料。(2) Take the above composite Li 1.4 Al 0.4 Ti 1.6 (PO 4 ) 3 solid electrolyte, polyvinylidene fluoride (PVDF), sodium alginate, N-methylpyrrolidone (NMP), and their mass ratio is 9: 0.5:0.5:25, the four were dispersed with a planetary ball mill for 3 hours to obtain a stable slurry.

(3)将稳定的浆料通过微凹辊涂覆在聚乙烯基膜上,涂覆厚度为3微米,80℃烘干后即得到复合隔膜。(3) Coat the stable slurry on the polyethylene base film through a gravure roll with a coating thickness of 3 microns, and obtain a composite membrane after drying at 80°C.

将得到的复合隔膜进行水分含量测试、130℃下1 h的热收缩率。具体数据见表2。The obtained composite membrane was tested for moisture content and thermal shrinkage at 130 °C for 1 h. The specific data are shown in Table 2.

实施例3Example 3

一种复合隔膜的制备方法,具体包括有以下步骤:A preparation method of a composite diaphragm, specifically comprising the following steps:

(1)将甲基丙烯酸甲酯:甲基丙烯酸锂=3:2(物质的量比)置于甲醇中中搅拌溶解,再加入D50=500 nm的Li1.4Al0.4Ti1.6(PO4)3粉末(Li1.4Al0.4Ti1.6(PO4)3粉末的质量:甲基丙烯酸甲酯和马来酸锂的总质量=98:2),搅拌1h后加入偶氮二异丁腈(AIBN),在70℃水浴条件下进行原位聚合反应,反应3小时后结束,将产物抽滤、无水乙醇洗涤、120℃真空烘干12h。最后得到复合的Li1.4Al0.4Ti1.6(PO4)3固态电解质,并对其压片进行接触角测试(对水)。具体数据见表1。(1) Methyl methacrylate: Lithium methacrylate=3:2 (material ratio) was dissolved in methanol with stirring, and then Li 1.4 Al 0.4 Ti 1.6 (PO 4 ) with D 50 =500 nm was added 3 powder (the mass of Li 1.4 Al 0.4 Ti 1.6 (PO 4 ) 3 powder: the total mass of methyl methacrylate and lithium maleate = 98:2), stir for 1 h and add azobisisobutyronitrile (AIBN) , in-situ polymerization was carried out under the condition of 70 ℃ water bath, the reaction was finished after 3 hours, the product was suction filtered, washed with absolute ethanol, and dried in vacuum at 120 ℃ for 12 hours. Finally, the composite Li 1.4 Al 0.4 Ti 1.6 (PO 4 ) 3 solid electrolyte was obtained, and the contact angle test (to water) was carried out on the tablet. The specific data are shown in Table 1.

(2)取上述复合的Li1.4Al0.4Ti1.6(PO4)3固态电解质、聚偏二氟乙烯(PVDF)、海藻酸钠、N-甲基吡咯烷酮(NMP),它们的质量比为9:0.5:0.5:25,四者用行星球磨机分散3h后得到稳定的浆料。(2) Take the above composite Li 1.4 Al 0.4 Ti 1.6 (PO 4 ) 3 solid electrolyte, polyvinylidene fluoride (PVDF), sodium alginate, N-methylpyrrolidone (NMP), and their mass ratio is 9: 0.5:0.5:25, the four were dispersed with a planetary ball mill for 3 hours to obtain a stable slurry.

(3)将稳定的浆料通过微凹辊涂覆在聚乙烯基隔膜上,涂覆厚度为2微米,80℃烘干后即得到复合隔膜。(3) Coat the stable slurry on the polyethylene-based diaphragm through a gravure roll with a coating thickness of 2 microns, and obtain a composite diaphragm after drying at 80°C.

将得到的复合隔膜进行水分含量测试、130℃下1 h的热收缩率。具体数据见表2。The obtained composite membrane was tested for moisture content and thermal shrinkage at 130 °C for 1 h. The specific data are shown in Table 2.

对比例1Comparative Example 1

选择未进行复合的D50=500 nm的Li1.4Al0.4Ti1.6(PO4)3粉末,同样进行压片,测试接触角(对水)。具体数据见表1。Li 1.4 Al 0.4 Ti 1.6 (PO 4 ) 3 powder with D 50 =500 nm that has not been compounded was selected, and the same was pressed to measure the contact angle (to water). The specific data are shown in Table 1.

对比例2Comparative Example 2

选择聚乙烯基隔膜,具体材料结构为聚丙烯-聚乙烯-聚丙烯。同样对其进行水分含量测试、130℃下1 h的热收缩率测试,结果见表2.The polyethylene-based diaphragm is selected, and the specific material structure is polypropylene-polyethylene-polypropylene. It was also tested for moisture content and thermal shrinkage at 130 °C for 1 h. The results are shown in Table 2.

水分含量的测试方法参照《GB/T 6283-2008化工产品中水分含量的测定卡尔•费休法(通用方法)》。The test method of moisture content refers to "GB/T 6283-2008 Determination of moisture content in chemical products Karl Fischer method (general method)".

上述各实施例和对比例制得的产品的检测结果见下表1和表2:The detection result of the product that each above-mentioned embodiment and comparative example make are shown in following table 1 and table 2:

表1.实施例与对比例中接触角(对水)测试结果Table 1. Contact angle (to water) test results in examples and comparative examples

Figure 925961DEST_PATH_IMAGE002
Figure 925961DEST_PATH_IMAGE002

表2.实施例与对比例中水分和热收缩率测试结果Table 2. Test results of moisture and thermal shrinkage in Examples and Comparative Examples

Figure 271491DEST_PATH_IMAGE003
Figure 271491DEST_PATH_IMAGE003

从表1中可以看出经过疏水单体处理过的LISICON型固态电解质具有良好的疏水性能,用此类LISICON型固态电解质涂覆后的隔膜可有效抵抗空气中的水分,同时有机组分可提高有机电解液的浸润性。从表2可看出,复合隔膜的水分相较于普通隔膜有更低的水分含量,有利于降低隔膜和电芯的烘烤成本;并且热收缩率降低明显,可降低因隔膜收缩导致的电芯安全风险。It can be seen from Table 1 that the LISICON type solid electrolyte treated with the hydrophobic monomer has good hydrophobic properties. The separator coated with this type of LISICON type solid electrolyte can effectively resist the moisture in the air, and the organic components can improve the Wetting properties of organic electrolytes. It can be seen from Table 2 that the moisture content of the composite diaphragm is lower than that of the ordinary diaphragm, which is beneficial to reduce the baking cost of the diaphragm and the battery core; and the thermal shrinkage rate is significantly reduced, which can reduce the electric power caused by the diaphragm shrinkage. core security risk.

尽管已经示出和描述了本发明的实施例,对于本领域的普通技术人员而言,可以理解在不脱离本发明的原理和精神的情况下可以对这些实施例进行多种变化、修改、替换和变型,本发明的范围由所附权利要求及其等同物限定。Although embodiments of the present invention have been shown and described, it will be understood by those skilled in the art that various changes, modifications, and substitutions can be made in these embodiments without departing from the principle and spirit of the invention and modifications, the scope of the present invention is defined by the appended claims and their equivalents.

Claims (8)

1. A composite separator comprising a base film, characterized in that: the surface of the base film is coated with a composite solid electrolyte coating; the composite solid electrolyte coating comprises a composite solid electrolyte, and the composite solid electrolyte is prepared from a solid electrolyte, a hydrophobic monomer and an ionic conductor monomer through in-situ polymerization;
the composite solid electrolyte is prepared by the following steps:
s1, dissolving a hydrophobic monomer and an ionic conductor monomer in a solvent to obtain a reaction solution;
s2, adding the solid electrolyte into the reaction liquid in the S1, and carrying out in-situ polymerization reaction after adding the initiator;
s3, carrying out suction filtration, washing and vacuum drying on a product obtained by the in-situ polymerization reaction to finally obtain a solid electrolyte, namely a composite solid electrolyte, coated by the hydrophobic polymer and the ionic conductor polymer;
the hydrophobic monomer is at least one of methyl methacrylate, vinyl trimethylsilane, alkyl silane coupling agent, hexafluorobutyl acrylate, hexafluorobutyl methacrylate, 2, 2, 2-trifluoroethyl methacrylate, dodecafluoro heptyl acrylate, tridecafluorooctyl methacrylate and tridecafluorooctyl acrylate; the ion conductor monomer is at least one of lithium acrylate, lithium methacrylate, lithium maleate, (methyl vinyl ether copolymerized maleic acid) lithium and lithium fumarate;
the chemical formula of the solid electrolyte is Li 1+x M x N 2-x (PO 4 ) 3 (ii) a Wherein: x is more than or equal to 0 and less than or equal to 0.5; m is selected from one of Al, Y, Ga, Cr and Fe; n is selected from one of Ti, Ge, Ta, Zr, Sn and V.
2. The composite membrane of claim 1, wherein: the mass ratio of the hydrophobic monomer to the ionic conductor monomer is 0.01-1; the mass ratio of the total mass of the hydrophobic monomer and the ionic conductor monomer to the solid electrolyte is 0.001-0.02.
3. The composite membrane of claim 1, wherein: the solvent is at least one of deionized water, DMF, DMSO, N-methyl pyrrolidone, methanol, ethanol, toluene or tetrahydrofuran.
4. The composite membrane of claim 1, wherein: the base film is made of polyethylene or polypropylene.
5. The composite membrane of claim 1, wherein: the thickness of the composite solid electrolyte coating is 0.2-20 mu m.
6. The composite membrane of claim 1, wherein: the particle size distribution of the solid electrolyte is as follows: d 50 Greater than or equal to 200 nm, dispersion
Figure 467613DEST_PATH_IMAGE001
7. The method for producing a composite separator according to any one of claims 1 to 6, wherein: the method comprises the following steps:
uniformly mixing a binder, a stabilizer, an organic solvent and a composite solid electrolyte to obtain a stable suspension; and coating the suspension on the surface of the base film, and drying to remove the organic solvent to obtain the composite diaphragm.
8. The method for producing a composite separator according to claim 7, wherein: the binder is polyvinylidene fluoride; the stabilizer is at least one of carboxymethyl cellulose, sodium alginate, sodium polyacrylate and polyamide; the organic solvent is at least one of N-methyl pyrrolidone, acetonitrile and tetrahydrofuran.
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