WO2018176981A1 - Electrolyte solution for lithium ion battery, and battery - Google Patents
Electrolyte solution for lithium ion battery, and battery Download PDFInfo
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- WO2018176981A1 WO2018176981A1 PCT/CN2018/071515 CN2018071515W WO2018176981A1 WO 2018176981 A1 WO2018176981 A1 WO 2018176981A1 CN 2018071515 W CN2018071515 W CN 2018071515W WO 2018176981 A1 WO2018176981 A1 WO 2018176981A1
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- carbonate
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- ion battery
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M10/00—Secondary cells; Manufacture thereof
- H01M10/05—Accumulators with non-aqueous electrolyte
- H01M10/056—Accumulators with non-aqueous electrolyte characterised by the materials used as electrolytes, e.g. mixed inorganic/organic electrolytes
- H01M10/0564—Accumulators with non-aqueous electrolyte characterised by the materials used as electrolytes, e.g. mixed inorganic/organic electrolytes the electrolyte being constituted of organic materials only
- H01M10/0566—Liquid materials
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M10/00—Secondary cells; Manufacture thereof
- H01M10/05—Accumulators with non-aqueous electrolyte
- H01M10/052—Li-accumulators
- H01M10/0525—Rocking-chair batteries, i.e. batteries with lithium insertion or intercalation in both electrodes; Lithium-ion batteries
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M10/00—Secondary cells; Manufacture thereof
- H01M10/05—Accumulators with non-aqueous electrolyte
- H01M10/056—Accumulators with non-aqueous electrolyte characterised by the materials used as electrolytes, e.g. mixed inorganic/organic electrolytes
- H01M10/0564—Accumulators with non-aqueous electrolyte characterised by the materials used as electrolytes, e.g. mixed inorganic/organic electrolytes the electrolyte being constituted of organic materials only
- H01M10/0566—Liquid materials
- H01M10/0567—Liquid materials characterised by the additives
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M10/00—Secondary cells; Manufacture thereof
- H01M10/42—Methods or arrangements for servicing or maintenance of secondary cells or secondary half-cells
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M10/00—Secondary cells; Manufacture thereof
- H01M10/42—Methods or arrangements for servicing or maintenance of secondary cells or secondary half-cells
- H01M10/4235—Safety or regulating additives or arrangements in electrodes, separators or electrolyte
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- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/10—Energy storage using batteries
Definitions
- the present application relates to the field of battery safety, and in particular to a lithium ion battery electrolyte and a battery.
- the power battery is provided with a safety valve.
- the safety valve When the internal pressure is too large, the safety valve will open due to internal pressure, releasing the pressure inside the battery and improving the safety of the battery.
- a violent reaction has occurred inside the battery, and the safety valve is not opened; or the violent reaction inside the battery does not cause the safety valve to be opened for the first time, resulting in safety measures being activated. Delays can adversely affect the battery.
- part of the practice is to add a flame retardant additive to the electrolyte to prevent combustion inside the battery; in part, a substance that is thermally decomposed and can generate water is introduced into the battery system, and in the case of abnormal battery, let A large amount of gas is formed inside the battery to assist in opening the safety valve.
- the addition of a flame retardant additive to the electrolyte has a large viscosity due to the flame retardant additive, which seriously affects the lithium ion transport performance of the electrolyte, thereby reducing the electrochemical performance such as the rate performance of the lithium battery.
- a substance which is thermally decomposed to generate water is introduced.
- this method it is usual to mix the substance into a slurry of a positive electrode or a negative electrode and then apply it to a current collector. Since these materials are non-electrochemically active and have extremely low electrical conductivity, they can significantly affect the energy density of the battery. In addition, these materials usually use crystalline water compounds, which will contain a small amount of adsorbed water, which will affect The electrolyte system leads to poor performance of the lithium battery.
- the disadvantage of this method is that the decomposition of the substance is slow to the thermal response inside the battery, and the thermal runaway cannot be suppressed in time.
- the present invention provides an electrolyte and a battery which can effectively control the thermal runaway phenomenon and have a negative influence on the performance of the battery itself at the same time.
- the invention provides a lithium ion battery electrolyte comprising a lithium salt, an additive and an organic solvent, wherein the additive is polyethylene glycol-polypropylene glycol-polyethylene glycol.
- the additive in the electrolyte polyethylene glycol-polypropylene glycol-polyethylene glycol (PEO-PPO-PEO) will It reacts with lithium salt and its decomposition products due to heat, and forms a gel after the reaction; and the newly formed gel will cover the surface of the positive and negative electrodes to form a protective film, which sharply increases the internal resistance of the lithium battery and avoids positive and negative Extremely direct contact, which suppresses thermal runaway and improves battery safety.
- the thermal response temperature of the above additive PEO-PPO-PEO is generally between 90 ° C and 120 ° C, and has little effect on the performance of the electrolyte itself at normal room temperature.
- the influence of the conductivity of the electrolyte at room temperature is very small. Therefore, in the electrolyte provided by the invention, the addition of the additive can well control the internal thermal runaway phenomenon of the battery and improve the safety of the battery; on the other hand, the negative impact on the performance of the battery itself is very small, very good.
- the present invention provides a battery comprising a housing, a pole core housed in the housing, and an electrolyte, which is the lithium ion battery electrolyte provided by the present invention.
- Fig. 1 is a graph showing temperature changes of acupuncture experiments of Examples 1-6 and Comparative Example 1.
- Fig. 3 is a SEM image of a pole piece after heat treatment in Example 3.
- the present invention provides an electrolyte comprising a lithium salt, an additive and an organic solvent, wherein the additive is polyethylene glycol-polypropylene glycol-polyethylene glycol.
- the additive in the electrolyte polyethylene glycol-polypropylene glycol-polyethylene glycol (PEO-PPO-PEO) will It interacts with the electrolyte system due to heat (for example, phosphorus pentafluoride produced by thermal decomposition of lithium hexafluorophosphate is a strong Lewis acid; the electrolyte system of other lithium salts is also thermally decomposed to produce a strong Lewis acid group like this.
- the group while PEO-PPO-PEO reacts with these strong Lewis acids), reacts to form a jelly product; and the newly formed gel coats the surface of the positive and negative electrodes to form a protective film, which sharply increases the internal resistance of the lithium battery.
- the heat corresponding temperature of the above additive PEO-PPO-PEO is generally between 90 ° C and 120 ° C, and has little effect on the performance of the electrolyte itself at normal room temperature. For example, the influence of the conductivity of the electrolyte at room temperature is very small.
- the addition of the additive can well control the internal thermal runaway phenomenon of the battery and improve the safety of the battery; on the other hand, the negative impact on the performance of the battery itself is very small, very good.
- PEO-PPO-PEO is widely used in other chemical fields due to its low price and non-toxic superior performance.
- the electrolyte contains from 0.5% to 20% by volume of the additive based on the total volume of the electrolyte.
- the additives in this range can achieve good results without affecting the performance of the battery.
- the additive of the present invention has an average molecular weight of 1800 to 10,000, which can further improve the performance of the battery of the present invention.
- the lithium salt is selected from one or more of LiPF 6 , LiBOB, LiTFSI or LiFSI.
- the concentration of the lithium salt is from 0.5 mol/L to 3 mol/L.
- the organic solvent is one or more selected from the group consisting of a cyclic carbonate or a chain carbonate.
- PEO-PPO-PEO has the properties of a surfactant, which is especially compatible with carbonate electrolytes; at the same time, it can also improve the contact between active material particles and electrolyte during long-period cycling.
- the cyclic carbonate is selected from the group consisting of ethylene carbonate (EC) and/or propylene carbonate (PC).
- EC and PC have a higher ignition point and can form a stable SEI film at the negative electrode.
- the chain carbonate is selected from one or more of dimethyl carbonate (DMC), diethyl carbonate (DEC), dipropyl carbonate (DPC) or methyl ethyl carbonate (EMC).
- DMC dimethyl carbonate
- DEC diethyl carbonate
- DPC dipropyl carbonate
- EMC methyl ethyl carbonate
- a negative electrode film-forming additive is further added to the electrolyte, and the mass percentage of the negative electrode film-forming additive contained in the electrolyte is 0.5% to 2% based on the total mass of the electrolyte. .
- the negative film forming additive is vinylene carbonate (VC) or fluoroethylene carbonate (FEC).
- the organic solvent is a mixed solution of ethylene carbonate, diethyl carbonate and methyl ethyl carbonate, the ethylene carbonate, diethyl carbonate and methyl ethyl carbonate
- the volume ratio of the ester was 1:1:1.
- the present invention provides a battery comprising a casing, a pole core housed in the casing, and an electrolyte, wherein the electrolyte is the electrolyte provided by the present invention.
- the polar core is formed by winding a positive electrode sheet, a negative electrode sheet, and a separator.
- Step 1 preparing an electrolyte: the electrolyte is the electrolyte provided by the present invention described above;
- Step 2 preparing a polar core: the positive electrode sheet, the separator and the negative electrode sheet are sequentially laminated and then wound to obtain a polar core;
- Step 3 packaging the battery: the pole core prepared in step 2 is loaded into the housing;
- Step 4 Injecting liquid and sealing: Injecting an electrolyte into the casing and sealing it to obtain a battery.
- Lithium cobaltate, acetylene black, polytetrafluoroethylene and N-methylpyrrolidone are mixed and stirred into a slurry at a weight ratio of 100:3:2:50, and the slurry is uniformly coated on a conductive base aluminum foil. On both sides, the film was dried, rolled, and cut at 110 ° C to obtain a positive electrode sheet having a size of 485 mm ⁇ 44 mm ⁇ 0.140 mm.
- the natural graphite, carboxymethyl cellulose, styrene-butadiene rubber and water are thoroughly mixed and stirred in a weight ratio of 100:2:2:180 to obtain a uniform slurry, and the slurry is uniformly coated on a conductive base copper foil of 0.008 mm. Both sides were dried at 100 ° C, and finally, a negative electrode sheet having a size of 480 mm ⁇ 45 mm ⁇ 0.156 mm was obtained by cutting.
- the positive electrode sheet, the negative electrode sheet and the polypropylene film prepared above were wound into a polar core of a prismatic lithium ion battery, and then the electrolytic solution was injected into the aluminum plastic film at a rate of 3.6 g/Ah, and sealed to prepare a soft-package lithium ion.
- the composition of the electrolyte is: 45 ml of organic solvent, and a mixed organic solvent containing EC, EMC and DEC is selected, wherein the volume ratio of EC, EMC and DEC is 1:1:1; the additive PEO-PPO-PEO is 5 ml, of which PEO-PPO The average molecular weight of PEO is 2900; a certain amount of LiPF 6 is added at a concentration of 1 mol/L.
- the battery S2 was prepared in the same manner as in Example 1, except that the composition of the electrolyte was 42.5 ml of an organic solvent, and a mixed organic solvent containing EC, EMC and DEC was selected, wherein the volume ratio of EC, EMC and DEC was 1:1:1; additive PEO-PPO-PEO 7.5ml, wherein the average molecular weight of PEO-PPO-PEO is 2900; a certain amount of LiPF 6 is added at a concentration of 1 mol/L.
- the composition of the electrolyte was 42.5 ml of an organic solvent, and a mixed organic solvent containing EC, EMC and DEC was selected, wherein the volume ratio of EC, EMC and DEC was 1:1:1; additive PEO-PPO-PEO 7.5ml, wherein the average molecular weight of PEO-PPO-PEO is 2900; a certain amount of LiPF 6 is added at a concentration of 1 mol/L.
- the battery S3 was prepared in the same manner as in Example 1, except that the composition of the electrolyte was 40 ml of an organic solvent, and a mixed organic solvent containing EC, EMC and DEC was selected, wherein the volume ratio of EC, EMC and DEC was 1. : 1:1; additive PEO-PPO-PEO 10ml, wherein the average molecular weight of PEO-PPO-PEO is 2900; a certain amount of LiPF 6 is added at a concentration of 1 mol/L.
- Battery S4 was prepared in the same manner as in Example 1, except that the additive (PEO-PPO-PEO had an average molecular weight of 3,500.
- Battery S5 was prepared in the same manner as in Example 1, except that the organic solvent was acetonitrile.
- Battery S6 was prepared in the same manner as in Example 1, except that the composition of the electrolyte further contained a negative electrode film-forming additive of VC, and the mass fraction of VC was 1.5%.
- the battery DS1 was prepared in the same manner as in Example 1, except that the electrolyte: 50 ml of an organic solvent selected from a mixed organic solvent containing EC, EMC and DEC, wherein the volume ratio of EC, EMC and DEC was 1:1:1; a certain amount of LiPF 6 was added at a concentration of 1 mol/L.
- an organic solvent selected from a mixed organic solvent containing EC, EMC and DEC, wherein the volume ratio of EC, EMC and DEC was 1:1:1; a certain amount of LiPF 6 was added at a concentration of 1 mol/L.
- the batteries DS1 and S6 prepared in the above Examples 1-6 and Comparative Example 1 were prepared to obtain a battery DS1.
- the batteries DS1 were prepared by first preparing the batteries S1-S6 prepared in the above Examples 1-6 and Comparative Example 1. Charge and discharge, charge and discharge current is 0.1C, charge and discharge voltage range is 2.65V-4.35V; after 0.1C cycle, charge to 4.35V, 2.5Ah capacity, puncture test. At the same time, the temperature change of the battery in the puncture experiment was detected. A detailed description of the puncture experiment is as follows:
- Eligibility criteria Cell temperature ⁇ 200 ° C, no explosion, no fire, no smoke.
- SEM Sccanning Electron Microscope Test: The surface of the pole piece was observed by instrument model JSM-7600F, FESEM/EDS-field emission scanning electron microscope and accessory energy spectrometer. The battery is charged and discharged in a range of 2.75 to 4.35 V, and charged and discharged at a rate of 1 C for 50 cycles, and then recharged to 100% SOC; then the battery is disassembled in an argon-filled glove box to separate the positive electrode sheets; Finally, after sealing treatment in an aluminum plastic film sealed bag in a glove box, SEM related characterization was performed.
- Example 1 The batteries prepared in Example 1, Example 2, Example 3, Example 4, Example 5 and Example 6 did not explode and did not burn vigorously;
- the battery prepared in the comparative example the battery burned violently, exploded, and the puncture failed.
- FIG. 2 is an SEM image of the comparative example
- FIG. 3 is an SEM image of the third embodiment; from the comparison of FIG. 2 and FIG. 3, the SEM image of the comparative example of FIG. 2 has a relatively bulky molecular structure and is relatively large.
- the gap of the embodiment 3 of Fig. 3 is relatively dense because the surface forms a gel and covers the surface.
- Fig. 2 and Fig. 3 show that the surface of the pole piece of the comparative example of Fig.
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Abstract
Provided is an electrolyte solution, comprising a lithium salt, an additive and an organic solvent, wherein the additive is poly(ethylene glycol)-poly(propylene glycol)-poly(ethylene glycol). Also provided is a battery, wherein same uses the electrolyte solution provided in the present invention. The electrolyte solution and the battery provided in the present invention can effectively control a thermal runaway phenomenon that may occur in the process of using the battery, and at the same time, there is little negative influence on the battery itself.
Description
本申请要求于2017年03月31日提交中国专利局、申请号为201710204908.8、发明名称为“一种锂离子电池电解液及电池”的中国专利申请的优先权,其全部内容通过引用结合在本申请中。This application claims priority to Chinese Patent Application No. 200910204908.8, entitled "Li-ion Battery Electrolyte and Battery" by the Chinese Patent Office on March 31, 2017, the entire contents of which are incorporated herein by reference. In the application.
本申请涉及电池安全领域,尤其涉及一种锂离子电池电解液及电池。The present application relates to the field of battery safety, and in particular to a lithium ion battery electrolyte and a battery.
随着人们对环境的重视程度越来越高,环保意识越来越强,作为替代传统燃油汽车的新能源车,其需求量也越来越大。而随着路面上新能源车数量的不断增加,安全性特别是作为新能源车动力源的动力电池的安全性,就变得越来越重要。As people pay more and more attention to the environment and become more environmentally aware, the demand for new energy vehicles that replace traditional fuel vehicles is increasing. With the increasing number of new energy vehicles on the road, safety, especially the safety of power batteries as the power source of new energy vehicles, has become more and more important.
在动力电池中,通常为锂离子电池,由于使用了可燃的碳酸酯类电解液;在使用过程中,可能会因过充或者过放、或者由于在意外撞击下(特别是针刺等因素的影响下),造成单体电池内部反应加剧,使得电池内部温度升高,导致电池热失控、自然、爆炸等安全问题的出现。因此,如何提高电池在过充、过放或者极端条件下的安全性能,成为了限制电动汽车发展的一大难题。In power batteries, usually lithium-ion batteries, due to the use of flammable carbonate-based electrolytes; may be overcharged or over-discharged during use, or due to accidental impact (especially acupuncture) Under the influence), the internal reaction of the single cell is intensified, causing the internal temperature of the battery to rise, which leads to the occurrence of safety problems such as thermal runaway, natural and explosion of the battery. Therefore, how to improve the safety performance of the battery under overcharge, over discharge or extreme conditions has become a major problem to limit the development of electric vehicles.
一般情况下,动力电池上均设置有安全阀,在内部压力过大时,该安全阀会因内部压力而打开,释放电池内部的压力,提高电池的安全性。但是,在实际使用过程中,往往可能出现电池内部已经发生剧烈反应,而安全阀并没有被打开的情况;或者电池内部的剧烈反应,不能使得安全阀第一时间被打开,造成安全措施启动的延迟,都会对电池造成不利的影响。Under normal circumstances, the power battery is provided with a safety valve. When the internal pressure is too large, the safety valve will open due to internal pressure, releasing the pressure inside the battery and improving the safety of the battery. However, in actual use, it is often the case that a violent reaction has occurred inside the battery, and the safety valve is not opened; or the violent reaction inside the battery does not cause the safety valve to be opened for the first time, resulting in safety measures being activated. Delays can adversely affect the battery.
现有技术中,部分做法是在电解液中添加阻燃添加剂,以阻止电池内部的燃烧;部分做法是在电池体系中引入受热分解并可以产生水的物质,在电池出现异常的情况下,让电池内部形成大量气体,从而辅助出发安全阀的打开。In the prior art, part of the practice is to add a flame retardant additive to the electrolyte to prevent combustion inside the battery; in part, a substance that is thermally decomposed and can generate water is introduced into the battery system, and in the case of abnormal battery, let A large amount of gas is formed inside the battery to assist in opening the safety valve.
但是,在电解液中添加阻燃添加剂的做法,由于阻燃添加剂具有较大的粘性,会严重影响到电解液的锂离子传输性能,进而降低锂电池的倍率性能等电化学表现。However, the addition of a flame retardant additive to the electrolyte has a large viscosity due to the flame retardant additive, which seriously affects the lithium ion transport performance of the electrolyte, thereby reducing the electrochemical performance such as the rate performance of the lithium battery.
而在电池体系中引入受热分解可以产生水的物质,此方法中,通常的做法是将该物质混合到正极或负极的浆料中,然后在涂覆到集流体上。由于这类物质都是非电化学活性的且电导率极低,因此会显著影响电池的能量密度;除此之外,该类物质通常采用的是结晶水化合物,会含有少量的吸附水,进而影响电解液体系,导致锂电池性能较差。该方法的弊端还在于,物质的分解对于电池内部的热响应较慢,无法及时抑制热失控。In the battery system, a substance which is thermally decomposed to generate water is introduced. In this method, it is usual to mix the substance into a slurry of a positive electrode or a negative electrode and then apply it to a current collector. Since these materials are non-electrochemically active and have extremely low electrical conductivity, they can significantly affect the energy density of the battery. In addition, these materials usually use crystalline water compounds, which will contain a small amount of adsorbed water, which will affect The electrolyte system leads to poor performance of the lithium battery. The disadvantage of this method is that the decomposition of the substance is slow to the thermal response inside the battery, and the thermal runaway cannot be suppressed in time.
发明内容Summary of the invention
本发明为解决现有技术中的方案,提供一种能够有效控制热失控现象,并且同时对电池本身性能的负面影响很小的电解液及电池。In order to solve the solution in the prior art, the present invention provides an electrolyte and a battery which can effectively control the thermal runaway phenomenon and have a negative influence on the performance of the battery itself at the same time.
本发明提供了一种锂离子电池电解液,包括锂盐、添加剂和有机溶剂,其中,所述添加剂为聚乙二醇-聚丙二醇-聚乙二醇。The invention provides a lithium ion battery electrolyte comprising a lithium salt, an additive and an organic solvent, wherein the additive is polyethylene glycol-polypropylene glycol-polyethylene glycol.
在本发明中,当电池因过充、过放或针刺等导致其内部温度升高时,电解液中的添加剂聚乙二醇-聚丙二醇-聚乙二醇(PEO-PPO-PEO)会因受热而与锂盐及其分解物产生相互作用,反应后生成胶状物;而该新生成的胶状物会覆盖在正负极表面形成保护膜,急剧增大锂电池内阻,避免正负极直接接触,从而压制热失控,提高电池的安全性。同时,上述添加剂PEO-PPO-PEO的热响应温度一般在90℃-120℃,在一般常温下对电解液本身的性能影响较小,比如,常温下对电解液的电导率影响非常小。因此,本发明提供的电解液中,添加剂的加入,一方面能够很好的控制电池内部热失控现象,提高电池的安全性;另一方面,对电池本身性能的负面影响非常小,很好的解决了本发明背景技术中存在的技术问题。In the present invention, when the internal temperature of the battery is increased due to overcharge, overdischarge or acupuncture, the additive in the electrolyte polyethylene glycol-polypropylene glycol-polyethylene glycol (PEO-PPO-PEO) will It reacts with lithium salt and its decomposition products due to heat, and forms a gel after the reaction; and the newly formed gel will cover the surface of the positive and negative electrodes to form a protective film, which sharply increases the internal resistance of the lithium battery and avoids positive and negative Extremely direct contact, which suppresses thermal runaway and improves battery safety. At the same time, the thermal response temperature of the above additive PEO-PPO-PEO is generally between 90 ° C and 120 ° C, and has little effect on the performance of the electrolyte itself at normal room temperature. For example, the influence of the conductivity of the electrolyte at room temperature is very small. Therefore, in the electrolyte provided by the invention, the addition of the additive can well control the internal thermal runaway phenomenon of the battery and improve the safety of the battery; on the other hand, the negative impact on the performance of the battery itself is very small, very good The technical problems existing in the background art of the present invention are solved.
此外,本发明提供了一种电池,包括壳体、容纳在壳体内的极芯以及电解液,该电解液为本发明提供的锂离子电池电解液。Further, the present invention provides a battery comprising a housing, a pole core housed in the housing, and an electrolyte, which is the lithium ion battery electrolyte provided by the present invention.
为了更清楚地说明本发明实施例或现有技术中的技术方案,下面将对实施例或现有技术描述中所需要使用的附图作简单地介绍,显而易见地,下面描述中的附图仅仅是本发明的实施例,对于本领域普通技术人员来讲,在不 付出创造性劳动的前提下,还可以根据提供的附图获得其他的附图。In order to more clearly illustrate the embodiments of the present invention or the technical solutions in the prior art, the drawings used in the embodiments or the description of the prior art will be briefly described below. Obviously, the drawings in the following description are only It is an embodiment of the present invention, and those skilled in the art can obtain other drawings according to the provided drawings without any creative work.
图1是实施例1-6和对比例1的针刺实验温度变化图。BRIEF DESCRIPTION OF THE DRAWINGS Fig. 1 is a graph showing temperature changes of acupuncture experiments of Examples 1-6 and Comparative Example 1.
图2是对比例1加热处理后的极片SEM图。2 is an SEM image of a pole piece after heat treatment of Comparative Example 1.
图3是实施例3加热处理后的极片SEM图。Fig. 3 is a SEM image of a pole piece after heat treatment in Example 3.
为了使本发明所解决的技术问题、技术方案及有益效果更加清楚明白,以下结合附图及实施例,对本发明进行进一步详细说明。应当理解,此处所描述的具体实施例仅仅用以解释本发明,并不用于限定本发明。The present invention will be further described in detail below with reference to the accompanying drawings and embodiments. It is understood that the specific embodiments described herein are merely illustrative of the invention and are not intended to limit the invention.
本发明提供了一种电解液,包括锂盐、添加剂和有机溶剂,其中,所述添加剂为聚乙二醇-聚丙二醇-聚乙二醇。The present invention provides an electrolyte comprising a lithium salt, an additive and an organic solvent, wherein the additive is polyethylene glycol-polypropylene glycol-polyethylene glycol.
在本发明中,当电池因过充、过放或针刺等导致其内部温度升高时,电解液中的添加剂聚乙二醇-聚丙二醇-聚乙二醇(PEO-PPO-PEO)会因受热而和电解液体系发生相互作用(比如,六氟磷酸锂受热分解产生的五氟化磷,为一种强路易斯酸;其他锂盐的电解液体系,也会受热分解产生类似这样的强路易斯酸基团,而PEO-PPO-PEO会和这些强路易斯酸反应),反应后生成胶状物产物;而该新生成的胶状物会覆盖在正负极表面形成保护膜,急剧增大锂电池内阻,避免正负极直接接触,从而压制热失控,提高电池的安全性。同时,上述添加剂PEO-PPO-PEO的热相应温度一般在90℃-120℃,在一般常温下对电解液本身的性能影响较小,比如,常温下对电解液的电导率影响非常小。因此,本发明提供的电解液中,添加剂的加入,一方面能够很好的控制电池内部热失控现象,提高电池的安全性;另一方面,对电池本身性能的负面影响非常小,很好的解决了本发明背景技术中存在的技术问题。In the present invention, when the internal temperature of the battery is increased due to overcharge, overdischarge or acupuncture, the additive in the electrolyte polyethylene glycol-polypropylene glycol-polyethylene glycol (PEO-PPO-PEO) will It interacts with the electrolyte system due to heat (for example, phosphorus pentafluoride produced by thermal decomposition of lithium hexafluorophosphate is a strong Lewis acid; the electrolyte system of other lithium salts is also thermally decomposed to produce a strong Lewis acid group like this. The group, while PEO-PPO-PEO reacts with these strong Lewis acids), reacts to form a jelly product; and the newly formed gel coats the surface of the positive and negative electrodes to form a protective film, which sharply increases the internal resistance of the lithium battery. To avoid direct contact between the positive and negative electrodes, thereby suppressing thermal runaway and improving the safety of the battery. At the same time, the heat corresponding temperature of the above additive PEO-PPO-PEO is generally between 90 ° C and 120 ° C, and has little effect on the performance of the electrolyte itself at normal room temperature. For example, the influence of the conductivity of the electrolyte at room temperature is very small. Therefore, in the electrolyte provided by the invention, the addition of the additive can well control the internal thermal runaway phenomenon of the battery and improve the safety of the battery; on the other hand, the negative impact on the performance of the battery itself is very small, very good The technical problems existing in the background art of the present invention are solved.
同时,PEO-PPO-PEO由于其售价低且无毒的优越性能,在其他化学领域的应用也较为广泛。At the same time, PEO-PPO-PEO is widely used in other chemical fields due to its low price and non-toxic superior performance.
本发明一个优选方案中,以电解液的总体积为基准,电解液中包含体积百分比为0.5%-20%的添加剂。在此范围内的添加剂,能够起到很好的效果,并且不会影响到电池的性能。In a preferred embodiment of the invention, the electrolyte contains from 0.5% to 20% by volume of the additive based on the total volume of the electrolyte. The additives in this range can achieve good results without affecting the performance of the battery.
为了更好的体现添加剂的作用,达到更好的效果,本发明优选添加剂的平均分子量为1800-10000,能够进一步提高本发明电池的性能。In order to better reflect the effect of the additive and achieve a better effect, it is preferred that the additive of the present invention has an average molecular weight of 1800 to 10,000, which can further improve the performance of the battery of the present invention.
本发明中,优选地,锂盐选自LiPF
6、LiBOB、LiTFSI或LiFSI中的一种或几种。
In the present invention, preferably, the lithium salt is selected from one or more of LiPF 6 , LiBOB, LiTFSI or LiFSI.
本发明中,优选地,锂盐的浓度为0.5mol/L-3mol/L。In the present invention, preferably, the concentration of the lithium salt is from 0.5 mol/L to 3 mol/L.
本发明中,为了进一步提高PEO-PPO-PEO与有机溶剂的互溶性,优选地,有机溶剂选自环状碳酸酯或链状碳酸酯中的一种或几种。PEO-PPO-PEO具有表面活性剂的性能,其尤其能与碳酸酯类电解液互溶性好;同时,也可以改善长周期循环过程中活性材料颗粒与电解液间的接触问题。In the present invention, in order to further improve the mutual solubility of PEO-PPO-PEO and an organic solvent, it is preferred that the organic solvent is one or more selected from the group consisting of a cyclic carbonate or a chain carbonate. PEO-PPO-PEO has the properties of a surfactant, which is especially compatible with carbonate electrolytes; at the same time, it can also improve the contact between active material particles and electrolyte during long-period cycling.
更具体的,所述环状碳酸酯选自碳酸乙烯酯(EC)和/或碳酸丙烯酯(PC)。EC和PC具有较高燃点,且可以在负极形成稳定的SEI膜。More specifically, the cyclic carbonate is selected from the group consisting of ethylene carbonate (EC) and/or propylene carbonate (PC). EC and PC have a higher ignition point and can form a stable SEI film at the negative electrode.
进一步,所述链状碳酸酯选自碳酸二甲酯(DMC)、碳酸二乙酯(DEC)、碳酸二丙酯(DPC)或碳酸甲基乙基酯(EMC)中的一种或几种。以上几种链状碳酸酯具有较低的粘度,可以改善EC或PC粘度过高的问题,提高混合电解液的锂离子扩散能力。Further, the chain carbonate is selected from one or more of dimethyl carbonate (DMC), diethyl carbonate (DEC), dipropyl carbonate (DPC) or methyl ethyl carbonate (EMC). . The above chain carbonates have a lower viscosity, can improve the problem of excessive viscosity of EC or PC, and improve the lithium ion diffusion ability of the mixed electrolyte.
另外,为了改善负极SEI膜的稳定性,在电解液中还添加有负极成膜添加剂,以电解液的总质量为基准,电解液中含有的负极成膜添加剂的质量百分比为0.5%-2%。In addition, in order to improve the stability of the negative electrode SEI film, a negative electrode film-forming additive is further added to the electrolyte, and the mass percentage of the negative electrode film-forming additive contained in the electrolyte is 0.5% to 2% based on the total mass of the electrolyte. .
更具体的,所述负极成膜添加剂为碳酸亚乙烯脂(VC)或氟代碳酸乙烯脂(FEC)。More specifically, the negative film forming additive is vinylene carbonate (VC) or fluoroethylene carbonate (FEC).
在本发明的一些实施例中,所述有机溶剂为碳酸乙烯脂、碳酸二乙酯和碳酸甲基乙基酯组成的混合溶液,所述碳酸乙烯脂、碳酸二乙酯和碳酸甲基乙基酯的体积比为1:1:1。In some embodiments of the invention, the organic solvent is a mixed solution of ethylene carbonate, diethyl carbonate and methyl ethyl carbonate, the ethylene carbonate, diethyl carbonate and methyl ethyl carbonate The volume ratio of the ester was 1:1:1.
另外,本发明还提供了一种电池,包括壳体、容纳在所述壳体内的极芯以及电解液,其中,上述电解液为本发明提供的电解液。Further, the present invention provides a battery comprising a casing, a pole core housed in the casing, and an electrolyte, wherein the electrolyte is the electrolyte provided by the present invention.
在本发明中,上述极芯由正极片、负极片和隔膜卷绕而成。In the present invention, the polar core is formed by winding a positive electrode sheet, a negative electrode sheet, and a separator.
本发明提供的电池的制备方法:The preparation method of the battery provided by the invention:
步骤1、制备电解液:该电解液为上文中所述的本发明提供的电解液; Step 1, preparing an electrolyte: the electrolyte is the electrolyte provided by the present invention described above;
步骤2、制备极芯:将正极片、隔膜和负极片依次层叠后进行卷绕,得 到极芯;Step 2: preparing a polar core: the positive electrode sheet, the separator and the negative electrode sheet are sequentially laminated and then wound to obtain a polar core;
步骤3、封装电池:将步骤2中制备得到的极芯装入壳体内;Step 3, packaging the battery: the pole core prepared in step 2 is loaded into the housing;
步骤4、注液、密封:向壳体内注入电解液并密封,制得电池。Step 4. Injecting liquid and sealing: Injecting an electrolyte into the casing and sealing it to obtain a battery.
实施例1Example 1
(1)正极的制备(1) Preparation of positive electrode
将钴酸锂、乙炔黑、聚四氟乙烯和N-甲基吡咯烷酮按照重量比为100:3:2:50的比例混合搅拌成浆料,将该浆料均匀地涂布在导电基体铝箔的两侧,然后110℃下烘干、辊压、裁切制得尺寸为485毫米×44毫米×0.140毫米的正极片。Lithium cobaltate, acetylene black, polytetrafluoroethylene and N-methylpyrrolidone are mixed and stirred into a slurry at a weight ratio of 100:3:2:50, and the slurry is uniformly coated on a conductive base aluminum foil. On both sides, the film was dried, rolled, and cut at 110 ° C to obtain a positive electrode sheet having a size of 485 mm × 44 mm × 0.140 mm.
(2)负极的制备(2) Preparation of negative electrode
将天然石墨、羧甲基纤维素、丁苯橡胶和水按照100:2:2:180的重量比充分混合搅拌得到均匀的浆料,将该浆料均匀涂布在0.008毫米的导电基体铜箔的两侧,100℃烘干,最后,经裁切制得尺寸为480毫米×45毫米×0.156毫米的负极片。The natural graphite, carboxymethyl cellulose, styrene-butadiene rubber and water are thoroughly mixed and stirred in a weight ratio of 100:2:2:180 to obtain a uniform slurry, and the slurry is uniformly coated on a conductive base copper foil of 0.008 mm. Both sides were dried at 100 ° C, and finally, a negative electrode sheet having a size of 480 mm × 45 mm × 0.156 mm was obtained by cutting.
(3)电池的装配(3) Assembly of the battery
将上述制备的正极片、负极片与聚丙烯膜卷绕成一个方型锂离子电池的极芯,随后将电解液以3.6g/Ah的量注入铝塑膜中,密封,制成软包装锂离子电池S1。电解液的成分为:有机溶剂45ml,选取同时含有EC、EMC和DEC的混合有机溶剂,其中EC、EMC和DEC的体积比为1:1:1;添加剂PEO-PPO-PEO5ml,其中PEO-PPO-PEO的平均分子量为2900;加入一定量的LiPF
6,其浓度为1mol/L。
The positive electrode sheet, the negative electrode sheet and the polypropylene film prepared above were wound into a polar core of a prismatic lithium ion battery, and then the electrolytic solution was injected into the aluminum plastic film at a rate of 3.6 g/Ah, and sealed to prepare a soft-package lithium ion. Battery S1. The composition of the electrolyte is: 45 ml of organic solvent, and a mixed organic solvent containing EC, EMC and DEC is selected, wherein the volume ratio of EC, EMC and DEC is 1:1:1; the additive PEO-PPO-PEO is 5 ml, of which PEO-PPO The average molecular weight of PEO is 2900; a certain amount of LiPF 6 is added at a concentration of 1 mol/L.
实施例2Example 2
采用与实施例1相同的方法步骤制备电池S2,不同的是电解液的成分为:有机溶剂42.5ml,选取同时含有EC、EMC和DEC的混合有机溶剂,其中EC、EMC和DEC的体积比为1:1:1;添加剂PEO-PPO-PEO7.5ml,其中PEO-PPO-PEO的平均分子量为2900;加入一定量的LiPF
6,其浓度为1mol/L。
The battery S2 was prepared in the same manner as in Example 1, except that the composition of the electrolyte was 42.5 ml of an organic solvent, and a mixed organic solvent containing EC, EMC and DEC was selected, wherein the volume ratio of EC, EMC and DEC was 1:1:1; additive PEO-PPO-PEO 7.5ml, wherein the average molecular weight of PEO-PPO-PEO is 2900; a certain amount of LiPF 6 is added at a concentration of 1 mol/L.
实施例3Example 3
采用与实施例1相同的方法步骤制备电池S3,不同的是电解液的成分为:有机溶剂40ml,选取同时含有EC、EMC和DEC的混合有机溶剂,其中EC、 EMC和DEC的体积比为1:1:1;添加剂PEO-PPO-PEO10ml,其中PEO-PPO-PEO的平均分子量为2900;加入一定量的LiPF
6,其浓度为1mol/L。
The battery S3 was prepared in the same manner as in Example 1, except that the composition of the electrolyte was 40 ml of an organic solvent, and a mixed organic solvent containing EC, EMC and DEC was selected, wherein the volume ratio of EC, EMC and DEC was 1. : 1:1; additive PEO-PPO-PEO 10ml, wherein the average molecular weight of PEO-PPO-PEO is 2900; a certain amount of LiPF 6 is added at a concentration of 1 mol/L.
实施例4Example 4
采用与实施例1相同的方法步骤制备电池S4,不同的是添加剂(PEO-PPO-PEO的平均分子量为3500。Battery S4 was prepared in the same manner as in Example 1, except that the additive (PEO-PPO-PEO had an average molecular weight of 3,500.
实施例5Example 5
采用与实施例1相同的方法步骤制备电池S5,不同的是有机溶剂为乙腈。Battery S5 was prepared in the same manner as in Example 1, except that the organic solvent was acetonitrile.
实施例6Example 6
采用与实施例1相同的方法步骤制备电池S6,不同的是电解液的成分中还含有VC的负极成膜添加剂,VC的质量分数为1.5%。Battery S6 was prepared in the same manner as in Example 1, except that the composition of the electrolyte further contained a negative electrode film-forming additive of VC, and the mass fraction of VC was 1.5%.
对比例1Comparative example 1
采用与实施例1相同的方法步骤制备电池DS1,不同的是电解液:50ml的有机溶剂,该有机溶剂选取同时含有EC、EMC和DEC的混合有机溶剂,其中EC、EMC和DEC的体积比为1:1:1;加入一定量的LiPF
6,其浓度为1mol/L。
The battery DS1 was prepared in the same manner as in Example 1, except that the electrolyte: 50 ml of an organic solvent selected from a mixed organic solvent containing EC, EMC and DEC, wherein the volume ratio of EC, EMC and DEC was 1:1:1; a certain amount of LiPF 6 was added at a concentration of 1 mol/L.
性能测试:Performance Testing:
1、对上述实施例1-6制备的电池S1-S6和对比例1制备得到电池DS1进行穿刺实验:先对上述实施例1-6制备的电池S1-S6和对比例1制备得到电池DS1进行充放电,充放电电流大小为0.1C,充放电电压范围是2.65V-4.35V;0.1C循环1圈后,充电至4.35V,2.5Ah容量时,进行穿刺实验。同时检测穿刺实验中电池的温度变化。穿刺实验的详细描述如下:1. The batteries DS1 and S6 prepared in the above Examples 1-6 and Comparative Example 1 were prepared to obtain a battery DS1. The batteries DS1 were prepared by first preparing the batteries S1-S6 prepared in the above Examples 1-6 and Comparative Example 1. Charge and discharge, charge and discharge current is 0.1C, charge and discharge voltage range is 2.65V-4.35V; after 0.1C cycle, charge to 4.35V, 2.5Ah capacity, puncture test. At the same time, the temperature change of the battery in the puncture experiment was detected. A detailed description of the puncture experiment is as follows:
1).0.2C电流充电至上限电压4.20V(4.35V/4.40V),截止条件0.02C;1).0.2C current is charged to the upper limit voltage 4.20V (4.35V/4.40V), the cutoff condition is 0.02C;
2).使用直径3mm的钢针以150mm/s的速度完全刺入电芯的中心,保持刺入状态;2). Use a steel needle with a diameter of 3 mm to completely penetrate the center of the battery core at a speed of 150 mm/s to maintain the piercing state;
3).电芯表面温度下降至35℃以下时终止测试;3) The test is terminated when the surface temperature of the cell drops below 35 °C;
合格标准:Cell温度<200℃、不爆炸、不起火、不冒烟。Eligibility criteria: Cell temperature <200 ° C, no explosion, no fire, no smoke.
2、SEM(扫描电镜)测试:采用仪器型号为JSM-7600F,FESEM/EDS—场发射扫描电镜及附件能谱仪观察极片的表面情况。电池在充放电电压2.75~4.35V范围内,以1C倍率进行充放电循环50圈后,再充电至100%SOC; 然后在充满氩气的手套箱中将电池进行拆解,将正极片分离;最后在手套箱中利用铝塑膜密封袋进行密封处理后,再进行SEM相关表征。2. SEM (Scanning Electron Microscope) Test: The surface of the pole piece was observed by instrument model JSM-7600F, FESEM/EDS-field emission scanning electron microscope and accessory energy spectrometer. The battery is charged and discharged in a range of 2.75 to 4.35 V, and charged and discharged at a rate of 1 C for 50 cycles, and then recharged to 100% SOC; then the battery is disassembled in an argon-filled glove box to separate the positive electrode sheets; Finally, after sealing treatment in an aluminum plastic film sealed bag in a glove box, SEM related characterization was performed.
测试结果如表1。The test results are shown in Table 1.
电池样品Battery sample | 穿刺实验Puncture experiment |
S1S1 | 合格qualified |
S2S2 | 合格qualified |
S3S3 | 合格qualified |
S4S4 | 合格qualified |
S5S5 | 合格qualified |
S6S6 | 合格qualified |
DS1DS1 | 不合格Failed |
实施例1、实施例2、实施例3、实施例4、实施例5和实施例6制备得到的电池,未发生爆炸,也没有剧烈燃烧;The batteries prepared in Example 1, Example 2, Example 3, Example 4, Example 5 and Example 6 did not explode and did not burn vigorously;
对比例制备得到的电池,电池剧烈燃烧,发生爆炸,穿刺未通过。The battery prepared in the comparative example, the battery burned violently, exploded, and the puncture failed.
如图1所示,为上述7个电池进行穿刺实验时,检测得到的电池温度变化图;从图中可以看出,实施例1、实施例2、实施例3、实施例4、实施例5和实施例6在穿刺实验过程中,电池温度随时间的变化较为缓慢,并且不会上升至太高的温度;而对比例在穿刺实验过程中,电池温度随时间变化剧烈上升,并且达到600℃以上的高温。As shown in Fig. 1, when the puncture test is performed on the above seven batteries, the obtained battery temperature change diagram is detected; as can be seen from the figure, the first embodiment, the second embodiment, the third embodiment, the fourth embodiment, and the fifth embodiment And in Example 6 during the puncture experiment, the battery temperature changes slowly with time and does not rise to too high temperature; while the comparative example during the puncture experiment, the battery temperature rises sharply with time and reaches 600 °C. Above the high temperature.
在对比例中,当钢针穿过充满电状态下的电池时,由于钢针是电子导体且直接接触正负极,造成对比例中电池发生内部短路,短时间释放热量,释放可燃气体,隔膜收缩、正负极大面积接触,引发热失控;而在实施例1、实施例2、实施例3、实施例4、实施例5和实施例6,由于电解液中添加有PEO-PPO-PEO,当钢针穿过电池造成内部短路产热时,PEO-PPO-PEO会优 先与PF5等强路易斯酸以及溶剂反应,生成胶状物覆盖在正负极表面,如图2和图3所示,其中,图2为对比例的SEM图,图3实施例3的SEM图;由图2和图3的对比可知,图2对比例的SEM图,分子结构比较蓬松,并且存在较多较大的间隙;而图3实施例3的SEM图,由于表面形成了胶状物,并覆盖在了表面,因此比较致密。图2和图3显示,图2对比例的极片表面,呈现疏松多孔状,与电解液的接触面积非常大,当电池内部温度升高时,会加剧电解液被氧化的速率,从而加速电芯的热失控;而图3实施例3的极片表面,存在一层平坦的覆盖物,隔绝其与电解液间的接触,从而压制电解液被氧化的速率,缓解电池的热失控,增大电池内阻,防止后续的正负极直接接触,同时PEO-PPO-PEO的燃点更高,不易被点燃,更加安全。In the comparative example, when the steel needle passes through the battery in a fully charged state, since the steel needle is an electronic conductor and directly contacts the positive and negative electrodes, the battery in the comparative example is internally short-circuited, releasing heat for a short time, releasing the combustible gas, and the diaphragm. Shrinkage, large-area contact between positive and negative electrodes, causing thermal runaway; and in Example 1, Example 2, Example 3, Example 4, Example 5, and Example 6, PEO-PPO-PEO was added to the electrolyte. When the steel needle passes through the battery to cause internal short-circuit heat generation, PEO-PPO-PEO will preferentially react with strong Lewis acid such as PF5 and solvent to form a gel covering the surface of the positive and negative electrodes, as shown in Figures 2 and 3. 2 is an SEM image of the comparative example, and FIG. 3 is an SEM image of the third embodiment; from the comparison of FIG. 2 and FIG. 3, the SEM image of the comparative example of FIG. 2 has a relatively bulky molecular structure and is relatively large. The gap of the embodiment 3 of Fig. 3 is relatively dense because the surface forms a gel and covers the surface. Fig. 2 and Fig. 3 show that the surface of the pole piece of the comparative example of Fig. 2 is loose and porous, and the contact area with the electrolyte is very large. When the internal temperature of the battery rises, the rate of oxidation of the electrolyte is increased, thereby accelerating the electricity. The thermal runaway of the core; and the surface of the pole piece of Embodiment 3 of Figure 3, there is a flat covering, which isolates the contact with the electrolyte, thereby suppressing the rate at which the electrolyte is oxidized, alleviating the thermal runaway of the battery, and increasing The internal resistance of the battery prevents the direct contact between the positive and negative electrodes, and the PEO-PPO-PEO has a higher ignition point, is not easy to be ignited, and is safer.
以上所述仅为本发明的较佳实施例而已,并不用以限制本发明,凡在本发明的精神和原则之内所作的任何修改、等同替换和改进等,均应包含在本发明的保护范围之内。The above is only the preferred embodiment of the present invention, and is not intended to limit the present invention. Any modifications, equivalent substitutions and improvements made within the spirit and principles of the present invention should be included in the protection of the present invention. Within the scope.
Claims (11)
- 一种锂离子电池电解液,包括锂盐、添加剂和有机溶剂,其特征在于,所述添加剂为聚乙二醇-聚丙二醇-聚乙二醇。A lithium ion battery electrolyte comprising a lithium salt, an additive and an organic solvent, characterized in that the additive is polyethylene glycol-polypropylene glycol-polyethylene glycol.
- 根据权利要求1所述的锂离子电池电解液,其特征在于,以电解液的总体积为基准,所述电解液中包含体积百分比为0.5%-20%的添加剂。The lithium ion battery electrolyte according to claim 1, wherein the electrolyte contains 0.5% to 20% by volume of an additive based on the total volume of the electrolyte.
- 根据权利要求1所述的锂离子电池电解液,其特征在于,所述添加剂的平均分子量为1800-10000。The lithium ion battery electrolyte according to claim 1, wherein the additive has an average molecular weight of from 1800 to 10,000.
- 根据权利要求1所述的锂离子电池电解液,其特征在于,所述锂盐选自LiPF 6、LiBOB、LiTFSI或LiFSI中的一种或几种。 The lithium ion battery electrolyte according to claim 1, wherein the lithium salt is one or more selected from the group consisting of LiPF 6 , LiBOB, LiTFSI, or LiFSI.
- 根据权利要求1或4所述的锂离子电池电解液,其特征在于,所述锂盐的浓度为0.5mol/L-3mol/L。The lithium ion battery electrolyte according to claim 1 or 4, wherein the lithium salt has a concentration of 0.5 mol/L to 3 mol/L.
- 根据权利要求1所述的锂离子电池电解液,其特征在于,所述有机溶剂选自环状碳酸酯或链状碳酸酯中的一种或几种。The lithium ion battery electrolyte according to claim 1, wherein the organic solvent is one or more selected from the group consisting of a cyclic carbonate or a chain carbonate.
- 根据权利要求6所述的锂离子电池电解液,其特征在于,所述环状碳酸酯为碳酸乙烯酯和/或碳酸丙烯酯;所述链状碳酸酯选自碳酸二甲酯、碳酸二乙酯、碳酸二丙酯或碳酸甲基乙基酯中的一种或几种。The lithium ion battery electrolyte according to claim 6, wherein the cyclic carbonate is ethylene carbonate and/or propylene carbonate; the chain carbonate is selected from the group consisting of dimethyl carbonate and diethyl carbonate. One or more of an ester, dipropyl carbonate or methyl ethyl carbonate.
- 根据权利要求6所述的锂离子电池电解液,其特征在于,所述有机溶剂为碳酸乙烯脂、碳酸二乙酯和碳酸甲基乙基酯组成的混合溶液,所述碳酸乙烯脂、碳酸二乙酯和碳酸甲基乙基酯的体积比为1:1:1。The lithium ion battery electrolyte according to claim 6, wherein the organic solvent is a mixed solution composed of ethylene carbonate, diethyl carbonate and methyl ethyl carbonate, the vinyl carbonate and the carbonic acid. The volume ratio of ethyl ester to methyl ethyl carbonate is 1:1:1.
- 根据权利要求1所述的锂离子电池电解液,其特征在于,所述电解液中还含有负极成膜添加剂,以电解液的总质量为基准,所述电解液中含有质量百分比为0.5%-2%的负极成膜添加剂。The lithium ion battery electrolyte according to claim 1, wherein the electrolyte further contains a negative electrode film-forming additive, wherein the electrolyte contains 0.5% by mass based on the total mass of the electrolyte. 2% negative film forming additive.
- 根据权利要求9所述的锂离子电池电解液,其特征在于,所述负极成膜添加剂为碳酸亚乙烯脂或氟代碳酸乙烯脂。The lithium ion battery electrolyte according to claim 9, wherein the negative electrode film forming additive is vinylene carbonate or fluoroethylene carbonate.
- 一种电池,包括壳体、容纳在所述壳体内的极芯以及电解液,其特征在于,所述电解液为权利要求1-10任意一项所述的锂离子电池电解液。A battery comprising a housing, a pole core housed in the housing, and an electrolyte, wherein the electrolyte is the lithium ion battery electrolyte according to any one of claims 1-10.
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Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN1148442A (en) * | 1995-03-02 | 1997-04-23 | 松下电器产业株式会社 | Electrolyte solution for driving electrolytic capacitor and electrolytic capacitor made therewith |
JP2003096232A (en) * | 2001-09-26 | 2003-04-03 | Nitto Denko Corp | Adhesive and porous film and polymer-gel electrolyte obtained from the same and their use |
CN102544582A (en) * | 2010-12-29 | 2012-07-04 | 东莞市杉杉电池材料有限公司 | Electrolyte for power lithium ion battery |
CN105762406A (en) * | 2016-05-10 | 2016-07-13 | 北京石油化工学院 | Organic zinc ion secondary battery |
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---|---|---|---|---|
CN1148442A (en) * | 1995-03-02 | 1997-04-23 | 松下电器产业株式会社 | Electrolyte solution for driving electrolytic capacitor and electrolytic capacitor made therewith |
JP2003096232A (en) * | 2001-09-26 | 2003-04-03 | Nitto Denko Corp | Adhesive and porous film and polymer-gel electrolyte obtained from the same and their use |
CN102544582A (en) * | 2010-12-29 | 2012-07-04 | 东莞市杉杉电池材料有限公司 | Electrolyte for power lithium ion battery |
CN105762406A (en) * | 2016-05-10 | 2016-07-13 | 北京石油化工学院 | Organic zinc ion secondary battery |
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