CN106816634B - pseudo high-concentration lithium-sulfur battery electrolyte and lithium-sulfur battery - Google Patents
pseudo high-concentration lithium-sulfur battery electrolyte and lithium-sulfur battery Download PDFInfo
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- 239000003792 electrolyte Substances 0.000 title claims abstract description 100
- JDZCKJOXGCMJGS-UHFFFAOYSA-N [Li].[S] Chemical compound [Li].[S] JDZCKJOXGCMJGS-UHFFFAOYSA-N 0.000 title claims abstract description 44
- 229910003002 lithium salt Inorganic materials 0.000 claims abstract description 43
- 159000000002 lithium salts Chemical class 0.000 claims abstract description 43
- RTZKZFJDLAIYFH-UHFFFAOYSA-N Diethyl ether Chemical compound CCOCC RTZKZFJDLAIYFH-UHFFFAOYSA-N 0.000 claims abstract description 30
- 239000002904 solvent Substances 0.000 claims abstract description 29
- WNXJIVFYUVYPPR-UHFFFAOYSA-N 1,3-dioxolane Chemical compound C1COCO1 WNXJIVFYUVYPPR-UHFFFAOYSA-N 0.000 claims description 29
- XTHFKEDIFFGKHM-UHFFFAOYSA-N Dimethoxyethane Chemical compound COCCOC XTHFKEDIFFGKHM-UHFFFAOYSA-N 0.000 claims description 23
- 229910052744 lithium Inorganic materials 0.000 claims description 21
- 229920001774 Perfluoroether Polymers 0.000 claims description 15
- 239000007788 liquid Substances 0.000 claims description 8
- 125000002733 (C1-C6) fluoroalkyl group Chemical group 0.000 claims description 4
- 125000003709 fluoroalkyl group Chemical group 0.000 claims description 4
- 239000011149 active material Substances 0.000 claims description 3
- 125000000008 (C1-C10) alkyl group Chemical group 0.000 claims description 2
- 125000004169 (C1-C6) alkyl group Chemical group 0.000 claims description 2
- 229910013188 LiBOB Inorganic materials 0.000 claims description 2
- -1 LiDFOB Inorganic materials 0.000 claims description 2
- 229910001290 LiPF6 Inorganic materials 0.000 claims 1
- 229910012265 LiPO2F2 Inorganic materials 0.000 claims 1
- 229910001496 lithium tetrafluoroborate Inorganic materials 0.000 claims 1
- MCVFFRWZNYZUIJ-UHFFFAOYSA-M lithium;trifluoromethanesulfonate Chemical compound [Li+].[O-]S(=O)(=O)C(F)(F)F MCVFFRWZNYZUIJ-UHFFFAOYSA-M 0.000 claims 1
- 239000011259 mixed solution Substances 0.000 claims 1
- LCGLNKUTAGEVQW-UHFFFAOYSA-N Dimethyl ether Chemical compound COC LCGLNKUTAGEVQW-UHFFFAOYSA-N 0.000 description 36
- HBBGRARXTFLTSG-UHFFFAOYSA-N Lithium ion Chemical compound [Li+] HBBGRARXTFLTSG-UHFFFAOYSA-N 0.000 description 18
- 229910001416 lithium ion Inorganic materials 0.000 description 18
- WHXSMMKQMYFTQS-UHFFFAOYSA-N Lithium Chemical compound [Li] WHXSMMKQMYFTQS-UHFFFAOYSA-N 0.000 description 17
- 239000004210 ether based solvent Substances 0.000 description 11
- 239000005077 polysulfide Substances 0.000 description 10
- 229920001021 polysulfide Polymers 0.000 description 10
- 150000008117 polysulfides Polymers 0.000 description 10
- 238000002360 preparation method Methods 0.000 description 10
- 239000000203 mixture Substances 0.000 description 9
- 238000013508 migration Methods 0.000 description 5
- 230000005012 migration Effects 0.000 description 5
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 4
- 230000000052 comparative effect Effects 0.000 description 4
- 229910052751 metal Inorganic materials 0.000 description 4
- 239000002184 metal Substances 0.000 description 4
- 239000011593 sulfur Substances 0.000 description 4
- 229910052717 sulfur Inorganic materials 0.000 description 4
- 230000000694 effects Effects 0.000 description 3
- 238000012986 modification Methods 0.000 description 3
- 230000004048 modification Effects 0.000 description 3
- 238000007614 solvation Methods 0.000 description 3
- WYURNTSHIVDZCO-UHFFFAOYSA-N Tetrahydrofuran Chemical group C1CCOC1 WYURNTSHIVDZCO-UHFFFAOYSA-N 0.000 description 2
- GJEAMHAFPYZYDE-UHFFFAOYSA-N [C].[S] Chemical compound [C].[S] GJEAMHAFPYZYDE-UHFFFAOYSA-N 0.000 description 2
- 239000002131 composite material Substances 0.000 description 2
- 230000007797 corrosion Effects 0.000 description 2
- 238000005260 corrosion Methods 0.000 description 2
- 238000007599 discharging Methods 0.000 description 2
- 238000004090 dissolution Methods 0.000 description 2
- 150000002170 ethers Chemical class 0.000 description 2
- 239000004744 fabric Substances 0.000 description 2
- 238000012360 testing method Methods 0.000 description 2
- JWUJQDFVADABEY-UHFFFAOYSA-N 2-methyltetrahydrofuran Chemical compound CC1CCCO1 JWUJQDFVADABEY-UHFFFAOYSA-N 0.000 description 1
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- 208000032953 Device battery issue Diseases 0.000 description 1
- 239000002000 Electrolyte additive Substances 0.000 description 1
- PXGOKWXKJXAPGV-UHFFFAOYSA-N Fluorine Chemical compound FF PXGOKWXKJXAPGV-UHFFFAOYSA-N 0.000 description 1
- 229910018091 Li 2 S Inorganic materials 0.000 description 1
- 229910013063 LiBF 4 Inorganic materials 0.000 description 1
- 229910013553 LiNO Inorganic materials 0.000 description 1
- 229910013870 LiPF 6 Inorganic materials 0.000 description 1
- 229910012258 LiPO Inorganic materials 0.000 description 1
- 229910012424 LiSO 3 Inorganic materials 0.000 description 1
- 241000872198 Serjania polyphylla Species 0.000 description 1
- ZWDBUTFCWLVLCQ-UHFFFAOYSA-N [Li]S[Li] Chemical compound [Li]S[Li] ZWDBUTFCWLVLCQ-UHFFFAOYSA-N 0.000 description 1
- 239000006230 acetylene black Substances 0.000 description 1
- 229910052782 aluminium Inorganic materials 0.000 description 1
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 1
- 238000000498 ball milling Methods 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 150000004649 carbonic acid derivatives Chemical class 0.000 description 1
- 150000007942 carboxylates Chemical class 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 238000013461 design Methods 0.000 description 1
- SBZXBUIDTXKZTM-UHFFFAOYSA-N diglyme Chemical compound COCCOCCOC SBZXBUIDTXKZTM-UHFFFAOYSA-N 0.000 description 1
- NKDDWNXOKDWJAK-UHFFFAOYSA-N dimethoxymethane Chemical compound COCOC NKDDWNXOKDWJAK-UHFFFAOYSA-N 0.000 description 1
- 239000011267 electrode slurry Substances 0.000 description 1
- 238000005868 electrolysis reaction Methods 0.000 description 1
- 239000008151 electrolyte solution Substances 0.000 description 1
- 229940021013 electrolyte solution Drugs 0.000 description 1
- 150000002148 esters Chemical class 0.000 description 1
- 229910052731 fluorine Inorganic materials 0.000 description 1
- 239000011737 fluorine Substances 0.000 description 1
- 239000011888 foil Substances 0.000 description 1
- 239000003365 glass fiber Substances 0.000 description 1
- 229920003063 hydroxymethyl cellulose Polymers 0.000 description 1
- 229940031574 hydroxymethyl cellulose Drugs 0.000 description 1
- 238000009413 insulation Methods 0.000 description 1
- 239000013067 intermediate product Substances 0.000 description 1
- 239000002608 ionic liquid Substances 0.000 description 1
- 239000003273 ketjen black Substances 0.000 description 1
- 231100000053 low toxicity Toxicity 0.000 description 1
- 230000014759 maintenance of location Effects 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 239000012266 salt solution Substances 0.000 description 1
- 239000002002 slurry Substances 0.000 description 1
- 229920003048 styrene butadiene rubber Polymers 0.000 description 1
- 238000010998 test method Methods 0.000 description 1
- YLQBMQCUIZJEEH-UHFFFAOYSA-N tetrahydrofuran Natural products C=1C=COC=1 YLQBMQCUIZJEEH-UHFFFAOYSA-N 0.000 description 1
- 238000009489 vacuum treatment Methods 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
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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
-
- 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
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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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- 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
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- General Chemical & Material Sciences (AREA)
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- Condensed Matter Physics & Semiconductors (AREA)
- General Physics & Mathematics (AREA)
- Inorganic Chemistry (AREA)
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Abstract
本发明公开了一种伪高浓度锂硫电池电解液和锂硫电池,该电解液含有锂盐、醚类溶剂和非溶剂溶液,所述锂盐在醚类溶剂中的浓度高于3.0mol/L,锂盐在伪高浓度电解液中的浓度不低于0.5mol/L。本发明提供的电池电解液,可以改善高浓度锂盐的锂硫电池电解液的高粘度和低电导率问题,并且具有不可燃性,可显著提高锂硫电池的电化学性能和安全性。The invention discloses a pseudo-high-concentration lithium-sulfur battery electrolyte and a lithium-sulfur battery. The electrolyte contains a lithium salt, an ether solvent and a non-solvent solution, and the concentration of the lithium salt in the ether solvent is higher than 3.0 mol/ L, the concentration of lithium salt in the pseudo high-concentration electrolyte is not less than 0.5mol/L. The battery electrolyte provided by the invention can improve the problems of high viscosity and low conductivity of lithium-sulfur battery electrolyte with high concentration of lithium salt, has non-flammability, and can significantly improve the electrochemical performance and safety of the lithium-sulfur battery.
Description
技术领域technical field
本发明涉及一种伪高浓度锂硫电池电解液和对应的锂硫电池,特别是涉及一种含有氟代醚的高浓度锂盐的锂硫电池电解液。The invention relates to a pseudo-high-concentration lithium-sulfur battery electrolyte and a corresponding lithium-sulfur battery, in particular to a lithium-sulfur battery electrolyte containing a high-concentration lithium salt of a fluoroether.
背景技术Background technique
锂硫电池理论比容量为1675mAh/g,理论比能量为2600Wh/Kg,远高于现有的锂离子电池。并且硫的储量丰富,价格低廉,低毒无公害。因此,锂硫电池成为下一代高比能锂电池的候选,引起了全世界范围的关注。锂硫电池中间产物多硫化锂会与酯类直接发生反应,锂硫电池一般采用醚类作为电解液溶剂,而不是锂离子电池电解液所采用的碳酸酯和羧酸酯等。多硫化锂在醚类电解液中的溶解度较高,充放电过程中溶解在电解中的多硫化锂会迁移至负极并与金属锂负极发生腐蚀反应,同时消耗正负极的活性物质,造成电池循环性能差、库伦效率低。同时,硫和Li2S的绝缘性、充放电过程中的体积膨胀等也严重影响了锂硫电池的活性物质利用率和循环稳定性,严重阻碍了其实用化进程。The theoretical specific capacity of the lithium-sulfur battery is 1675mAh/g, and the theoretical specific energy is 2600Wh/Kg, much higher than the existing lithium-ion batteries. Moreover, sulfur reserves are abundant, the price is low, low toxicity and no pollution. Therefore, lithium-sulfur batteries have become candidates for next-generation high-energy lithium batteries and have attracted worldwide attention. Lithium polysulfide, an intermediate product of lithium-sulfur batteries, will react directly with esters. Lithium-sulfur batteries generally use ethers as electrolyte solvents instead of carbonates and carboxylates used in lithium-ion battery electrolytes. The solubility of lithium polysulfide in the ether electrolyte is high, and the lithium polysulfide dissolved in the electrolysis during charging and discharging will migrate to the negative electrode and corrode with the metal lithium negative electrode, and consume the active materials of the positive and negative electrodes at the same time, resulting in battery failure. Poor cycle performance and low Coulombic efficiency. At the same time, the insulation of sulfur and Li 2 S and the volume expansion during charging and discharging also seriously affect the utilization rate of active materials and cycle stability of lithium-sulfur batteries, seriously hindering its practical application.
针对锂硫电池的问题,全世界的科研工作者从硫正极微结构设计、功能性隔膜的制备、电解液改性以及金属锂负极的保护等多个方面开展了许多研究工作,取得了显著的效果。其中围绕着锂硫电池电解液的改性,开展了许多工作,比如采用能够溶解锂盐却不能溶解多硫化锂的离子液体作为电解液共溶剂,抑制多硫化锂在电解液中的溶解和迁移。采用LiNO3、KNO3、P2S5等作为电解液添加剂,辅助金属锂负极侧形成比较稳定的SEI膜,抑制溶解在电解液中的多硫化锂与金属锂之间的腐蚀反应。另外,将更多的锂盐溶解在醚类溶剂中,形成高浓度锂盐电解液。高浓度锂盐溶中大部分溶剂分子都参与了锂盐中的锂离子溶剂化,很少有自由的溶剂分子,因而不能再溶解多硫化锂。并且,高浓度锂盐电解液的粘度很高,明显降低了多硫化锂在电解液中的迁移。因此,高浓度锂盐的电解液能明显降低由于多硫化锂在电解液中的溶解和迁移造成的穿梭效应和金属锂负极的腐蚀对电池性能的影响,有助于获得高性能的锂硫电池。Aiming at the problems of lithium-sulfur batteries, researchers around the world have carried out a lot of research work on the microstructure design of sulfur cathodes, the preparation of functional separators, the modification of electrolytes, and the protection of metal lithium anodes, and have achieved remarkable results. Effect. Among them, a lot of work has been carried out around the modification of lithium-sulfur battery electrolytes, such as using ionic liquids that can dissolve lithium salts but not lithium polysulfides as electrolyte co-solvents to inhibit the dissolution and migration of lithium polysulfides in the electrolyte . LiNO 3 , KNO 3 , P 2 S 5 , etc. are used as electrolyte additives to assist the formation of a relatively stable SEI film on the lithium metal negative electrode side and inhibit the corrosion reaction between lithium polysulfide dissolved in the electrolyte and lithium metal. In addition, more lithium salts are dissolved in ether solvents to form high-concentration lithium salt electrolytes. Most of the solvent molecules in the high-concentration lithium salt solution participated in the solvation of lithium ions in the lithium salt, and there were few free solvent molecules, so lithium polysulfide could no longer be dissolved. Moreover, the viscosity of the high-concentration lithium salt electrolyte is very high, which significantly reduces the migration of lithium polysulfide in the electrolyte. Therefore, the electrolyte with a high concentration of lithium salt can significantly reduce the impact of the shuttle effect caused by the dissolution and migration of lithium polysulfide in the electrolyte and the corrosion of the metal lithium negative electrode on battery performance, which is helpful to obtain high-performance lithium-sulfur batteries. .
锂离子电池电解液中的电导率决定于电解液中锂离子的移动性和电解液粘度。但是,高浓度锂盐电解液中大部分溶剂分子参与锂离子的溶剂化而很少有自由的溶剂分子,高浓度锂硫电池电解液存在的主要问题是电解液的粘度高和电导率低。粘度高不利于锂离子的迁移和电解液与电极之间的充分接触,对应的锂硫电池阻抗值较高。电导率较低预示着锂离子在电解液的迁移速率较慢,不利于电池的倍率性能和低温性能。因此,寻找新的方法,解决高浓度锂硫电池电解液粘度高和电导率低的问题是推动高浓度锂硫电池电解液实用化和加快锂硫电池商业化进程的重要途径。The conductivity in the electrolyte of lithium-ion batteries depends on the mobility of lithium ions in the electrolyte and the viscosity of the electrolyte. However, most solvent molecules in high-concentration lithium-salt electrolytes participate in the solvation of lithium ions and there are few free solvent molecules. The main problems of high-concentration lithium-sulfur battery electrolytes are high viscosity and low conductivity of the electrolyte. High viscosity is not conducive to the migration of lithium ions and the full contact between the electrolyte and the electrode, and the corresponding lithium-sulfur battery has a high impedance value. The lower conductivity indicates that the migration rate of lithium ions in the electrolyte is slower, which is not conducive to the rate performance and low temperature performance of the battery. Therefore, finding new ways to solve the problems of high viscosity and low conductivity of high-concentration lithium-sulfur battery electrolytes is an important way to promote the practical application of high-concentration lithium-sulfur battery electrolytes and accelerate the commercialization of lithium-sulfur batteries.
发明内容Contents of the invention
本发明的目的在于提供一种伪高浓度锂硫电池电解液,能够解决高浓度锂硫电池电解液的高粘度和低电导率的问题。The purpose of the present invention is to provide a pseudo-high-concentration lithium-sulfur battery electrolyte, which can solve the problems of high viscosity and low conductivity of the high-concentration lithium-sulfur battery electrolyte.
本发明提供具体的技术方案如下:The present invention provides concrete technical scheme as follows:
一种伪高浓度锂硫电池电解液,其特征在于:A pseudo-high-concentration lithium-sulfur battery electrolyte, characterized in that:
所述电解液含有锂盐、醚类溶剂和非溶剂液体;The electrolyte contains lithium salt, ether solvent and non-solvent liquid;
所述锂盐在醚类溶剂中的浓度不低于3mol/L;The concentration of the lithium salt in the ether solvent is not less than 3mol/L;
所述的非溶剂液体对锂盐的溶解度低于0.1mol/L。The solubility of the non-solvent liquid to lithium salt is lower than 0.1mol/L.
作为优选,所述锂盐在醚类溶剂中的摩尔浓度高于3.0mol/L,且所述锂盐在伪高浓度电解液中的整体浓度高于0.5mol/L。Preferably, the molar concentration of the lithium salt in the ether solvent is higher than 3.0 mol/L, and the overall concentration of the lithium salt in the pseudo high-concentration electrolyte is higher than 0.5 mol/L.
作为优选,所述非溶剂液体优选自以下结构式(I)所示的氟代醚中的至少一种Preferably, the non-solvent liquid is preferably selected from at least one of the fluoroethers represented by the following structural formula (I):
其中:Rf1、Rf2独立地选自C1~C10的烷基或C1~C10的氟代烷基,且至少一个选自C1~C10的氟代烷基。。Wherein: Rf 1 and Rf 2 are independently selected from C1-C10 alkyl groups or C1-C10 fluoroalkyl groups, and at least one is selected from C1-C10 fluoroalkyl groups. .
更优选的,所述Rf1、Rf2独立地优选自C1~C6的氟代烷基或C1~C6的烷基,且至少一个选自C1~C6的氟代烷基。More preferably, the Rf 1 and Rf 2 are independently preferably selected from C1-C6 fluoroalkyl groups or C1-C6 alkyl groups, and at least one is selected from C1-C6 fluoroalkyl groups.
作为优选,所述电解液中,氟代醚的质量分数为5~90%,醚类溶剂溶剂的质量分数为20~98%。Preferably, in the electrolyte, the mass fraction of the fluoroether is 5-90%, and the mass fraction of the ether solvent is 20-98%.
更优选的,所述电解液中,氟代醚的质量分数为30~60%,醚类溶剂的质量分数为40~70%。More preferably, in the electrolyte, the mass fraction of fluoroether is 30-60%, and the mass fraction of ether solvent is 40-70%.
作为优选,所述锂盐选自LiPF6、LiBF4、LiBOB、LiDFOB、LiPO2F2、LiSO3CF3、双三氟甲基磺酰亚胺锂(LiTFSI)和双氟磺酰亚胺锂(LiFSI)中的至少一种。Preferably, the lithium salt is selected from LiPF 6 , LiBF 4 , LiBOB, LiDFOB, LiPO 2 F 2 , LiSO 3 CF 3 , lithium bistrifluoromethylsulfonylimide (LiTFSI) and lithium bisfluorosulfonylimide (LiFSI) at least one.
作为优选,所述醚类溶剂选自四氢呋喃、2-甲基四氢呋喃、1,3-二氧环戊烷、乙二醇二甲醚、二甲氧甲烷、1,2-二甲氧乙烷和二甘醇二甲醚中的至少一种;Preferably, the ether solvent is selected from tetrahydrofuran, 2-methyltetrahydrofuran, 1,3-dioxolane, ethylene glycol dimethyl ether, dimethoxymethane, 1,2-dimethoxyethane and At least one of diglyme;
一种锂硫电池,采用如上所述的电解液。A lithium-sulfur battery adopts the above electrolyte.
本发明是在高浓度锂硫电池电解液中添加适量的非溶剂液体,尤其是氟代醚。首先氟代醚中的氟具有很强的电负性和弱极性,因而醚类溶剂被氟代之后溶解性大幅下降,很多不能溶解锂盐和多硫化锂。因而,氟代醚的添加不会改变高浓度锂盐电解液中锂离子和溶剂分子溶剂化状态,形成的新的电解液性能与高浓度锂盐电解液性能类似,虽然整体上看新的电解液锂盐浓度有所降低,这种新的电解液被命名为伪高浓度锂盐锂硫电池电解液。The invention adds a proper amount of non-solvent liquid, especially fluorinated ether, to the high-concentration lithium-sulfur battery electrolyte. First of all, the fluorine in fluoroethers has strong electronegativity and weak polarity, so the solubility of ether solvents is greatly reduced after being fluorinated, and many of them cannot dissolve lithium salts and lithium polysulfides. Therefore, the addition of fluoroether will not change the solvation state of lithium ions and solvent molecules in the high-concentration lithium-salt electrolyte, and the performance of the new electrolyte is similar to that of the high-concentration lithium-salt electrolyte. The concentration of liquid lithium salt is reduced, and this new electrolyte is named pseudo-high-concentration lithium-salt lithium-sulfur battery electrolyte.
相对于高浓度锂盐电解液,伪高浓度锂盐电解液中添加了适量的氟代醚。氟代醚粘度很低,对电极、隔膜都具有比较好的润湿性。因此,伪高浓度锂盐电解液粘度明显下降,引起电解液电导率增加。另外,氟代醚本身是不可燃的,因而氟代醚的添加还能在一定程度上降低电解液的可燃性,甚至获得不可燃的电解液。Compared with the high-concentration lithium-salt electrolyte, an appropriate amount of fluoroether is added to the pseudo-high-concentration lithium-salt electrolyte. Fluoroethers have very low viscosity and have good wettability to electrodes and separators. Therefore, the viscosity of the pseudo-high-concentration lithium salt electrolyte decreased significantly, causing an increase in the conductivity of the electrolyte. In addition, the fluoroether itself is non-flammable, so the addition of fluoroether can also reduce the flammability of the electrolyte to a certain extent, and even obtain a non-flammable electrolyte.
具体实施方式Detailed ways
下面结合具体实施例来对本发明进行进一步说明,但并不将本发明局限于这些具体实施方式。本领域技术人员应该认识到,本发明涵盖了权利要求书范围内所可能包括的所有备选方案、改进方案和等效方案。The present invention will be further described below in conjunction with specific examples, but the present invention is not limited to these specific implementations. Those skilled in the art will realize that the present invention covers all alternatives, modifications and equivalents as may be included within the scope of the claims.
以下实施例中所述氟代醚的缩写如下:The abbreviations of fluoroethers described in the following examples are as follows:
HFMOP为(CF3)2CHOCH3,HFEOP为(CF3)2CHOCH2CH3,HFTFPOP为(CF3)2CHOCH2CF2CF2H,TFEOTFP为HCF2CF2OCH2CF2CF2H,TFEOPFP为HCF2CF2OCH2CF2CF3,HFPEE为CF3CF2CHFOCH2CH3。HFMOP is (CF 3 ) 2 CHOCH 3 , HFEOP is (CF 3 ) 2 CHOCH 2 CH 3 , HFTFPOP is (CF 3 ) 2 CHOCH 2 CF 2 CF 2 H, TFEOTFP is HCF 2 CF 2 OCH 2 CF 2 CF 2 H , TFEOPFP is HCF 2 CF 2 OCH 2 CF 2 CF 3 , HFPEE is CF 3 CF 2 CHFOCH 2 CH 3 .
实施例1Example 1
一种锂离子电池电解液,包括1,3二氧戊环(DOL)、乙二醇二甲醚(DME)两种醚类溶剂,以LiTFSI为锂盐。其制备方法为:将DOL、DME按体积比1∶1混合,然后加入LiTFSI,使之浓度达到5.0mol/L。之后向电解液中加入HFMOP,使HFMOP在电解液中的质量分数为40%,得到锂硫电池电解液。A lithium-ion battery electrolyte, including 1,3 dioxolane (DOL) and ethylene glycol dimethyl ether (DME) two ether solvents, with LiTFSI as lithium salt. The preparation method is as follows: mix DOL and DME at a volume ratio of 1:1, and then add LiTFSI to make the concentration reach 5.0 mol/L. Afterwards, HFMOP is added to the electrolyte, so that the mass fraction of HFMOP in the electrolyte is 40%, so as to obtain the lithium-sulfur battery electrolyte.
实施例2Example 2
一种锂离子电池电解液,包括1,3二氧戊环(DOL)、乙二醇二甲醚(DME)两种醚类溶剂,以LiTFSI为锂盐。其制备方法为:将DOL、DME按体积比1∶1混合,然后加入LiTFSI,使之浓度达到5.0mol/L。之后向电解液中加入HFEOP,使HFEOP在电解液中的质量分数为50%,得到锂硫电池电解液。A lithium-ion battery electrolyte, including 1,3 dioxolane (DOL) and ethylene glycol dimethyl ether (DME) two ether solvents, with LiTFSI as lithium salt. The preparation method is as follows: mix DOL and DME at a volume ratio of 1:1, and then add LiTFSI to make the concentration reach 5.0 mol/L. Then add HFEOP to the electrolyte, so that the mass fraction of HFEOP in the electrolyte is 50%, to obtain the lithium-sulfur battery electrolyte.
实施例3Example 3
一种锂离子电池电解液,包括1,3二氧戊环(DOL)、乙二醇二甲醚(DME)两种醚类溶剂,以LiTFSI为锂盐。其制备方法为:将DOL、DME按体积比1∶1混合,然后加入LiTFSI,使之浓度达到5.0mol/L。之后向电解液中加入HFTFPOP,使HFTFPOP在电解液中的质量分数为60%,得到锂硫电池电解液。A lithium-ion battery electrolyte, including 1,3 dioxolane (DOL) and ethylene glycol dimethyl ether (DME) two ether solvents, with LiTFSI as lithium salt. The preparation method is as follows: mix DOL and DME at a volume ratio of 1:1, and then add LiTFSI to make the concentration reach 5.0 mol/L. Then add HFTFPOP to the electrolyte, so that the mass fraction of HFTFPOP in the electrolyte is 60%, to obtain the lithium-sulfur battery electrolyte.
实施例4Example 4
一种锂离子电池电解液,包括1,3二氧戊环(DOL)、乙二醇二甲醚(DME)两种醚类溶剂,以LiTFSI为锂盐。其制备方法为:将DOL、DME按体积比1∶1混合,然后加入LiTFSI,使之浓度达到5.0mol/L。之后向电解液中加入TFEOTFP,使TFEOTFP在电解液中的质量分数为60%,得到锂硫电池电解液。A lithium-ion battery electrolyte, including 1,3 dioxolane (DOL) and ethylene glycol dimethyl ether (DME) two ether solvents, with LiTFSI as lithium salt. The preparation method is as follows: mix DOL and DME at a volume ratio of 1:1, and then add LiTFSI to make the concentration reach 5.0 mol/L. Afterwards, TFEOTFP is added to the electrolyte so that the mass fraction of TFEOTFP in the electrolyte is 60%, so as to obtain an electrolyte for a lithium-sulfur battery.
实施例5Example 5
一种锂离子电池电解液,包括1,3二氧戊环(DOL)、乙二醇二甲醚(DME)两种醚类溶剂,以LiTFSI为锂盐。其制备方法为:将DOL、DME按体积比1∶1混合,然后加入LiTFSI,使之浓度达到7.0mol/L。之后向电解液中加入TFEOPFP,使TFEOPFP在电解液中的质量分数为60%,得到锂硫电池电解液。A lithium-ion battery electrolyte, including 1,3 dioxolane (DOL) and ethylene glycol dimethyl ether (DME) two ether solvents, with LiTFSI as lithium salt. The preparation method is as follows: mix DOL and DME at a volume ratio of 1:1, and then add LiTFSI to make the concentration reach 7.0 mol/L. Afterwards, TFEOPFP is added to the electrolyte, so that the mass fraction of TFEOPFP in the electrolyte is 60%, so as to obtain the lithium-sulfur battery electrolyte.
实施例6Example 6
一种锂离子电池电解液,包括1,3二氧戊环(DOL)、乙二醇二甲醚(DME)两种醚类溶剂,以LiTFSI为锂盐。其制备方法为:将DOL、DME按体积比1∶1混合,然后加入LiTFSI,使之浓度达到7.0mol/L。之后向电解液中加入HFPEE,使HFPEE在电解液中的质量分数为60%,得到锂硫电池电解液。A lithium-ion battery electrolyte, including 1,3 dioxolane (DOL) and ethylene glycol dimethyl ether (DME) two ether solvents, with LiTFSI as lithium salt. The preparation method is as follows: mix DOL and DME at a volume ratio of 1:1, and then add LiTFSI to make the concentration reach 7.0 mol/L. Then add HFPEE to the electrolyte, so that the mass fraction of HFPEE in the electrolyte is 60%, to obtain the lithium-sulfur battery electrolyte.
对比例1Comparative example 1
一种锂离子电池电解液,包括1,3二氧戊环(DOL)、乙二醇二甲醚(DME)两种醚类溶剂,以LiTFSI为锂盐。其制备方法为:将DOL、DME按体积比1∶1混合,然后加入LiTFSI,使之浓度达到1.0mol/L。A lithium-ion battery electrolyte, including 1,3 dioxolane (DOL) and ethylene glycol dimethyl ether (DME) two ether solvents, with LiTFSI as lithium salt. The preparation method is as follows: mix DOL and DME at a volume ratio of 1:1, and then add LiTFSI to make the concentration reach 1.0 mol/L.
对比例2Comparative example 2
一种锂离子电池电解液,包括1,3二氧戊环(DOL)、乙二醇二甲醚(DME)两种醚类溶剂,以LiTFSI为锂盐。其制备方法为:将DOL、DME按体积比1∶1混合,然后加入LiTFSI,使之浓度达到5.0mol/L。A lithium-ion battery electrolyte, including 1,3 dioxolane (DOL) and ethylene glycol dimethyl ether (DME) two ether solvents, with LiTFSI as lithium salt. The preparation method is as follows: mix DOL and DME at a volume ratio of 1:1, and then add LiTFSI to make the concentration reach 5.0 mol/L.
对比例3Comparative example 3
一种锂离子电池电解液,包括1,3二氧戊环(DOL)、乙二醇二甲醚(DME)两种醚类溶剂,以LiTFSI为锂盐。其制备方法为:将DOL、DME按体积比1∶1混合,然后加入LiTFSI,使之浓度达到7.0mol/L。A lithium-ion battery electrolyte, including 1,3 dioxolane (DOL) and ethylene glycol dimethyl ether (DME) two ether solvents, with LiTFSI as lithium salt. The preparation method is as follows: mix DOL and DME at a volume ratio of 1:1, and then add LiTFSI to make the concentration reach 7.0 mol/L.
将实施例1至6和对比例1至3制备得到的电解液,进行测试。The electrolyte solutions prepared in Examples 1 to 6 and Comparative Examples 1 to 3 were tested.
主要测试方法:Main test methods:
(1)采用2cm*10cm的玻璃纤维布浸润在电解液中1min,测试浸润电解液后的布条可燃性和自熄时间。(1) Use a 2cm*10cm glass fiber cloth to soak in the electrolyte for 1 minute, and test the flammability and self-extinguishing time of the cloth soaked in the electrolyte.
(2)20℃下电解液的电导率、粘度及其与隔膜的接触角;(2) The conductivity, viscosity and contact angle of the electrolyte with the diaphragm at 20°C;
(3)将质量比为2:1的硫和科琴黑混合均匀后,在155℃下真空处理12h获得硫碳复合材料。将硫碳复合材料:乙炔黑:羟甲基纤维素+丁苯橡胶=8:1:1分散到适量的水中,球磨6h后获得电极浆料。将得到的浆料涂覆于铝箔上,红外灯下干燥后,真空60℃下干燥12h,裁切成直径为14mm的电极片备用。之后,采用上述电解液、金属锂为负极、Cegrald2400为隔膜组装锂硫电池,0.2C倍率下测试锂硫电池的循环50周后的循环性能。测试结果如下:(3) After mixing sulfur and Ketjen black with a mass ratio of 2:1, vacuum treatment at 155 °C for 12 h to obtain a sulfur-carbon composite material. Sulfur-carbon composite material: acetylene black: hydroxymethyl cellulose + styrene-butadiene rubber = 8:1:1 was dispersed in an appropriate amount of water, and the electrode slurry was obtained after ball milling for 6 hours. The obtained slurry was coated on an aluminum foil, dried under an infrared lamp, then dried under vacuum at 60° C. for 12 hours, and cut into electrode sheets with a diameter of 14 mm for use. Afterwards, a lithium-sulfur battery was assembled using the above-mentioned electrolyte, metal lithium as the negative electrode, and Cegrald2400 as the diaphragm, and the cycle performance of the lithium-sulfur battery after 50 cycles was tested at a rate of 0.2C. The test results are as follows:
表1Table 1
由表1可知,本发明提供的伪高浓度锂盐电解液与高浓度锂盐电解液相比,克服了其原有的缺点,具有粘度低、电导率高、与隔膜的接触角较小等优点。而且,该伪高浓度锂盐的电解液保留了高浓度锂盐电解液的优点,如由于穿梭效应被抑制而获得的较低的平均库伦效率和较高的容量保持率。同时,伪高浓度电解液中添加了一定量的不可燃的氟代醚,电解液整体不可燃,进一步提升了电解液的安全性。As can be seen from Table 1, compared with the high-concentration lithium salt electrolyte, the pseudo high-concentration lithium salt electrolyte provided by the present invention overcomes its original shortcomings, and has low viscosity, high electrical conductivity, and small contact angle with the separator. advantage. Moreover, the pseudo-high-concentration Li-salt electrolyte retains the advantages of the high-concentration Li-salt electrolyte, such as lower average Coulombic efficiency and higher capacity retention due to the suppressed shuttling effect. At the same time, a certain amount of non-flammable fluoroether is added to the pseudo-high-concentration electrolyte, and the electrolyte as a whole is non-flammable, which further improves the safety of the electrolyte.
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