CN102569885A - Non-aqueous electrolyte for lithium ion battery and lithium ion secondary battery - Google Patents
Non-aqueous electrolyte for lithium ion battery and lithium ion secondary battery Download PDFInfo
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- CN102569885A CN102569885A CN2011104511322A CN201110451132A CN102569885A CN 102569885 A CN102569885 A CN 102569885A CN 2011104511322 A CN2011104511322 A CN 2011104511322A CN 201110451132 A CN201110451132 A CN 201110451132A CN 102569885 A CN102569885 A CN 102569885A
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- electrolyte
- lithium
- carbonate
- battery
- cyclic
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- HBBGRARXTFLTSG-UHFFFAOYSA-N Lithium ion Chemical compound [Li+] HBBGRARXTFLTSG-UHFFFAOYSA-N 0.000 title claims abstract description 50
- 229910001416 lithium ion Inorganic materials 0.000 title claims abstract description 50
- 239000011255 nonaqueous electrolyte Substances 0.000 title claims abstract description 18
- 239000003792 electrolyte Substances 0.000 claims abstract description 86
- -1 cyclic carboxylic ester Chemical class 0.000 claims abstract description 34
- 229920001774 Perfluoroether Polymers 0.000 claims abstract description 28
- 125000000217 alkyl group Chemical group 0.000 claims abstract description 12
- 125000004432 carbon atom Chemical group C* 0.000 claims abstract description 12
- 239000004094 surface-active agent Substances 0.000 claims abstract description 12
- YCKRFDGAMUMZLT-UHFFFAOYSA-N Fluorine atom Chemical compound [F] YCKRFDGAMUMZLT-UHFFFAOYSA-N 0.000 claims abstract description 10
- 229910052731 fluorine Inorganic materials 0.000 claims abstract description 10
- 239000011737 fluorine Substances 0.000 claims abstract description 10
- NBVXSUQYWXRMNV-UHFFFAOYSA-N fluoromethane Chemical compound FC NBVXSUQYWXRMNV-UHFFFAOYSA-N 0.000 claims abstract description 10
- YEJRWHAVMIAJKC-UHFFFAOYSA-N 4-Butyrolactone Chemical compound O=C1CCCO1 YEJRWHAVMIAJKC-UHFFFAOYSA-N 0.000 claims description 29
- 239000008151 electrolyte solution Substances 0.000 claims description 27
- 229910013870 LiPF 6 Inorganic materials 0.000 claims description 19
- 239000000654 additive Substances 0.000 claims description 13
- 229910003002 lithium salt Inorganic materials 0.000 claims description 13
- 159000000002 lithium salts Chemical class 0.000 claims description 13
- 150000005676 cyclic carbonates Chemical class 0.000 claims description 10
- 229910013063 LiBF 4 Inorganic materials 0.000 claims description 9
- IEJIGPNLZYLLBP-UHFFFAOYSA-N dimethyl carbonate Chemical compound COC(=O)OC IEJIGPNLZYLLBP-UHFFFAOYSA-N 0.000 claims description 9
- QAOWNCQODCNURD-UHFFFAOYSA-N sulfuric acid Substances OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 claims description 9
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical group [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 8
- XEKOWRVHYACXOJ-UHFFFAOYSA-N Ethyl acetate Chemical compound CCOC(C)=O XEKOWRVHYACXOJ-UHFFFAOYSA-N 0.000 claims description 6
- KMTRUDSVKNLOMY-UHFFFAOYSA-N Ethylene carbonate Chemical compound O=C1OCCO1 KMTRUDSVKNLOMY-UHFFFAOYSA-N 0.000 claims description 6
- 229910013716 LiNi Inorganic materials 0.000 claims description 6
- 239000011149 active material Substances 0.000 claims description 6
- 150000007942 carboxylates Chemical class 0.000 claims description 6
- 229910002804 graphite Inorganic materials 0.000 claims description 6
- 239000010439 graphite Substances 0.000 claims description 6
- 229910013188 LiBOB Inorganic materials 0.000 claims description 5
- WHXSMMKQMYFTQS-UHFFFAOYSA-N Lithium Chemical compound [Li] WHXSMMKQMYFTQS-UHFFFAOYSA-N 0.000 claims description 5
- 230000000996 additive effect Effects 0.000 claims description 5
- 229910052744 lithium Inorganic materials 0.000 claims description 5
- 239000000203 mixture Substances 0.000 claims description 5
- VAYTZRYEBVHVLE-UHFFFAOYSA-N 1,3-dioxol-2-one Chemical compound O=C1OC=CO1 VAYTZRYEBVHVLE-UHFFFAOYSA-N 0.000 claims description 4
- 229910012851 LiCoO 2 Inorganic materials 0.000 claims description 4
- 150000005678 chain carbonates Chemical class 0.000 claims description 4
- FKRCODPIKNYEAC-UHFFFAOYSA-N ethyl propionate Chemical compound CCOC(=O)CC FKRCODPIKNYEAC-UHFFFAOYSA-N 0.000 claims description 4
- 125000004435 hydrogen atom Chemical group [H]* 0.000 claims description 4
- ZZXUZKXVROWEIF-UHFFFAOYSA-N 1,2-butylene carbonate Chemical compound CCC1COC(=O)O1 ZZXUZKXVROWEIF-UHFFFAOYSA-N 0.000 claims description 3
- FSSPGSAQUIYDCN-UHFFFAOYSA-N 1,3-Propane sultone Chemical compound O=S1(=O)CCCO1 FSSPGSAQUIYDCN-UHFFFAOYSA-N 0.000 claims description 3
- HNAGHMKIPMKKBB-UHFFFAOYSA-N 1-benzylpyrrolidine-3-carboxamide Chemical compound C1C(C(=O)N)CCN1CC1=CC=CC=C1 HNAGHMKIPMKKBB-UHFFFAOYSA-N 0.000 claims description 3
- SBLRHMKNNHXPHG-UHFFFAOYSA-N 4-fluoro-1,3-dioxolan-2-one Chemical compound FC1COC(=O)O1 SBLRHMKNNHXPHG-UHFFFAOYSA-N 0.000 claims description 3
- OIFBSDVPJOWBCH-UHFFFAOYSA-N Diethyl carbonate Chemical compound CCOC(=O)OCC OIFBSDVPJOWBCH-UHFFFAOYSA-N 0.000 claims description 3
- JGFBQFKZKSSODQ-UHFFFAOYSA-N Isothiocyanatocyclopropane Chemical compound S=C=NC1CC1 JGFBQFKZKSSODQ-UHFFFAOYSA-N 0.000 claims description 3
- 229910013684 LiClO 4 Inorganic materials 0.000 claims description 3
- 229910010707 LiFePO 4 Inorganic materials 0.000 claims description 3
- 229910015643 LiMn 2 O 4 Inorganic materials 0.000 claims description 3
- 229910013528 LiN(SO2 CF3)2 Inorganic materials 0.000 claims description 3
- LSNNMFCWUKXFEE-UHFFFAOYSA-N Sulfurous acid Chemical compound OS(O)=O LSNNMFCWUKXFEE-UHFFFAOYSA-N 0.000 claims description 3
- RTAQQCXQSZGOHL-UHFFFAOYSA-N Titanium Chemical compound [Ti] RTAQQCXQSZGOHL-UHFFFAOYSA-N 0.000 claims description 3
- 239000000956 alloy Substances 0.000 claims description 3
- OBNCKNCVKJNDBV-UHFFFAOYSA-N butanoic acid ethyl ester Natural products CCCC(=O)OCC OBNCKNCVKJNDBV-UHFFFAOYSA-N 0.000 claims description 3
- PWLNAUNEAKQYLH-UHFFFAOYSA-N butyric acid octyl ester Natural products CCCCCCCCOC(=O)CCC PWLNAUNEAKQYLH-UHFFFAOYSA-N 0.000 claims description 3
- NVJBFARDFTXOTO-UHFFFAOYSA-N diethyl sulfite Chemical compound CCOS(=O)OCC NVJBFARDFTXOTO-UHFFFAOYSA-N 0.000 claims description 3
- BDUPRNVPXOHWIL-UHFFFAOYSA-N dimethyl sulfite Chemical compound COS(=O)OC BDUPRNVPXOHWIL-UHFFFAOYSA-N 0.000 claims description 3
- RBBXSUBZFUWCAV-UHFFFAOYSA-N ethenyl hydrogen sulfite Chemical compound OS(=O)OC=C RBBXSUBZFUWCAV-UHFFFAOYSA-N 0.000 claims description 3
- JBTWLSYIZRCDFO-UHFFFAOYSA-N ethyl methyl carbonate Chemical compound CCOC(=O)OC JBTWLSYIZRCDFO-UHFFFAOYSA-N 0.000 claims description 3
- FMQCKJHUYDYTMA-UHFFFAOYSA-N ethyl methyl sulfite Chemical compound CCOS(=O)OC FMQCKJHUYDYTMA-UHFFFAOYSA-N 0.000 claims description 3
- KKQAVHGECIBFRQ-UHFFFAOYSA-N methyl propyl carbonate Chemical compound CCCOC(=O)OC KKQAVHGECIBFRQ-UHFFFAOYSA-N 0.000 claims description 3
- UUIQMZJEGPQKFD-UHFFFAOYSA-N n-butyric acid methyl ester Natural products CCCC(=O)OC UUIQMZJEGPQKFD-UHFFFAOYSA-N 0.000 claims description 3
- RUOJZAUFBMNUDX-UHFFFAOYSA-N propylene carbonate Chemical compound CC1COC(=O)O1 RUOJZAUFBMNUDX-UHFFFAOYSA-N 0.000 claims description 3
- 229910052710 silicon Inorganic materials 0.000 claims description 3
- 229910052718 tin Inorganic materials 0.000 claims description 3
- UHOPWFKONJYLCF-UHFFFAOYSA-N 2-(2-sulfanylethyl)isoindole-1,3-dione Chemical compound C1=CC=C2C(=O)N(CCS)C(=O)C2=C1 UHOPWFKONJYLCF-UHFFFAOYSA-N 0.000 claims description 2
- GVNVAWHJIKLAGL-UHFFFAOYSA-N 2-(cyclohexen-1-yl)cyclohexan-1-one Chemical compound O=C1CCCCC1C1=CCCCC1 GVNVAWHJIKLAGL-UHFFFAOYSA-N 0.000 claims description 2
- OMQHDIHZSDEIFH-UHFFFAOYSA-N 3-Acetyldihydro-2(3H)-furanone Chemical compound CC(=O)C1CCOC1=O OMQHDIHZSDEIFH-UHFFFAOYSA-N 0.000 claims description 2
- 101150065749 Churc1 gene Proteins 0.000 claims description 2
- 229910013385 LiN(SO2C2F5)2 Inorganic materials 0.000 claims description 2
- RJUFJBKOKNCXHH-UHFFFAOYSA-N Methyl propionate Chemical compound CCC(=O)OC RJUFJBKOKNCXHH-UHFFFAOYSA-N 0.000 claims description 2
- XBDQKXXYIPTUBI-UHFFFAOYSA-M Propionate Chemical compound CCC([O-])=O XBDQKXXYIPTUBI-UHFFFAOYSA-M 0.000 claims description 2
- 102100038239 Protein Churchill Human genes 0.000 claims description 2
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 claims description 2
- KXKVLQRXCPHEJC-UHFFFAOYSA-N acetic acid trimethyl ester Natural products COC(C)=O KXKVLQRXCPHEJC-UHFFFAOYSA-N 0.000 claims description 2
- 150000001408 amides Chemical class 0.000 claims description 2
- 150000001412 amines Chemical class 0.000 claims description 2
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical group [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims description 2
- VUPKGFBOKBGHFZ-UHFFFAOYSA-N dipropyl carbonate Chemical compound CCCOC(=O)OCCC VUPKGFBOKBGHFZ-UHFFFAOYSA-N 0.000 claims description 2
- 229940093499 ethyl acetate Drugs 0.000 claims description 2
- CYEDOLFRAIXARV-UHFFFAOYSA-N ethyl propyl carbonate Chemical compound CCCOC(=O)OCC CYEDOLFRAIXARV-UHFFFAOYSA-N 0.000 claims description 2
- 125000000524 functional group Chemical group 0.000 claims description 2
- GAEKPEKOJKCEMS-UHFFFAOYSA-N gamma-valerolactone Chemical compound CC1CCC(=O)O1 GAEKPEKOJKCEMS-UHFFFAOYSA-N 0.000 claims description 2
- 229940017219 methyl propionate Drugs 0.000 claims description 2
- YKYONYBAUNKHLG-UHFFFAOYSA-N n-Propyl acetate Natural products CCCOC(C)=O YKYONYBAUNKHLG-UHFFFAOYSA-N 0.000 claims description 2
- 229910052760 oxygen Inorganic materials 0.000 claims description 2
- 239000001301 oxygen Substances 0.000 claims description 2
- 229940090181 propyl acetate Drugs 0.000 claims description 2
- LSNNMFCWUKXFEE-UHFFFAOYSA-L sulfite Chemical class [O-]S([O-])=O LSNNMFCWUKXFEE-UHFFFAOYSA-L 0.000 claims description 2
- 229940124530 sulfonamide Drugs 0.000 claims description 2
- 150000003456 sulfonamides Chemical class 0.000 claims description 2
- 229910052717 sulfur Inorganic materials 0.000 claims description 2
- 239000011593 sulfur Substances 0.000 claims description 2
- 229910000314 transition metal oxide Inorganic materials 0.000 claims description 2
- NQPDZGIKBAWPEJ-UHFFFAOYSA-N valeric acid Chemical compound CCCCC(O)=O NQPDZGIKBAWPEJ-UHFFFAOYSA-N 0.000 claims description 2
- XDJSUFKXJGFOKY-UHFFFAOYSA-N 1,3-dioxolan-2-one;ethene Chemical compound C=C.O=C1OCCO1 XDJSUFKXJGFOKY-UHFFFAOYSA-N 0.000 claims 1
- 125000004122 cyclic group Chemical group 0.000 abstract description 9
- QAOWNCQODCNURD-UHFFFAOYSA-L Sulfate Chemical compound [O-]S([O-])(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-L 0.000 abstract description 8
- 229910052799 carbon Inorganic materials 0.000 abstract description 3
- 230000001351 cycling effect Effects 0.000 abstract 1
- 150000003839 salts Chemical class 0.000 abstract 1
- 230000000052 comparative effect Effects 0.000 description 37
- 238000000034 method Methods 0.000 description 31
- 230000008569 process Effects 0.000 description 28
- 238000003860 storage Methods 0.000 description 24
- 239000002904 solvent Substances 0.000 description 22
- 230000014759 maintenance of location Effects 0.000 description 16
- 238000009835 boiling Methods 0.000 description 15
- 239000003063 flame retardant Substances 0.000 description 11
- RNFJDJUURJAICM-UHFFFAOYSA-N 2,2,4,4,6,6-hexaphenoxy-1,3,5-triaza-2$l^{5},4$l^{5},6$l^{5}-triphosphacyclohexa-1,3,5-triene Chemical compound N=1P(OC=2C=CC=CC=2)(OC=2C=CC=CC=2)=NP(OC=2C=CC=CC=2)(OC=2C=CC=CC=2)=NP=1(OC=1C=CC=CC=1)OC1=CC=CC=C1 RNFJDJUURJAICM-UHFFFAOYSA-N 0.000 description 9
- 238000012360 testing method Methods 0.000 description 9
- 230000009286 beneficial effect Effects 0.000 description 8
- 238000011084 recovery Methods 0.000 description 7
- 238000000354 decomposition reaction Methods 0.000 description 5
- 239000007789 gas Substances 0.000 description 5
- 239000003960 organic solvent Substances 0.000 description 5
- XKRFYHLGVUSROY-UHFFFAOYSA-N Argon Chemical compound [Ar] XKRFYHLGVUSROY-UHFFFAOYSA-N 0.000 description 4
- BVKZGUZCCUSVTD-UHFFFAOYSA-L Carbonate Chemical compound [O-]C([O-])=O BVKZGUZCCUSVTD-UHFFFAOYSA-L 0.000 description 4
- 230000007423 decrease Effects 0.000 description 4
- 230000000694 effects Effects 0.000 description 4
- 230000015572 biosynthetic process Effects 0.000 description 3
- 238000006243 chemical reaction Methods 0.000 description 3
- 230000002401 inhibitory effect Effects 0.000 description 3
- 238000004519 manufacturing process Methods 0.000 description 3
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- 239000013074 reference sample Substances 0.000 description 3
- 238000007086 side reaction Methods 0.000 description 3
- 239000000126 substance Substances 0.000 description 3
- OZJPLYNZGCXSJM-UHFFFAOYSA-N 5-valerolactone Chemical compound O=C1CCCCO1 OZJPLYNZGCXSJM-UHFFFAOYSA-N 0.000 description 2
- SECXISVLQFMRJM-UHFFFAOYSA-N N-Methylpyrrolidone Chemical compound CN1CCCC1=O SECXISVLQFMRJM-UHFFFAOYSA-N 0.000 description 2
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 description 2
- 239000002033 PVDF binder Substances 0.000 description 2
- 229910052782 aluminium Inorganic materials 0.000 description 2
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 2
- 238000004458 analytical method Methods 0.000 description 2
- 229910052786 argon Inorganic materials 0.000 description 2
- 230000015556 catabolic process Effects 0.000 description 2
- 238000011161 development Methods 0.000 description 2
- 238000007599 discharging Methods 0.000 description 2
- 239000007772 electrode material Substances 0.000 description 2
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- 238000004880 explosion Methods 0.000 description 2
- 230000020169 heat generation Effects 0.000 description 2
- 238000009830 intercalation Methods 0.000 description 2
- 239000005486 organic electrolyte Substances 0.000 description 2
- 229920002981 polyvinylidene fluoride Polymers 0.000 description 2
- 239000002994 raw material Substances 0.000 description 2
- 230000009467 reduction Effects 0.000 description 2
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- JOROOXPAFHWVRW-UHFFFAOYSA-N 1,1,1,2,3,3-hexafluoro-3-(2,2,3,3,3-pentafluoropropoxy)propane Chemical compound FC(F)(F)C(F)C(F)(F)OCC(F)(F)C(F)(F)F JOROOXPAFHWVRW-UHFFFAOYSA-N 0.000 description 1
- GEWWCWZGHNIUBW-UHFFFAOYSA-N 1-(4-nitrophenyl)propan-2-one Chemical compound CC(=O)CC1=CC=C([N+]([O-])=O)C=C1 GEWWCWZGHNIUBW-UHFFFAOYSA-N 0.000 description 1
- GAPYETXMWCTXDQ-UHFFFAOYSA-N 2-hydroxyethyl hydrogen sulfate Chemical compound OCCOS(O)(=O)=O GAPYETXMWCTXDQ-UHFFFAOYSA-N 0.000 description 1
- MVUQPZYUKUJXTK-UHFFFAOYSA-N 3-hydroxybutan-2-yl hydrogen sulfate Chemical compound CC(O)C(C)OS(O)(=O)=O MVUQPZYUKUJXTK-UHFFFAOYSA-N 0.000 description 1
- BJWMSGRKJIOCNR-UHFFFAOYSA-N 4-ethenyl-1,3-dioxolan-2-one Chemical compound C=CC1COC(=O)O1 BJWMSGRKJIOCNR-UHFFFAOYSA-N 0.000 description 1
- 240000001913 Atriplex hortensis Species 0.000 description 1
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 1
- 229910032387 LiCoO2 Inorganic materials 0.000 description 1
- 229910013131 LiN Inorganic materials 0.000 description 1
- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 description 1
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- ITAPPIWTGWUYNX-UHFFFAOYSA-N butane-1,2-diol;sulfuric acid Chemical compound OS(O)(=O)=O.CCC(O)CO ITAPPIWTGWUYNX-UHFFFAOYSA-N 0.000 description 1
- GTJRDLYFFWVVCZ-UHFFFAOYSA-N butane-1,3-diol;sulfuric acid Chemical compound OS(O)(=O)=O.CC(O)CCO GTJRDLYFFWVVCZ-UHFFFAOYSA-N 0.000 description 1
- 229930188620 butyrolactone Natural products 0.000 description 1
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- 238000006056 electrooxidation reaction Methods 0.000 description 1
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Classifications
-
- 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
Landscapes
- Secondary Cells (AREA)
Abstract
Description
技术领域 technical field
本发明涉及一种锂离子电池非水电解液及其制成的锂离子二次电池。The invention relates to a lithium-ion battery non-aqueous electrolyte and a lithium-ion secondary battery made thereof.
背景技术 Background technique
锂离子电池是新一代最具竞争力的电池,被称为“绿色环保能源”,是解决当代环境污染问题和能源问题的首选技术。近年来,在高能电池领域中锂离子电池已取得了巨大成功,但消费者仍然期望综合性能更高的电池面世,而这取决于对新的电极材料和电解质体系的研究和开发。锂离子电池电解液体系作为锂离子电池重要组成部分,是锂离子电池必需的关键材料,其性能优劣对锂离子电池的发展是极大地制约。目前锂离子电池的电解液是由易燃的有机溶剂和锂盐组成,当锂离子二次电池在过度充放电,短路和大电流长时间工作的情况下,放出大量的热,这些热量致使电池体系内部温度过高,成为易燃电解液的安全隐患,可能造成灾难性热击穿,甚至电池爆破[郑洪河.锂离子电池电解质[M].北京:化学工业出版社,2006,134.]。因此,安全性问题已经成为锂离子电池市场创新的重要前提,特别是在电动汽车(EV)和混合动力汽车(HEV)的动力锂离子电池领域的应用对电池的安全性提出了更高,更新的要求。Lithium-ion battery is the most competitive battery of the new generation, known as "green energy", and is the preferred technology to solve contemporary environmental pollution and energy problems. In recent years, lithium-ion batteries have achieved great success in the field of high-energy batteries, but consumers still expect batteries with higher comprehensive performance, which depends on the research and development of new electrode materials and electrolyte systems. Lithium-ion battery electrolyte system, as an important part of lithium-ion batteries, is a key material necessary for lithium-ion batteries, and its performance is a great constraint on the development of lithium-ion batteries. At present, the electrolyte of lithium-ion batteries is composed of flammable organic solvents and lithium salts. When lithium-ion secondary batteries are overcharged and discharged, short-circuited, and operated for a long time with a high current, a large amount of heat is released, which causes the battery The internal temperature of the system is too high, which becomes a safety hazard of the flammable electrolyte, which may cause catastrophic thermal breakdown, or even battery explosion [Zheng Honghe. Lithium-ion battery electrolyte [M]. Beijing: Chemical Industry Press, 2006, 134.]. Therefore, safety issues have become an important prerequisite for innovation in the lithium-ion battery market, especially in the field of power lithium-ion batteries for electric vehicles (EV) and hybrid electric vehicles (HEV). requirements.
目前业界开发阻燃型电解液主要有两条技术路线。一方面通过添加磷系阻燃剂,卤系阻燃剂,复合阻燃剂和其它新型阻燃剂到常规电解液中,可以使易燃的有机电解液变成难燃或不可燃的电解液,降低电池放热值和电池自热率,增加电解液自身的热稳定性,从而避免电池在过热条件下的燃烧或爆炸。为了不降低作为电解液的性能,并提高其阻燃性,日本大金株式会社在中国申请的专利CN101490893A,CN101584075A提出了添加含氟醚的方案。另一方面尝试采用高沸点,高闪点的有机溶剂取代低沸点,低闪点的线性碳酸酯类溶剂,以此提高电解液的安全性能和高温放置性能,取得了一定的进展。韩国三星SDI株式会社专利CN1577944公开了一种用于锂离子电池的电解液,其中包含高沸点、高闪点的γ-丁内酯,环状碳酸酯和具有吸电子基团的酯类化合物,此电解液体系具有良好的安全性和良好的储存特性。Kejha J B在专利US2006204857(A1)中公开了一种适用于锂离子电池的高性能和更安全的电解质体系,此体系采用以LiBF4为锂盐,以10~30%的高闪点、高沸点的γBL(或PC或BC)加70~90%的EC为有机溶剂,所得电解液难点燃,且电化学性能可以与采用了线性碳酸酯类溶剂的常规电解液相媲美。At present, there are two main technical routes for the development of flame-retardant electrolytes in the industry. On the one hand, by adding phosphorus-based flame retardants, halogen-based flame retardants, composite flame retardants and other new flame retardants to conventional electrolytes, flammable organic electrolytes can be turned into flammable or non-flammable electrolytes , reduce the heat release value of the battery and the self-heating rate of the battery, increase the thermal stability of the electrolyte itself, so as to avoid the combustion or explosion of the battery under overheating conditions. In order not to reduce the performance of the electrolyte and to improve its flame retardancy, the patents CN101490893A and CN101584075A applied by Daikin Corporation in China proposed to add fluorine-containing ethers. On the other hand, try to use high boiling point, high flash point organic solvents to replace low boiling point, low flash point linear carbonate solvents, so as to improve the safety performance and high temperature storage performance of the electrolyte, and some progress has been made. South Korea's Samsung SDI Co., Ltd. patent CN1577944 discloses an electrolyte for lithium-ion batteries, which contains gamma-butyrolactone with high boiling point and high flash point, cyclic carbonates and ester compounds with electron-withdrawing groups. The electrolyte system has good safety and good storage properties. Kejha J B disclosed a high-performance and safer electrolyte system suitable for lithium-ion batteries in the patent US2006204857 (A1). This system uses LiBF 4 as lithium salt, with a high flash point and high boiling point The γBL (or PC or BC) plus 70-90% EC is an organic solvent, and the obtained electrolyte is difficult to ignite, and its electrochemical performance can be comparable to that of a conventional electrolyte using a linear carbonate solvent.
近年来,盼随着电池的高能化,要求电池壳重量轻,厚度薄,从而使得电池更容易膨胀。在实际应用中,通常与使用条件相应,对电池的各种性能要求也发生变化,其一是电池的高温储存性能。提高电池的高温储存性能可以使用具有高沸点、低蒸气压的电解质溶剂,或者采用抑制非水电解质在正负极表面上分解的方法(CN1282272C)。在使用高沸点,低蒸气压的溶剂时,一般都存在溶剂的粘度升高,非水电解质的电导率降低和放电特性降低等问题,因此,为了使非水电解质的电导率不降低,特开平(2000-235868)提出了使用高介电常数而且高沸点的γ-丁内酯(GBL)等方案。但是使用GBL基电解液在电化学耐氧化性和耐还原性方面劣于使用混合碳酸亚乙酯和低粘度溶剂得到的电解液。GBL基电解液在碳负极成膜疏松多孔,粗糙,稳定性不好,在充电时容易在负极上引起还原分解反应,由于该分解生成物的作用使负极的表面电阻增大,同时引起隔膜的微孔堵塞,因此在反复进行充放电时存在电池容量显著降低的问题。同时在高温保存充电状态GBL基电解液更不稳定,容易与正负极发生副反应,致使内阻增长显著,同时对SEI膜破坏严重,造成保持容量和恢复容量下降,电池鼓胀厉害。因此GBL基电解液存在以石墨为负极的电池中使用时,容量衰减快的问题;在高温下的电池容量保持等方面的问题,需要进一步改进。另外,在电解液中的添加剂过剩的情况下,过剩的那部分添加剂在高温放置时会在正极上发生氧化分解反应并产生气体,因此会由于内压的上升而导致电池的显著膨胀,这些都是存在的问题。In recent years, with the increase in battery energy, the battery case is required to be light in weight and thin in thickness, so that the battery can expand more easily. In practical applications, various performance requirements for the battery usually change corresponding to the use conditions, one of which is the high-temperature storage performance of the battery. To improve the high-temperature storage performance of the battery, an electrolyte solvent with a high boiling point and a low vapor pressure can be used, or a method of inhibiting the decomposition of the non-aqueous electrolyte on the surface of the positive and negative electrodes can be used (CN1282272C). When using a solvent with a high boiling point and a low vapor pressure, there are generally problems such as an increase in the viscosity of the solvent, a decrease in the conductivity of the non-aqueous electrolyte, and a decrease in the discharge characteristics. (2000-235868) proposed to use γ-butyrolactone (GBL) with high dielectric constant and high boiling point, etc. However, the electrochemical oxidation resistance and reduction resistance of GBL-based electrolytes are inferior to those obtained by mixing ethylene carbonate and low-viscosity solvents. The GBL-based electrolyte film on the carbon negative electrode is loose, porous, rough, and has poor stability. It is easy to cause reduction and decomposition reactions on the negative electrode during charging. Due to the action of the decomposition products, the surface resistance of the negative electrode increases, and at the same time, it causes the diaphragm. Since the micropores are clogged, there is a problem that the battery capacity significantly decreases when charging and discharging are repeated. At the same time, the GBL-based electrolyte in the charging state is more unstable when stored at high temperature, and it is prone to side reactions with the positive and negative electrodes, resulting in a significant increase in internal resistance. At the same time, the SEI film is severely damaged, resulting in a decrease in the retention capacity and recovery capacity, and severe battery swelling. Therefore, the GBL-based electrolyte has the problem of rapid capacity decay when used in a battery with graphite as the negative electrode; the problem of battery capacity retention at high temperature needs to be further improved. In addition, in the case of excess additives in the electrolyte, the excess additives will oxidize and decompose on the positive electrode and generate gas when placed at high temperature, which will cause significant expansion of the battery due to the increase in internal pressure, all of which are is the problem.
发明内容 Contents of the invention
本发明人经过大量的实验尝试发现,通过添加环状的硫酸酯和线状氟醚,能够成功解决以γBL基电解液容量衰减以及高温储存性能劣化的问题。The inventors have found through a lot of experiments that the problems of capacity fading and high-temperature storage performance degradation of γBL-based electrolytes can be successfully solved by adding cyclic sulfuric acid esters and linear fluoroethers.
基于上述发现,本发明为了解决上述电解液存在的相关技术问题。提供一种锂离子电池非水电解液,该电解液可以使锂离子电池在具有高安全性的同时获得优良的电化学性能,包括卓越的高温储存性能和良好的循环性能。Based on the above findings, the present invention aims to solve the related technical problems existing in the above electrolyte. Provided is a non-aqueous electrolyte solution for a lithium ion battery, which enables the lithium ion battery to obtain excellent electrochemical performance while having high safety, including excellent high-temperature storage performance and good cycle performance.
该种锂离子电池非水电解液采用高闪点,高沸点的有机溶剂,再加卤系阻燃剂(线性氟醚)或者进一步添加氟碳表面活性剂的思路。依此想法而得到的一种有利于提高锂离子电池循环性能和改善高温储存性能的电解液,此电解液尤其适用于中低倍率下的容量型电池。This kind of non-aqueous electrolyte solution for lithium-ion batteries uses an organic solvent with a high flash point and a high boiling point, and then adds a halogenated flame retardant (linear fluoroether) or further adds a fluorocarbon surfactant. An electrolyte solution obtained based on this idea is beneficial to improving the cycle performance and high-temperature storage performance of lithium-ion batteries, and the electrolyte solution is especially suitable for capacity batteries at low and medium rates.
本发明提供一种锂离子电池用非水电解液,该电解液含有:The invention provides a non-aqueous electrolytic solution for a lithium ion battery, the electrolytic solution contains:
锂盐;Lithium salt;
环状羧酸酯、环状碳酸酯或环状羧酸酯与环状碳酸酯的混合物;Cyclic carboxylates, cyclic carbonates or mixtures of cyclic carboxylates and cyclic carbonates;
如结构式(I)所示的氟醚:Fluoroethers as shown in structural formula (I):
Rf1-O-Rf2 结构式(I)R f1 -OR f2 structural formula (I)
式中Rf1是碳原子数为3~4的含氟烷基,Rf2是碳原子数为2~5的含氟烷基;In the formula, R f1 is a fluorine-containing alkyl group with 3 to 4 carbon atoms, and R f2 is a fluorine-containing alkyl group with 2 to 5 carbon atoms;
如结构式(II)所示的环状硫酸酯:Cyclic sulfuric acid ester as shown in structural formula (II):
结构式(II)Structural formula (II)
式中n的值为0或1,R1,R2,R3和R4分别独立地表示氢原子或1~5个碳原子的烷基。In the formula, the value of n is 0 or 1, and R 1 , R 2 , R 3 and R 4 each independently represent a hydrogen atom or an alkyl group with 1 to 5 carbon atoms.
其中,所述环状羧酸酯优选自:γ-丁内酯、γ-戊内酯、δ-戊内酯、卤代γ-丁内酯、硝基γ-丁内酯、氰基γ-丁内酯、α-乙酰基-γ-丁内酯中的一种或多种。Among them, the cyclic carboxylic acid ester is preferably selected from: γ-butyrolactone, γ-valerolactone, δ-valerolactone, halogenated γ-butyrolactone, nitro γ-butyrolactone, cyano γ- One or more of butyrolactone and α-acetyl-γ-butyrolactone.
其中,所述环状碳酸酯优选自:碳酸乙烯酯、碳酸丙烯酯、碳酸丁烯酯或卤代碳酸乙烯酯中的一种或多种。Wherein, the cyclic carbonate is preferably selected from one or more of ethylene carbonate, propylene carbonate, butylene carbonate or halogenated ethylene carbonate.
其中,所述的氟醚在电解液中的质量百分比优选为10~50%。Wherein, the mass percentage of the fluoroether in the electrolyte is preferably 10-50%.
其中,所述环状硫酸酯在电解液中的质量百分比优选为0.01%~2%。Wherein, the mass percentage of the cyclic sulfuric acid ester in the electrolyte is preferably 0.01%-2%.
优选地,所述电解液还包含结构式如下式(III)的氟碳表面活性剂:Preferably, the electrolyte also includes a fluorocarbon surfactant of the following formula (III):
Rf3X(CH2CH2O)n R1或Rf3X(CHCH3CH2O)n R1 结构式(III)R f3 X(CH 2 CH 2 O) n R 1 or R f3 X(CHCH 3 CH 2 O) n R 1 structural formula (III)
其中,Rf3是碳原子数为2~18的含氟烷基,X是氧(-O-)、硫(-S-)、氧化胺(-+NO--)、酰胺(-CONH-)或磺酰胺(-SO2N-)官能团,R1是氢原子或者碳原子数为1~4的烷基,n=1~25。Among them, R f3 is a fluorine-containing alkyl group with 2 to 18 carbon atoms, X is oxygen (-O-), sulfur (-S-), amine oxide (- + NO - -), amide (-CONH-) Or a sulfonamide (-SO 2 N-) functional group, R 1 is a hydrogen atom or an alkyl group with 1-4 carbon atoms, n=1-25.
优选地,所述电解液还含有链状碳酸酯、链状羧酸酯或链状亚硫酸酯中的一种或几种。Preferably, the electrolyte also contains one or more of chain carbonates, chain carboxylates or chain sulfites.
其中所述链状碳酸酯优选自:碳酸二甲酯,碳酸甲乙酯,碳酸二乙酯,碳酸甲基丙基酯,碳酸乙基丙基酯,碳酸二丙酯中的一种或多种;Wherein said chain carbonate is preferably selected from: one or more in dimethyl carbonate, ethyl methyl carbonate, diethyl carbonate, methyl propyl carbonate, ethyl propyl carbonate, dipropyl carbonate ;
所述链状羧酸酯优选自:乙酸甲酯,乙酸乙酯,乙酸丙酯,丙酸甲酯,丙酸乙酯,丙酸丙酯,丁酸甲酯,丁酸乙酯中的一种或多种;The chain carboxylate is preferably selected from: methyl acetate, ethyl acetate, propyl acetate, methyl propionate, ethyl propionate, propyl propionate, methyl butyrate, a kind of in ethyl butyrate or more;
所述链状亚硫酸酯优选自:亚硫酸二甲酯,亚硫酸二乙酯、亚硫酸甲乙酯中的一种或多种。The chain sulfite is preferably selected from one or more of dimethyl sulfite, diethyl sulfite, and ethyl methyl sulfite.
其中,所述锂盐优选自:LiPF6、LiBF4、LiClO4、LiBOB、LiODFB、LiN(SO2CF3)2、LiN(SO2C2F5)2、LiN(SO2F)2中的一种或多种,所述锂盐在电解液中的浓度按锂离子计为0.6~2mol/L。Among them, the lithium salt is preferably selected from: LiPF 6 , LiBF 4 , LiClO 4 , LiBOB, LiODFB, LiN(SO 2 CF 3 ) 2 , LiN(SO 2 C 2 F 5 ) 2 , LiN(SO 2 F) 2 One or more of them, the concentration of the lithium salt in the electrolyte is 0.6-2 mol/L in terms of lithium ions.
优选地,所述电解液还含有添加剂,所述添加剂优选自:碳酸亚乙烯酯,亚硫酸乙烯酯,氟代碳酸乙烯酯,碳酸乙烯亚乙酯,1,3-丙烷磺内酯中的一种或多种,所述添加剂在电解液中的质量百分比为0.1~10%。Preferably, the electrolyte solution also contains additives, and the additives are preferably selected from one of: vinylene carbonate, vinyl sulfite, fluoroethylene carbonate, vinylethylene carbonate, 1,3-propane sultone One or more, the mass percentage of the additive in the electrolyte is 0.1-10%.
本发明还提供了以上述电解液为基础的锂离子二次电池,其包括正极、负极以及电解液。The present invention also provides a lithium ion secondary battery based on the above electrolytic solution, which includes a positive electrode, a negative electrode and an electrolytic solution.
优选地,所述正极具有含过渡金属氧化物的锂盐活性物质,该锂盐包括LiCoO2,LiMn2O4,LiNi1-x-yCoxMnyO2(0<x<1,0<y<1),LiNi1-xCoxO2(0<x<1),LiFePO4中的一种或几种;负极具有活性物质是石墨、含Si或Sn的合金材料或者钛酸锂。Preferably, the positive electrode has a lithium salt active material containing a transition metal oxide, and the lithium salt includes LiCoO 2 , LiMn 2 O 4 , LiNi 1-xy Co x Mn y O 2 (0<x<1, 0<y <1), one or more of LiNi 1-x Co x O 2 (0<x<1), LiFePO 4 ; the active material of the negative electrode is graphite, an alloy material containing Si or Sn, or lithium titanate.
该技术方案与现有技术相比具有如下有益效果:Compared with the prior art, this technical solution has the following beneficial effects:
1.环状羧酸酯、环状碳酸酯或环状羧酸酯与环状碳酸酯的混合物与氟醚组成的高沸点、低蒸气压溶剂加抑制高温产气的成膜添加剂,高温储存性能卓越。因此本发明的高闪点,低蒸气压溶剂组成的电解液高温储存时产气少,有利于改善高温储存性能。为配合该溶剂,本发明通过添加少量添加剂环状硫酸酯,在电极上形成稳定的SEI膜,使非水电解质的分解在动力学上得以抑制而更有利于提高高温储存性能。1. Cyclic carboxylate, cyclic carbonate or a mixture of cyclic carboxylate and cyclic carbonate and fluoroether with high boiling point, low vapor pressure solvent plus film-forming additives to suppress high-temperature gas production, high-temperature storage performance excellence. Therefore, the electrolyte solution composed of high flash point and low vapor pressure solvent of the present invention produces less gas during high-temperature storage, which is beneficial to improve high-temperature storage performance. In order to cooperate with the solvent, the present invention forms a stable SEI film on the electrode by adding a small amount of additive cyclic sulfate, so that the decomposition of the non-aqueous electrolyte is kinetically inhibited and is more conducive to improving the high-temperature storage performance.
2.通过添加环状硫酸酯和线状氟醚联用,能够成功解决在以石墨为负极的电池中γBL基电解液成膜不稳定,PC基电解液共插入的副反应而致使电池容量衰减问题。氟醚用作溶剂可以降低电解液与电极的反应性,抑制了电极界面的产热;环状硫酸酯成膜性能好,实验发现两者联用能抑制γBL,PC等高闪点,高沸点溶剂在石墨负极的副反应,大大提高高温储存性能,成为进一步提高电池的安全性和电池性能的有效保障。2. By adding cyclic sulfuric acid ester and linear fluoroether in combination, it can successfully solve the unstable film formation of γBL-based electrolyte and co-intercalation of PC-based electrolyte in batteries with graphite as the negative electrode, resulting in battery capacity attenuation question. The use of fluoroether as a solvent can reduce the reactivity between the electrolyte and the electrode, and inhibit the heat generation at the electrode interface; the cyclic sulfuric acid ester has good film-forming properties. Experiments have found that the combination of the two can inhibit high flash points and high boiling points such as γBL and PC. The side reaction of the solvent in the graphite negative electrode greatly improves the high-temperature storage performance, and becomes an effective guarantee for further improving the safety and performance of the battery.
3.高闪点,高沸点溶剂组成的电解液其闪点和沸点也高;不容易点燃,另加氟醚阻燃剂,氟醚本身含有阻燃元素氟元素,其闪点高,难燃,加到电解液中,使易燃的有机电解液变成难燃或不可燃的电解液,对阻燃有效果;即使在非常恶劣的环境下,电解液达到了其闪燃点而被点燃,还存有氟醚的阻燃自熄作用,相比于常规电解液多了两重安全保障,更有效地提高了电池的安全性能。3. The electrolyte composed of high flash point and high boiling point solvent has high flash point and boiling point; it is not easy to ignite, and fluoroether flame retardant is added. Fluoroether itself contains the flame retardant element fluorine, which has a high flash point and is difficult to burn. , added to the electrolyte to make the flammable organic electrolyte into a flammable or non-flammable electrolyte, which is effective for flame retardancy; even in a very harsh environment, the electrolyte reaches its flash point and is ignited, There is also the flame-retardant and self-extinguishing effect of fluoroether, which has two more safety guarantees than conventional electrolytes, and more effectively improves the safety performance of the battery.
4.为了进一步优化电池性能,利用氟碳表面活性剂对氟醚和其它组分溶剂的分散性能,有利于改善氟醚与高沸点,高闪点溶剂的相溶性。氟碳表面活性剂对提高溶剂的润湿性能高度有效,尤其对于高沸点,高闪点溶剂组成的高粘度溶剂体系,表面活性剂的加入能改善非水电解液与电极之间的润湿性和在该界面的离子扩散性;在确保电解液难燃或不燃的前提下,同时具有优良的电池特性。4. In order to further optimize battery performance, the dispersibility of fluorocarbon surfactants to fluoroethers and other component solvents is beneficial to improve the compatibility of fluoroethers with high boiling point and high flash point solvents. Fluorocarbon surfactants are highly effective in improving the wetting properties of solvents, especially for high-viscosity solvent systems composed of high boiling point and high flash point solvents. The addition of surfactants can improve the wettability between non-aqueous electrolytes and electrodes And ion diffusivity at the interface; under the premise of ensuring that the electrolyte is flammable or non-flammable, it also has excellent battery characteristics.
因此,通过以高闪点,高沸点环状的溶剂取代低闪点的线性碳酸酯或羧酸酯;再加环状硫酸酯和卤系阻燃剂氟醚的技术方案,而得到阻燃性和电池特性(高温储存性能、循环性能)兼优的锂二次电池用电解液。Therefore, by replacing the low-flash point linear carbonate or carboxylate with a high-flash point, high-boiling point cyclic solvent; adding a technical solution of cyclic sulfuric acid ester and halogenated flame retardant fluoroether, the flame retardancy can be obtained An electrolyte solution for lithium secondary batteries that is excellent in battery characteristics (high temperature storage performance, cycle performance).
具体实施方式 Detailed ways
为详细说明本发明的技术内容、构造特征、所实现目的及效果,以下结合实施方式详予说明。In order to describe in detail the technical content, structural features, achieved objectives and effects of the present invention, the following will be described in detail in conjunction with the embodiments.
一.实施例电解液的制备方法One. The preparation method of embodiment electrolyte
在充氩气的手套箱中(H2O<10ppm),将环状碳酸酯、环状羧酸酯、线状氟醚、锂盐、环状硫酸酯、成膜添加剂和氟碳表面活性剂按表1各实施例和对比例列出的电解液质量比进行配制。将上述各原料依次加入,充分搅拌均匀,即得到本发明的锂离子电池电解液,用于可燃性能测试和电池性能测试。In an argon-filled glove box (H 2 O<10ppm), the cyclic carbonate, cyclic carboxylate, linear fluoroether, lithium salt, cyclic sulfate, film-forming additive and fluorocarbon surfactant Prepare according to the electrolyte mass ratio listed in each embodiment and comparative example in Table 1. The above-mentioned raw materials are added in sequence and fully stirred evenly to obtain the lithium-ion battery electrolyte of the present invention, which is used for flammability test and battery performance test.
二.实施例锂离子电池的制作方法Two. The manufacture method of embodiment lithium-ion battery
本发明的非水电解液二次电池由上述非水电解液,负极和正极构成。The non-aqueous electrolyte secondary battery of the present invention is composed of the above-mentioned non-aqueous electrolyte, a negative electrode and a positive electrode.
构成正极的活性物质可以是LiCoO2,LiMn2O4,LiNi1-x-yCoxMnyO2(0<x<1,0<y<1),LiNi1-xCoxO2(0<x<1),LiFePO4等。The active material constituting the positive electrode can be LiCoO 2 , LiMn 2 O 4 , LiNi 1-xy Co x Mn y O 2 (0<x<1, 0<y<1), LiNi 1-x Co x O 2 (0<x<1), LiFePO 4 and so on.
构成负极的活性物质可以是石墨、含Si或Sn的合金材料或者钛酸锂等。The active material constituting the negative electrode may be graphite, an alloy material containing Si or Sn, or lithium titanate.
将LiCoO2,导电剂乙炔黑和聚偏氟乙烯按8∶1∶1的重量比混合,随后加入1-甲基-2-吡咯烷酮形成浆料,然后将其涂覆于铝箔上,之后干燥并模压形成阴极。LiCoO 2 , conductive agent acetylene black and polyvinylidene fluoride were mixed in a weight ratio of 8:1:1, then 1-methyl-2-pyrrolidone was added to form a slurry, which was then coated on an aluminum foil, then dried and Molded to form the cathode.
将天然石墨,聚偏氟乙烯按9∶1的重量比混合,随后加入1-甲基-2-吡咯烷酮形成浆料,然后将其涂布于铜箔上,之后干燥,模压并且热处理形成阳极。使用聚丙烯多孔膜为隔膜,后将阳极片,阴极片和隔膜卷绕形成卷绕体,或叠片成极组,将上述组件与上述制备的电解质一起被封装在金属外壳内而制成方形锂离子电池。Mix natural graphite and polyvinylidene fluoride at a weight ratio of 9:1, then add 1-methyl-2-pyrrolidone to form a slurry, which is then coated on a copper foil, dried, pressed and heat-treated to form an anode. Use polypropylene porous membrane as the separator, then wind the anode sheet, cathode sheet and separator to form a winding body, or stack the sheets into an electrode group, and package the above components together with the electrolyte prepared above in a metal casing to make a square shape Lithium Ion Battery.
三.实施例锂离子电池的化成与测试方法:Three. Formation and test method of embodiment lithium-ion battery:
本发明采用的化成工步:一次化成条件:0.05C,3min;0.2C,5min;0.5C,25min。然后补注液并整形封口,二次化成以0.2C恒流充到4.2V,再室温老化24h,然后以0.2C恒流恒压(4.2V)补充,再以0.2C恒流放电到3.0V。The chemical conversion steps adopted in the present invention: primary chemical conversion conditions: 0.05C, 3min; 0.2C, 5min; 0.5C, 25min. Then replenish the liquid and seal it, charge it to 4.2V with a constant current of 0.2C, and age at room temperature for 24 hours, then supplement it with a constant current and voltage (4.2V) at 0.2C, and discharge it to 3.0V with a constant current of 0.2C .
本发明对锂离子电池电解液充放电性能评价:将所配制的锂离子电池电解液注入到1000mAh的铝壳方型LiCoO2电池中,电压区间在3.0~4.2V,在1C条件下进行充放电循环测试。The present invention evaluates the charging and discharging performance of the lithium-ion battery electrolyte: inject the prepared lithium-ion battery electrolyte into a 1000mAh aluminum shell square LiCoO2 battery, charge and discharge at 1C with a voltage range of 3.0-4.2V Cycle test.
本发明对锂离子电池电解液高温储存性能测试方法:The present invention tests the high-temperature storage performance of lithium-ion battery electrolyte:
首先将电池在常温(25℃±2℃)状态下以1C充放电一次,记录常温下放电容量为C1,再以1C恒流恒压将电池充满电,测试满电状态下电池的厚度D1,将满电状态的电池进行高温保存测试。待电池完全冷却后再次测试电池的厚度D2;将取出的电池按下列方式进行充放电:First charge and discharge the battery once at 1C at room temperature (25°C±2°C), record the discharge capacity at room temperature as C 1 , then fully charge the battery at 1C constant current and constant voltage, and test the thickness of the battery at full charge D 1. Carry out a high-temperature storage test on a fully charged battery. After the battery is completely cooled, test the thickness D 2 of the battery again; charge and discharge the removed battery as follows:
a、1C恒流放电至终止电压2.75V,放电容量记为C2。a. 1C constant current discharge to the end voltage of 2.75V, and the discharge capacity is recorded as C 2 .
b、搁置5min。b. Leave it on hold for 5 minutes.
c、1C恒流恒压充电至4.2V,截止电流0.02C。c, 1C constant current and constant voltage charge to 4.2V, cut-off current 0.02C.
d、搁置5min。d. Leave it on hold for 5 minutes.
e、1C恒流放电至终止电压2.75V,放电容量记为C3。e. Discharge at a constant current of 1C to a termination voltage of 2.75V, and record the discharge capacity as C 3 .
高温保存后容量保持率=C2/C1×100%,容量恢复率=C3/C1×100%,Capacity retention rate after high temperature storage = C 2 /C 1 ×100%, capacity recovery rate = C 3 /C 1 ×100%,
厚度膨胀率=(D2-D1)/D1×100%。Thickness expansion ratio = (D 2 -D 1 )/D 1 ×100%.
本发明对锂电池电解液的阻燃性能的测试方法:用长50mm,宽5mm,厚1.65mm的泡膜镍浸于本发明提及的实施例或对比例的电解液中,然后用镊子取出,靠近点火器火焰,停留2s,再移开火焰观察现象并记录自熄时间。The present invention is to the test method of the flame retardant property of lithium battery electrolyte: with long 50mm, wide 5mm, thick 1.65mm bubble film nickel is immersed in the embodiment that the present invention mentions or the electrolyte of comparative example, then take out with tweezers , close to the flame of the igniter, stay for 2s, then remove the flame to observe the phenomenon and record the self-extinguishing time.
四.实施例中有机物代号说明Four. In the embodiment, the code name of the organic matter is explained
1.各实施例中的氟醚:1. Fluoroethers in each embodiment:
S1为HCF2CF2CH2OCF2CF2HS 1 is HCF 2 CF 2 CH 2 OCF 2 CF 2 H
S2为HCF2CF2CH2OCF2CFHCF3 S 2 is HCF 2 CF 2 CH 2 OCF 2 CFHCF 3
S3为CF3CF2CH2OCF2CFHCF3 S 3 is CF 3 CF 2 CH 2 OCF 2 CFHCF 3
S4为CF3CF2CH2OCF2CF2CF2CF2HS 4 is CF 3 CF 2 CH 2 OCF 2 CF 2 CF 2 CF 2 H
S5为HCF2CF2CF2CH2OCH2CF2CF2CF2CF2HS 5 is HCF 2 CF 2 CF 2 CH 2 OCH 2 CF 2 CF 2 CF 2 CF 2 H
S6为HCF2CF2CF2CH2OCF2CF2HS 6 is HCF 2 CF 2 CF 2 CH 2 OCF 2 CF 2 H
S7为(CH2F)2CHOC(CF3)3 S 7 is (CH 2 F) 2 CHOC(CF 3 ) 3
2.各实施例中的环状硫酸酯:2. the cyclic sulfuric acid ester in each embodiment:
A1为乙二醇硫酸酯A 1 is ethylene glycol sulfate
A2为1,2-丙二醇硫酸酯A 2 is 1,2-propanediol sulfate
A3为1,2-丁二醇硫酸酯A 3 is 1,2-butanediol sulfate
A4为1,3-丁二醇硫酸酯A 4 is 1,3-butanediol sulfate
A5为2,3-丁二醇硫酸酯A 5 is 2,3-butanediol sulfate
A6为1,2-庚二醇硫酸酯A 6 is 1,2-heptanediol sulfate
A7为 A 7 is
3.各实施例中的氟碳表面活性剂:3. the fluorocarbon surfactant in each embodiment:
a1为CF3(CF2)4CH2O(CH2CH2O)3H,a 1 is CF 3 (CF 2 ) 4 CH 2 O(CH 2 CH 2 O) 3 H,
a2为C6F13CH2CH2S(CH2CH2O)3H,a 2 is C 6 F 13 CH 2 CH 2 S(CH 2 CH 2 O) 3 H,
a3为C8F17CH2CH2SO2N(CH3)CH2CH2OH,a 3 is C 8 F 17 CH 2 CH 2 SO 2 N(CH 3 )CH 2 CH 2 OH,
a4为CF3CHFCF2CH2O[CH(CH3)CH2O]2Ha 4 is CF 3 CHFCF 2 CH 2 O[CH(CH 3 )CH 2 O] 2 H
a5为CF3CH2NO(CH2CHO)25CH3 a 5 is CF 3 CH 2 NO(CH 2 CHO) 25 CH 3
a6为CH2F(CH2)16CH2CONH(CH(CH3)CH2O)10(CH2)3CH3 a 6 is CH 2 F(CH 2 ) 16 CH 2 CONH(CH(CH 3 )CH 2 O) 10 (CH 2 ) 3 CH 3
4.其它有机组分代号说明4. Description of other organic component codes
实施例1:Example 1:
在充氩气的手套箱中(H2O<10ppm),将有机溶剂按质量比为EC∶GBL∶S1=1∶1∶1与六氟磷酸锂(1.2M)混合,添加剂为环状硫酸酯A1,占电解液总重量的1%。将上述各原料依次加入,充分搅拌均匀,即得到本发明的锂离子电池电解液(游离酸<30ppm,水分<10ppm)。电解液用于可燃性能测试和电池性能测试。可燃性能测试结果和常温循环第100周容量保持率;60℃储存30天后其容量保持率、容量恢复率和厚度膨胀率示于表1。In an argon-filled glove box (H 2 O<10ppm), the organic solvent is mixed with lithium hexafluorophosphate (1.2M) at a mass ratio of EC:GBL:S 1 =1:1:1, and the additive is cyclic sulfate A 1 , accounting for 1% of the total weight of the electrolyte. The above-mentioned raw materials are added in sequence, fully stirred evenly, and the lithium-ion battery electrolyte solution (free acid<30ppm, moisture<10ppm) of the present invention is obtained. Electrolyte is used for flammability test and battery performance test. The test results of flammability and the capacity retention rate at the 100th cycle of normal temperature cycle; the capacity retention rate, capacity recovery rate and thickness expansion rate after storage at 60°C for 30 days are shown in Table 1.
实施例2:Example 2:
与实施例1的工艺相同,不同之处在于氟醚为S2,环状硫酸酯为A2。The process is the same as in Example 1, except that the fluoroether is S 2 , and the cyclic sulfate is A 2 .
实施例3:Example 3:
与实施例1的工艺相同,不同之处在于电解液配比为:EC∶GBL∶S4=1∶1∶1,1.0M LiPF6和0.2M LiBF4,A3:1%。The process is the same as in Example 1, except that the electrolyte solution ratio is: EC:GBL:S 4 =1:1:1, 1.0M LiPF 6 and 0.2M LiBF 4 , A 3 : 1%.
实施例4:Example 4:
与实施例3的工艺相同,不同之处在于氟醚为S5,环状硫酸酯为A4。The same process as in Example 3, except that the fluoroether is S 5 , and the cyclic sulfate is A 4 .
实施例5:Example 5:
与实施例3的工艺相同,不同之处在于氟醚为S6,环状硫酸酯为A5。The same process as in Example 3, except that the fluoroether is S 6 , and the cyclic sulfate is A 5 .
实施例6:Embodiment 6:
与实施例1的工艺相同,不同之处在于电解液配比为:EC∶PC∶GBL∶S3=30∶30∶10∶30,1.0M LiPF6和0.2M LiBF4,A1:1%。The same process as in Example 1, except that the electrolyte ratio is: EC:PC:GBL:S 3 =30:30:10:30, 1.0M LiPF 6 and 0.2M LiBF 4 , A 1 : 1% .
实施例7:Embodiment 7:
与实施例1的工艺相同,不同之处在实施例1电解液配比的基础上添加了2%的VC。The process is the same as in Example 1, except that 2% VC is added on the basis of the electrolyte ratio in Example 1.
实施例8:Embodiment 8:
与实施例1的工艺相同,不同之处在于电解液配比为:EC∶GBL∶MB∶S6=30∶40∶10∶20,0.8M LiBF4和0.2M LiN(SO2CF3)2,VC:1%,A5:2%。The process is the same as in Example 1, except that the electrolyte ratio is: EC:GBL:MB:S 6 =30:40:10:20, 0.8M LiBF 4 and 0.2M LiN(SO 2 CF 3 ) 2 , VC: 1%, A 5 : 2%.
实施例9:Embodiment 9:
与实施例1的工艺相同,不同之处在于电解液配比为:PC∶S2=60∶40,1.2M LiPF6和0.2M LiBOB,VC:1%,A2:0.8%。The process is the same as in Example 1, except that the electrolyte ratio is: PC:S 2 =60:40, 1.2M LiPF 6 and 0.2M LiBOB, VC: 1%, A 2 : 0.8%.
实施例10:Example 10:
与实施例1的工艺相同,不同之处在于电解液配比为:GBL∶S1=50∶50,1.4M LiBF4,VC:1%,A4:0.8%。The process is the same as that of Example 1, except that the electrolyte ratio is: GBL:S 1 =50:50, 1.4M LiBF 4 , VC: 1%, A 4 : 0.8%.
实施例11:Example 11:
与实施例1的工艺相同,不同之处在于电解液配比为:PC∶S2=60∶40,1.2M LiPF6和0.2M LiBOB,VC:1%,ES:2%,A2:0.8%。The same process as in Example 1, except that the electrolyte ratio is: PC:S 2 =60:40, 1.2M LiPF 6 and 0.2M LiBOB, VC: 1%, ES: 2%, A 2 : 0.8 %.
实施例12:Example 12:
与实施例1的工艺相同,不同之处在于电解液配比为:GBL∶S1=50∶50,1.4M LiBF4,VC:1%,1,3-PS:2%,A4:0.8%。The process is the same as in Example 1, except that the electrolyte ratio is: GBL:S 1 =50:50, 1.4M LiBF 4 , VC: 1%, 1,3-PS: 2%, A 4 : 0.8 %.
实施例13:Example 13:
与实施例1的工艺相同,不同之处在于电解液配比为:EC∶PC∶EMC∶S1=30∶20∶10∶40,1.2M LiPF6,A5:0.6%。The process is the same as that of Example 1, except that the electrolyte ratio is: EC:PC:EMC:S 1 =30:20:10:40, 1.2M LiPF 6 , A 5 : 0.6%.
实施例14:Example 14:
与实施例1的工艺相同,不同之处在于电解液配比为:EC∶PC∶EMC∶S1=30∶20∶10∶40,1.2M LiPF6,VC:1%,A5:0.6%。The same process as in Example 1, except that the electrolyte ratio is: EC:PC:EMC:S 1 =30:20:10:40, 1.2M LiPF 6 , VC: 1%, A 5 : 0.6% .
实施例15:Example 15:
与实施例1的工艺相同,不同之处在于电解液配比为:EC∶PC∶EMC∶S1=30∶20∶10∶40,1.2M LiPF6,VC:1%,A5:0.6%,a1:0.1%。The same process as in Example 1, except that the electrolyte ratio is: EC:PC:EMC:S 1 =30:20:10:40, 1.2M LiPF 6 , VC: 1%, A 5 : 0.6% , a 1 : 0.1%.
实施例16:Example 16:
与实施例1的工艺相同,不同之处在于电解液配比为:EC∶PC∶DMS∶S3=20∶20∶20∶40,1.2M LiPF6,VC:1%,A1:1%。The same process as in Example 1, except that the electrolyte ratio is: EC:PC:DMS:S 3 =20:20:20:40, 1.2M LiPF 6 , VC: 1%, A 1 : 1% .
实施例17:Example 17:
与实施例1的工艺相同,不同之处在于电解液配比为:EC∶PC∶DMS∶S3=20∶20∶20∶40,1.2M LiPF6,VC:1%,A1:1%,a2:0.1%。The same process as in Example 1, except that the electrolyte ratio is: EC:PC:DMS:S 3 =20:20:20:40, 1.2M LiPF 6 , VC: 1%, A 1 : 1% , a 2 : 0.1%.
实施例18:Example 18:
与实施例1的工艺相同,不同之处在于电解液配比为:EC∶PC∶EB∶S2=30∶20∶20∶30,1.2M LiPF6,VC:1%,A2:1.5%。The process is the same as in Example 1, except that the electrolyte ratio is: EC:PC:EB:S 2 =30:20:20:30, 1.2M LiPF 6 , VC: 1%, A 2 : 1.5% .
实施例19:Example 19:
与实施例1的工艺相同,不同之处在于电解液配比为:EC∶PC∶EB∶S2=30∶20∶20∶30,1.2M LiPF6,VC:1%,A2:1.5%,,a3:0.1%。The process is the same as in Example 1, except that the electrolyte ratio is: EC:PC:EB:S 2 =30:20:20:30, 1.2M LiPF 6 , VC: 1%, A 2 : 1.5% ,, a 3 : 0.1%.
实施例20:Example 20:
与实施例1的工艺相同,不同之处在于电解液配比为:EC∶PC∶EMC∶S5=40∶5∶15∶40,1.4M LiPF6,VC:1%,A2:1.5%,,a4:0.1%。The same process as in Example 1, except that the electrolyte ratio is: EC:PC:EMC:S 5 =40:5:15:40, 1.4M LiPF 6 , VC: 1%, A 2 : 1.5% ,, a 4 : 0.1%.
实施例21:Example 21:
与实施例1的工艺相同,不同之处在于电解液配比为:BC∶DEC∶MPC∶DES∶S7=20∶10∶10∶10∶50;LiClO4:0.6M;A6:0.01%;FEC:0.1%;a5:0.2%。The same process as in Example 1, except that the electrolyte ratio is: BC:DEC:MPC:DES:S 7 =20:10:10:10:50; LiClO 4 : 0.6M; A 6 : 0.01% ; FEC: 0.1%; a 5 : 0.2%.
实施例22:Example 22:
与实施例1的工艺相同,不同之处在于电解液配比为:FEC∶DVL∶BA∶MES∶S1=25∶10∶20∶15∶30;LiN(SO2F)2:2.0M;A7:2%;VEC:10%;a6:0.02%。The process is the same as in Example 1, except that the electrolyte ratio is: FEC:DVL:BA:MES:S 1 =25:10:20:15:30; LiN(SO 2 F) 2 : 2.0M; A 7 : 2%; VEC: 10%; a 6 : 0.02%.
对比例1(基准样):Comparative example 1 (reference sample):
与实施例1的工艺相同,不同之处在于电解液配比为:EC∶PC∶DMC=40∶5∶55,1.2M LiPF6,VC:2%。The process is the same as in Example 1, except that the electrolyte solution ratio is: EC:PC:DMC=40:5:55, 1.2M LiPF 6 , VC: 2%.
对比例2:Comparative example 2:
与实施例1的工艺相同,不同之处在于电解液配比为:EC∶PC∶EMC∶S5=40∶5∶15∶40,1.4M LiPF6,VC:1%,a4:0.1%。The same process as in Example 1, except that the electrolyte ratio is: EC:PC:EMC:S 5 =40:5:15:40, 1.4M LiPF 6 , VC: 1%, a 4 : 0.1% .
对比例3:Comparative example 3:
与实施例1的工艺相同,不同之处在于电解液配比为:EC∶PC∶EMC∶S1=30∶20∶10∶40,1.2M LiPF6,VC:1%。The process is the same as in Example 1, except that the electrolyte solution ratio is: EC:PC:EMC:S 1 =30:20:10:40, 1.2M LiPF 6 , VC: 1%.
对比例4:Comparative example 4:
与实施例1的工艺相同,不同之处在于电解液配比为:EC∶GBL∶DMC=1∶1∶1,1.2M LiPF6,VC:1%,A1:1%。The process is the same as in Example 1, except that the electrolyte solution ratio is: EC:GBL:DMC=1:1:1, 1.2M LiPF 6 , VC: 1%, A 1 : 1%.
对比例5:Comparative example 5:
与实施例1的工艺相同,不同之处在于电解液配比为:PC∶DMC=60∶40,1.2M LiPF6和0.2M LiBOB,A2:0.8%。The process is the same as that of Example 1, except that the electrolyte ratio is: PC:DMC=60:40, 1.2M LiPF 6 and 0.2M LiBOB, A 2 : 0.8%.
对比例6:Comparative example 6:
与实施例1的工艺相同,不同之处在于电解液配比为:GBL∶S1=50∶50,1.4M LiBF4,VC:1%,1,3-PS:2%。The process is the same as that of Example 1, except that the electrolyte ratio is: GBL:S 1 =50:50, 1.4M LiBF 4 , VC: 1%, 1,3-PS: 2%.
五.有益效果分析:Five. Beneficial effect analysis:
从各实施例和对比例中电解液可燃性能测试结果表1分析得知:对比例1、对比例4和对比例5由于含有大量的低闪点DMC,电解液可燃,而其它各实施例和对比例因为含有氟醚,均表现出一定程度的阻燃自熄作用。其中实施例1~7、实施例9~12中不含低闪点的线性碳酸酯或羧酸酯或亚硫酸酯,电解液短时间内难以点燃,说明其阻燃效果更好。From the analysis of electrolyte flammability performance test result table 1 in each embodiment and comparative example, it is known that: comparative example 1, comparative example 4 and comparative example 5 are due to containing a large amount of low-flash point DMC, and electrolyte is flammable, and other each embodiment and Because the comparative examples contain fluoroether, they all show a certain degree of flame retardant and self-extinguishing effect. Among them, Examples 1-7 and Examples 9-12 do not contain low-flash point linear carbonate or carboxylate or sulfite, and the electrolyte is difficult to ignite in a short time, which shows that the flame retardant effect is better.
从表1各实施例和对比例高温储存性能参数可知:各实施例的容量保持率,容量恢复率均高于基准样(对比例1),厚度膨胀率明显低于基准样(对比例1)。比较以氟醚取代对比例4中DMC的实施例1,对比例4的容量保持率和恢复率低于实施例1,同时实施例1的厚度膨胀率明显低于对比例4,说明氟醚的存在,能抑制电极与电解液界面间的产热,对高温储存有利。进一步比较具有相同溶剂配比的对比例2和实施例20、对比例3和实施例14,其中实施例20(或实施例14)电解液中加有环状硫酸酯A2(或A5),其容量保持率和容量恢复率均高于对比例2(或对比例3),厚度膨胀率低于对比例2(或对比例3),说明环状硫酸酯的加入有利于改善电池的高温储存性能,能抑制电池在高温储存时产气。通过使用环状硫酸酯化合物可提高高温放置性能,尽管其原因还不明确,不过可推测是由于具有硫酸酯在电极材料的表面上形成良好的SEI膜,从而抑制了溶剂在正极表面上的氧化和负极表面上的还原分解,而导致气体的产生。From the high temperature storage performance parameters of each embodiment and comparative example in Table 1, it can be seen that the capacity retention rate and capacity recovery rate of each embodiment are higher than that of the reference sample (comparative example 1), and the thickness expansion rate is obviously lower than that of the reference sample (comparative example 1). . Comparing Example 1 which replaces DMC in Comparative Example 4 with fluoroether, the capacity retention and recovery rate of Comparative Example 4 are lower than that of Example 1, while the thickness expansion rate of Example 1 is significantly lower than that of Comparative Example 4, indicating that the fluoroether Existence can suppress the heat generation between the electrode and the electrolyte interface, which is beneficial to high-temperature storage. Further compare comparative example 2 and embodiment 20, comparative example 3 and embodiment 14 with the same solvent ratio, wherein embodiment 20 (or embodiment 14) is added with cyclic sulfuric acid ester A 2 (or A 5 ) in the electrolyte , its capacity retention rate and capacity recovery rate are higher than that of Comparative Example 2 (or Comparative Example 3), and the thickness expansion rate is lower than that of Comparative Example 2 (or Comparative Example 3), indicating that the addition of cyclic sulfate is beneficial to improve the high temperature of the battery Storage performance, can inhibit the gas production of the battery when stored at high temperature. The high-temperature storage performance can be improved by using a cyclic sulfate ester compound. Although the reason for this is not clear, it is presumed that it is due to the formation of a good SEI film on the surface of the electrode material with the sulfate ester compound, thereby inhibiting the oxidation of the solvent on the surface of the positive electrode. and reductive decomposition on the surface of the negative electrode, resulting in the generation of gas.
由表可知,实施例7,实施例14,实施例15,实施例17和实施例19常温循环第100周的容量保持率高于或与常规电解液(对比例1)相当。比较实施例1和对比例4;实施例9和对比例5可知,含氟醚的实施例1和实施例9容量保持率远高于不含氟醚的对比例4和对比例5。可见氟醚的存在,对PC基的共插入和GBL基电解液成膜稳定性差致使的副反应有一定的抑制作用,有利于改善电池循环性能,故100周后其容量保持率在80%以上。进一步比较具有相同溶剂配比的对比例2和实施例20、对比例3和实施例14、对比例6和实施例12,其中实施例20、实施例14和实施例12的电解液中加有环状硫酸酯A2、A5和A4,其常温循环第100周容量保持率高于对比例2、对比例3和对比例6,说明环状硫酸酯的加入除可以改善高温储存性能,还有利于改善电池的常温循环性能。It can be seen from the table that the capacity retention rate of Example 7, Example 14, Example 15, Example 17 and Example 19 at room temperature cycle 100 is higher than or equivalent to that of the conventional electrolyte (Comparative Example 1). Comparing Example 1 and Comparative Example 4; Example 9 and Comparative Example 5, it can be seen that the capacity retention rate of Example 1 and Example 9 containing fluoroether is much higher than that of Comparative Example 4 and Comparative Example 5 not containing fluoroether. It can be seen that the presence of fluoroether has a certain inhibitory effect on the side reactions caused by the co-intercalation of the PC group and the poor film stability of the GBL-based electrolyte, which is conducive to improving the battery cycle performance, so its capacity retention rate is above 80% after 100 weeks . Further compare comparative example 2 and embodiment 20, comparative example 3 and embodiment 14, comparative example 6 and embodiment 12 with the same solvent proportioning, wherein in the electrolyte of embodiment 20, embodiment 14 and embodiment 12, add Cyclic sulfates A 2 , A 5 , and A 4 have higher capacity retention rates in the 100th cycle at room temperature than those of Comparative Example 2, Comparative Example 3, and Comparative Example 6, indicating that the addition of cyclic sulfates can improve high-temperature storage performance. It is also beneficial to improve the normal temperature cycle performance of the battery.
从表1可知,含表面活性剂的实施例15、实施例17、实施例19、实施例20,其容量保持率高于具有相同溶剂组成的实施例14、实施例16,实施例18,说明少量氟碳表面活性剂的加入能改善电池的循环性能;在实施例1的基础上添加2%VC的实施例7,实施例13的基础上添加VC的实施例14循环性能得到改善,在实施例9和实施例10的基础上添加ES的实施例11,添加1,3-PS的实施例12常温循环第100周的容量保持率均有所提高,高温储存性能也进一步得到改善。可见,往本发明的电解液中添加成膜添加剂,电池性能还可以得到进一步优化。As can be seen from Table 1, the embodiment 15, embodiment 17, embodiment 19, embodiment 20 containing surfactant, its capacity retention rate is higher than embodiment 14, embodiment 16, embodiment 18 with the same solvent composition, illustrates The addition of a small amount of fluorocarbon surfactant can improve the cycle performance of the battery; on the basis of embodiment 1, add 2% VC embodiment 7, on the basis of embodiment 13, add VC embodiment 14 cycle performance is improved, in the implementation On the basis of Example 9 and Example 10, Example 11 with ES added and Example 12 with 1,3-PS added had increased capacity retention at the 100th cycle of normal temperature cycle, and the high-temperature storage performance was further improved. It can be seen that the performance of the battery can be further optimized by adding film-forming additives to the electrolyte of the present invention.
表1各实施例和对比例电解液配比,可燃性能以及100周后容量保持率和高温储存后其容量保持率,容量恢复率,厚度膨胀率测试结果Table 1 The ratio of the electrolytes of each embodiment and comparative example, the flammability and the capacity retention rate after 100 weeks and the capacity retention rate after high temperature storage, the capacity recovery rate, and the test results of the thickness expansion rate
以上所述仅为本发明的实施例,并非因此限制本发明的专利范围,凡是利用本发明说明书内容所作的等效结构或等效流程变换,或直接或间接运用在其他相关的技术领域,均同理包括在本发明的专利保护范围内。The above is only an embodiment of the present invention, and does not limit the patent scope of the present invention. Any equivalent structure or equivalent process conversion made by using the content of the description of the present invention, or directly or indirectly used in other related technical fields, shall be The same reasoning is included in the patent protection scope of the present invention.
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