CN114976263A - Solid-state battery integrating positive electrode and electrolyte and preparation method thereof - Google Patents
Solid-state battery integrating positive electrode and electrolyte and preparation method thereof Download PDFInfo
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- 238000002360 preparation method Methods 0.000 title claims abstract description 18
- 239000007784 solid electrolyte Substances 0.000 claims abstract description 32
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- 239000003960 organic solvent Substances 0.000 claims abstract description 12
- 229920000620 organic polymer Polymers 0.000 claims abstract description 10
- 239000012528 membrane Substances 0.000 claims description 28
- 239000002002 slurry Substances 0.000 claims description 17
- ZMXDDKWLCZADIW-UHFFFAOYSA-N N,N-Dimethylformamide Chemical compound CN(C)C=O ZMXDDKWLCZADIW-UHFFFAOYSA-N 0.000 claims description 16
- WEVYAHXRMPXWCK-UHFFFAOYSA-N Acetonitrile Chemical compound CC#N WEVYAHXRMPXWCK-UHFFFAOYSA-N 0.000 claims description 12
- 238000000034 method Methods 0.000 claims description 10
- SECXISVLQFMRJM-UHFFFAOYSA-N N-Methylpyrrolidone Chemical compound CN1CCCC1=O SECXISVLQFMRJM-UHFFFAOYSA-N 0.000 claims description 9
- WHXSMMKQMYFTQS-UHFFFAOYSA-N Lithium Chemical compound [Li] WHXSMMKQMYFTQS-UHFFFAOYSA-N 0.000 claims description 8
- 229910052744 lithium Inorganic materials 0.000 claims description 8
- 229910052782 aluminium Inorganic materials 0.000 claims description 7
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 claims description 7
- 239000011888 foil Substances 0.000 claims description 7
- 238000001291 vacuum drying Methods 0.000 claims description 7
- CSCPPACGZOOCGX-UHFFFAOYSA-N Acetone Chemical compound CC(C)=O CSCPPACGZOOCGX-UHFFFAOYSA-N 0.000 claims description 6
- 239000002033 PVDF binder Substances 0.000 claims description 6
- 229920003171 Poly (ethylene oxide) Polymers 0.000 claims description 6
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- 238000001035 drying Methods 0.000 claims description 6
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- 229910003002 lithium salt Inorganic materials 0.000 claims description 6
- 159000000002 lithium salts Chemical class 0.000 claims description 6
- 229920005569 poly(vinylidene fluoride-co-hexafluoropropylene) Polymers 0.000 claims description 6
- 229920002981 polyvinylidene fluoride Polymers 0.000 claims description 6
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical group [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 5
- 239000006230 acetylene black Substances 0.000 claims description 5
- -1 polytetrafluoroethylene Polymers 0.000 claims description 5
- 239000007774 positive electrode material Substances 0.000 claims description 5
- WYURNTSHIVDZCO-UHFFFAOYSA-N Tetrahydrofuran Chemical compound C1CCOC1 WYURNTSHIVDZCO-UHFFFAOYSA-N 0.000 claims description 4
- 239000006258 conductive agent Substances 0.000 claims description 4
- 239000000463 material Substances 0.000 claims description 4
- 238000002156 mixing Methods 0.000 claims description 4
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- 239000000758 substrate Substances 0.000 claims description 4
- 239000011521 glass Substances 0.000 claims description 3
- 229920002239 polyacrylonitrile Polymers 0.000 claims description 3
- 229910013870 LiPF 6 Inorganic materials 0.000 claims description 2
- 239000004642 Polyimide Substances 0.000 claims description 2
- NRJJZXGPUXHHTC-UHFFFAOYSA-N [Li+].[O--].[O--].[O--].[O--].[Zr+4].[La+3] Chemical compound [Li+].[O--].[O--].[O--].[O--].[Zr+4].[La+3] NRJJZXGPUXHHTC-UHFFFAOYSA-N 0.000 claims description 2
- KFDQGLPGKXUTMZ-UHFFFAOYSA-N [Mn].[Co].[Ni] Chemical compound [Mn].[Co].[Ni] KFDQGLPGKXUTMZ-UHFFFAOYSA-N 0.000 claims description 2
- OCQSXFPWUMTHNA-UHFFFAOYSA-N [O-2].[Al+3].[Zr+4].[La+3].[Li+] Chemical compound [O-2].[Al+3].[Zr+4].[La+3].[Li+] OCQSXFPWUMTHNA-UHFFFAOYSA-N 0.000 claims description 2
- SZEFOBMPGYTUDO-UHFFFAOYSA-N [O-2].[Ta+5].[La+3].[Li+] Chemical compound [O-2].[Ta+5].[La+3].[Li+] SZEFOBMPGYTUDO-UHFFFAOYSA-N 0.000 claims description 2
- DGQGEJIVIMHONW-UHFFFAOYSA-N [O-2].[Ta+5].[Zr+4].[La+3].[Li+] Chemical compound [O-2].[Ta+5].[Zr+4].[La+3].[Li+] DGQGEJIVIMHONW-UHFFFAOYSA-N 0.000 claims description 2
- CVJYOKLQNGVTIS-UHFFFAOYSA-K aluminum;lithium;titanium(4+);phosphate Chemical compound [Li+].[Al+3].[Ti+4].[O-]P([O-])([O-])=O CVJYOKLQNGVTIS-UHFFFAOYSA-K 0.000 claims description 2
- 239000011248 coating agent Substances 0.000 claims description 2
- 238000000576 coating method Methods 0.000 claims description 2
- HNCXPJFPCAYUGJ-UHFFFAOYSA-N dilithium bis(trifluoromethylsulfonyl)azanide Chemical compound [Li+].[Li+].FC(F)(F)S(=O)(=O)[N-]S(=O)(=O)C(F)(F)F.FC(F)(F)S(=O)(=O)[N-]S(=O)(=O)C(F)(F)F HNCXPJFPCAYUGJ-UHFFFAOYSA-N 0.000 claims description 2
- QHGJSLXSVXVKHZ-UHFFFAOYSA-N dilithium;dioxido(dioxo)manganese Chemical compound [Li+].[Li+].[O-][Mn]([O-])(=O)=O QHGJSLXSVXVKHZ-UHFFFAOYSA-N 0.000 claims description 2
- 238000010030 laminating Methods 0.000 claims description 2
- 238000003475 lamination Methods 0.000 claims description 2
- GELKBWJHTRAYNV-UHFFFAOYSA-K lithium iron phosphate Chemical compound [Li+].[Fe+2].[O-]P([O-])([O-])=O GELKBWJHTRAYNV-UHFFFAOYSA-K 0.000 claims description 2
- MHCFAGZWMAWTNR-UHFFFAOYSA-M lithium perchlorate Chemical compound [Li+].[O-]Cl(=O)(=O)=O MHCFAGZWMAWTNR-UHFFFAOYSA-M 0.000 claims description 2
- 239000005486 organic electrolyte Substances 0.000 claims description 2
- 229920001721 polyimide Polymers 0.000 claims description 2
- 238000009824 pressure lamination Methods 0.000 claims description 2
- 238000007790 scraping Methods 0.000 claims description 2
- 239000007787 solid Substances 0.000 claims description 2
- YLQBMQCUIZJEEH-UHFFFAOYSA-N tetrahydrofuran Natural products C=1C=COC=1 YLQBMQCUIZJEEH-UHFFFAOYSA-N 0.000 claims description 2
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 claims 2
- BLJNPOIVYYWHMA-UHFFFAOYSA-N alumane;cobalt Chemical compound [AlH3].[Co] BLJNPOIVYYWHMA-UHFFFAOYSA-N 0.000 claims 1
- 229910001486 lithium perchlorate Inorganic materials 0.000 claims 1
- 229910052759 nickel Inorganic materials 0.000 claims 1
- 238000009792 diffusion process Methods 0.000 abstract description 7
- 239000007788 liquid Substances 0.000 abstract description 5
- 230000000694 effects Effects 0.000 abstract description 2
- 238000007654 immersion Methods 0.000 abstract 1
- 238000005507 spraying Methods 0.000 abstract 1
- 239000000203 mixture Substances 0.000 description 7
- HBBGRARXTFLTSG-UHFFFAOYSA-N Lithium ion Chemical compound [Li+] HBBGRARXTFLTSG-UHFFFAOYSA-N 0.000 description 5
- 229910001416 lithium ion Inorganic materials 0.000 description 5
- 229910001251 solid state electrolyte alloy Inorganic materials 0.000 description 5
- 238000003756 stirring Methods 0.000 description 5
- 229910000664 lithium aluminum titanium phosphates (LATP) Inorganic materials 0.000 description 4
- 239000007921 spray Substances 0.000 description 4
- 229910010707 LiFePO 4 Inorganic materials 0.000 description 3
- 239000012298 atmosphere Substances 0.000 description 3
- 239000011230 binding agent Substances 0.000 description 3
- 238000011161 development Methods 0.000 description 3
- 238000010586 diagram Methods 0.000 description 3
- 239000002270 dispersing agent Substances 0.000 description 3
- 238000011065 in-situ storage Methods 0.000 description 3
- 150000002500 ions Chemical class 0.000 description 3
- 229910052751 metal Inorganic materials 0.000 description 3
- 239000002184 metal Substances 0.000 description 3
- 239000004570 mortar (masonry) Substances 0.000 description 3
- 230000010287 polarization Effects 0.000 description 3
- 238000006116 polymerization reaction Methods 0.000 description 3
- 230000001681 protective effect Effects 0.000 description 3
- 238000001238 wet grinding Methods 0.000 description 3
- 230000001351 cycling effect Effects 0.000 description 2
- 238000013461 design Methods 0.000 description 2
- 238000003760 magnetic stirring Methods 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 229920000642 polymer Polymers 0.000 description 2
- 239000000243 solution Substances 0.000 description 2
- 239000002904 solvent Substances 0.000 description 2
- 229910012851 LiCoO 2 Inorganic materials 0.000 description 1
- 229910014689 LiMnO Inorganic materials 0.000 description 1
- 229910013716 LiNi Inorganic materials 0.000 description 1
- 229910013290 LiNiO 2 Inorganic materials 0.000 description 1
- 239000011149 active material Substances 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 239000003153 chemical reaction reagent Substances 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 229920005570 flexible polymer Polymers 0.000 description 1
- 238000000265 homogenisation Methods 0.000 description 1
- 230000008595 infiltration Effects 0.000 description 1
- 238000001764 infiltration Methods 0.000 description 1
- 230000000670 limiting effect Effects 0.000 description 1
- 229910000625 lithium cobalt oxide Inorganic materials 0.000 description 1
- BFZPBUKRYWOWDV-UHFFFAOYSA-N lithium;oxido(oxo)cobalt Chemical compound [Li+].[O-][Co]=O BFZPBUKRYWOWDV-UHFFFAOYSA-N 0.000 description 1
- 230000014759 maintenance of location Effects 0.000 description 1
- 239000011572 manganese Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 239000003505 polymerization initiator Substances 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 238000012546 transfer Methods 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
- H01M10/052—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
- H01M10/058—Construction or manufacture
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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
-
- 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
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P70/00—Climate change mitigation technologies in the production process for final industrial or consumer products
- Y02P70/50—Manufacturing or production processes characterised by the final manufactured product
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Abstract
本发明属于固态电池技术领域,具体公开了一种正极和电解质一体化的固态电池及其制备方法。通过制备复合固态电解质及复合正极,喷涂少量有机溶剂后将两者贴合,利用正极及固态电解质中的有机聚合物溶于有机溶剂的特性,使得两者的表面呈现液态特性,在贴合接触时达到液液浸润式接触的效果,促进两者间的有效接触,增加离子扩散通路,降低界面阻抗,提升电池性能。
The invention belongs to the technical field of solid-state batteries, and specifically discloses a solid-state battery with an integrated positive electrode and an electrolyte and a preparation method thereof. By preparing a composite solid electrolyte and a composite positive electrode, spraying a small amount of organic solvent and bonding the two, using the properties of the organic polymer in the positive electrode and the solid electrolyte to dissolve in the organic solvent, the surfaces of the two exhibit liquid characteristics, and they are in contact with each other. At the same time, it can achieve the effect of liquid-liquid immersion contact, promote the effective contact between the two, increase the ion diffusion path, reduce the interface impedance, and improve the battery performance.
Description
技术领域technical field
本发明属于固态电池技术领域,具体涉及一体化固态电池。The invention belongs to the technical field of solid-state batteries, and particularly relates to an integrated solid-state battery.
背景技术Background technique
在众多可再生能源中,锂离子电池因其能量密度高、循环寿命长及放电区间稳定等优点脱颖而出。然而,用于动力电池的锂离子电池对安全性要求极高,一定程度上限制了电动汽车的快速发展。Among many renewable energy sources, lithium-ion batteries stand out due to their high energy density, long cycle life and stable discharge range. However, lithium-ion batteries used in power batteries have extremely high safety requirements, which limits the rapid development of electric vehicles to a certain extent.
固态电池因其内部的固态电解质具有良好的机械性能、热稳定性及化学稳定性,安全性能相对高于常规电池。此外,固态电池能量密度更高,适用范围更广。但是目前固态电池的发展较慢,限制其快速发展的主要瓶颈在于固态电解质较差的离子电导率及其与正负极间不良的界面兼容性。通过设计一系列新型固态电解质缓解了固态电解质较差的离子电导率的问题,但固态电解质与正负极间不良的界面兼容性则仍有待解决,且成为了阻碍固态电池走向商业化的主要障碍。界面兼容性包括界面接触及界面反应稳定性两方面。固固界面的不良接触会导致电池的界面阻抗增大,不利于离子的快速扩散,使得电池循环过程中产生极大的极化,进而造成倍率性能差及容量快速衰减等现象。Solid-state batteries have good mechanical properties, thermal stability and chemical stability due to the solid electrolyte inside, and their safety performance is relatively higher than that of conventional batteries. In addition, solid-state batteries have higher energy density and wider application range. However, the current development of solid-state batteries is relatively slow, and the main bottleneck restricting their rapid development lies in the poor ionic conductivity of solid-state electrolytes and their poor interfacial compatibility with positive and negative electrodes. The problem of poor ionic conductivity of solid-state electrolytes has been alleviated by designing a series of new solid-state electrolytes, but the poor interfacial compatibility between solid-state electrolytes and positive and negative electrodes remains to be resolved, and has become a major obstacle to the commercialization of solid-state batteries. . Interface compatibility includes two aspects: interface contact and interface reaction stability. Poor contact at the solid-solid interface will increase the interface impedance of the battery, which is not conducive to the rapid diffusion of ions, resulting in great polarization during the battery cycle, resulting in poor rate performance and rapid capacity decay.
针对固态电池不良的界面接触,研究人员通常采用电解质结构设计、原位聚合、一体化设计的方式促进电解质与电极界面的接触。For the poor interface contact of solid-state batteries, researchers usually use electrolyte structure design, in-situ polymerization, and integrated design to promote the contact between the electrolyte and the electrode interface.
公告号为CN112599847B的专利文献公开了一种由双层固态电解质组装的固态电池,电解质由复合固态电解质层和柔性聚合物固态电解质层构成,同时具备较好的电化学性能和电极电解质界面兼容性。The patent document with the publication number CN112599847B discloses a solid-state battery assembled by a double-layer solid-state electrolyte. The electrolyte is composed of a composite solid-state electrolyte layer and a flexible polymer solid-state electrolyte layer, and has good electrochemical performance and electrode-electrolyte interface compatibility. .
公开号为CN111933894A的专利文献公开了一种原位聚合的固态电池,将含聚合物及聚合引发剂的极片和固态电解质膜分别制备后,两者中的聚合物在一定温度条件下发生二次聚合,原位修饰两者间的界面,得到了界面电阻小、电导率高、耐高电压的固态电池。The patent document whose publication number is CN111933894A discloses a solid-state battery of in-situ polymerization. After the pole piece and the solid-state electrolyte membrane containing the polymer and the polymerization initiator are prepared respectively, the polymer in the two undergoes ionization under a certain temperature condition. Secondary polymerization, in-situ modification of the interface between the two, resulting in a solid-state battery with low interface resistance, high conductivity, and high voltage resistance.
公开号为CN111342124A的专利文献公开了一种一体化成型的固态电池,在制备得到正极、电解质膜及负极后,通过堆叠并进行热压处理,使得固态电池内容实现一体化粘结,提高了电极与电解质间的有效接触。The patent document with the publication number CN111342124A discloses an integrated solid-state battery. After the positive electrode, the electrolyte membrane and the negative electrode are prepared, they are stacked and hot-pressed, so that the contents of the solid-state battery can be integrated and bonded, and the electrode is improved. effective contact with the electrolyte.
然而,上述专利文献公开的固态电池仍然存在循环性能不好、倍率性能不够的问题。However, the solid-state batteries disclosed in the above-mentioned patent documents still have the problems of poor cycle performance and insufficient rate performance.
发明内容SUMMARY OF THE INVENTION
针对现有技术存在的缺陷,本发明的目的是提供一种正极和电解质一体化的固态电池及其制备方法,提高固态电池的循环性能和倍率性能。In view of the defects in the prior art, the purpose of the present invention is to provide a solid-state battery with an integrated positive electrode and an electrolyte and a preparation method thereof, so as to improve the cycle performance and rate performance of the solid-state battery.
为实现上述目的,本发明提供以下具体的技术方案。To achieve the above objects, the present invention provides the following specific technical solutions.
本发明提供一种正极和电解质一体化的固态电池的制备方法,包括以下步骤:The present invention provides a method for preparing a solid-state battery with an integrated positive electrode and an electrolyte, comprising the following steps:
将有机聚合物、无机陶瓷填料、锂盐和有机溶剂Ⅰ混合均匀,得到电解质浆料;真空干燥电解质浆料,制备复合固态电解质膜;Mixing organic polymer, inorganic ceramic filler, lithium salt and organic solvent I uniformly to obtain electrolyte slurry; vacuum drying electrolyte slurry to prepare composite solid electrolyte membrane;
将正极活性物质、导电剂和电解质浆料混合均匀,在铝箔上涂片并烘干,得到正极极片;Mixing the positive electrode active material, the conductive agent and the electrolyte slurry uniformly, coating and drying on the aluminum foil to obtain the positive electrode plate;
在复合固态电解质膜表面和/或正极极片表面均匀喷涂有机溶剂Ⅱ,然后将复合固态电解质膜与正极极片贴合,真空烘干后,与负极组装,得到正极和电解质一体化的固态电池。The organic solvent II is uniformly sprayed on the surface of the composite solid electrolyte membrane and/or the surface of the positive electrode plate, and then the composite solid electrolyte membrane is attached to the positive electrode plate, dried in vacuum, and then assembled with the negative electrode to obtain a solid-state battery integrating the positive electrode and the electrolyte. .
进一步地,在本发明的部分优选实施方式中,所述有机聚合物为聚偏氟乙烯(PVDF)、聚偏氟乙烯-六氟丙烯共聚物(PVDF-HFP)、聚丙烯腈(PAN)、聚环氧乙烷(PEO)中的一种或多种。Further, in some preferred embodiments of the present invention, the organic polymer is polyvinylidene fluoride (PVDF), polyvinylidene fluoride-hexafluoropropylene copolymer (PVDF-HFP), polyacrylonitrile (PAN), One or more of polyethylene oxide (PEO).
进一步地,在本发明的部分优选实施方式中,所述无机陶瓷填料为磷酸钛铝锂(LATP)、锂镧锆氧(LLZO)、锂镧钽氧(LLTO)、锂镧锆铝氧(LLZAO)、锂镧锆钽氧(LLZTO)中的一种或多种。Further, in some preferred embodiments of the present invention, the inorganic ceramic fillers are lithium aluminum titanium phosphate (LATP), lithium lanthanum zirconium oxide (LLZO), lithium lanthanum tantalum oxide (LLTO), lithium lanthanum zirconium aluminum oxide (LLZAO) ), one or more of lithium lanthanum zirconium tantalum oxide (LLZTO).
进一步地,在本发明的部分优选实施方式中,所述锂盐为双三氟甲基磺酸亚酰胺锂(LiTFSI)、双氟磺酰亚胺锂盐(LiFSI)、高氯酸锂(LiClO4)中的一种。Further, in some preferred embodiments of the present invention, the lithium salt is lithium bis-trifluoromethanesulfonimide (LiTFSI), lithium bisfluorosulfonimide (LiFSI), lithium perchlorate (LiClO 4 ) in one.
进一步地,在本发明的部分优选实施方式中,所述有机溶剂Ⅰ为N,N-二甲基甲酰胺(DMF)、丙酮、四氢呋喃、乙腈中的一种或多种,所述有机溶剂Ⅱ为N-甲基吡咯烷酮(NMP)。Further, in some preferred embodiments of the present invention, the organic solvent I is one or more of N,N-dimethylformamide (DMF), acetone, tetrahydrofuran, and acetonitrile, and the organic solvent II It is N-methylpyrrolidone (NMP).
进一步地,在本发明的部分优选实施方式中,电解质浆料中,有机聚合物与无机陶瓷填料的质量比为1:0.05~1,有机聚合物与锂盐的质量比为1:0.2~2。Further, in some preferred embodiments of the present invention, in the electrolyte slurry, the mass ratio of the organic polymer to the inorganic ceramic filler is 1:0.05~1, and the mass ratio of the organic polymer to the lithium salt is 1:0.2~2 .
进一步地,在本发明的部分优选实施方式中,通过以下方式制备得到复合固态电解质膜:将电解质浆料倒入模具中、或刮涂在基底上,然后真空干燥,即可得到一定厚度的复合固态电解质膜。Further, in some preferred embodiments of the present invention, the composite solid electrolyte membrane is prepared by the following methods: pouring the electrolyte slurry into a mold, or scraping on the substrate, and then vacuum drying, a composite solid electrolyte membrane of a certain thickness can be obtained. solid electrolyte membrane.
所述模具为聚四氟乙烯模具或培养皿,所述基底为玻璃、铝箔、聚四氟乙烯、聚酰亚胺中的至少一种。The mold is a polytetrafluoroethylene mold or a petri dish, and the substrate is at least one of glass, aluminum foil, polytetrafluoroethylene, and polyimide.
所述真空干燥的温度为60~90℃,干燥时间为24~48h。The temperature of the vacuum drying is 60~90°C, and the drying time is 24~48h.
进一步地,在本发明的部分优选实施方式中,所述复合固态电解质膜的厚度为50~200μm。Further, in some preferred embodiments of the present invention, the thickness of the composite solid-state electrolyte membrane is 50-200 μm.
进一步地,在本发明的部分优选实施方式中,所述正极活性物质为磷酸铁锂(LiFePO4)、钴酸锂(LiCoO2)、锰酸锂(LiMnO2)、镍酸锂(LiNiO2)、镍钴锰三元材料或镍钴铝三元材料中的一种。Further, in some preferred embodiments of the present invention, the positive electrode active material is lithium iron phosphate (LiFePO 4 ), lithium cobalt oxide (LiCoO 2 ), lithium manganate (LiMnO 2 ), lithium nickelate (LiNiO 2 ) , one of nickel-cobalt-manganese ternary materials or nickel-cobalt-aluminum ternary materials.
进一步地,在本发明的部分优选实施方式中,所述导电剂为乙炔黑。Further, in some preferred embodiments of the present invention, the conductive agent is acetylene black.
进一步地,在本发明的部分优选实施方式中,复合固态电解质膜与正极极片贴合的方式为压力压合;压合时的压力为0.1~2 Mpa。Further, in some preferred embodiments of the present invention, the method of laminating the composite solid electrolyte membrane and the positive electrode plate is pressure lamination; the pressure during lamination is 0.1-2 Mpa.
进一步地,所述真空烘干的温度为80-120℃,时间为0.5-2小时。Further, the temperature of the vacuum drying is 80-120° C., and the time is 0.5-2 hours.
进一步地,在本发明的部分优选实施方式中,组装固态电池时在复合电解质膜及负极极片的界面上滴加含LiPF6的有机电解液。Further, in some preferred embodiments of the present invention, an organic electrolyte solution containing LiPF 6 is dropwise added to the interface between the composite electrolyte membrane and the negative electrode plate when the solid-state battery is assembled.
此外,本发明提供一种正极和电解质一体化的固态电池,通过上述制备方法制备而成。In addition, the present invention provides a solid-state battery with an integrated positive electrode and an electrolyte, which is prepared by the above-mentioned preparation method.
固态电池的关键组分包括正极、固态电解质及负极。正极材料大部分由微米级的活性物质构成,导致正极极片表面极易凹凸不平。同时,固态电解质也因其固态性质而导致表面难以平整。组装电池时,正极与固态电解质间产生点接触或局部接触,造成界面上离子扩散通道少,电池界面阻抗值高,循环时易产生较大的极化,电池库伦效率低、倍率性能及循环稳定性较差。本发明通过制备复合固态电解质及复合正极,喷涂少量有机溶剂后将两者贴合,利用正极及固态电解质中的有机聚合物溶于有机溶剂的特性,使得两者的表面呈现液态特性,在贴合接触时达到液液浸润式接触的效果,促进两者间的有效接触,增加离子扩散通路,降低界面阻抗,提升电池性能。The key components of solid-state batteries include positive electrodes, solid electrolytes, and negative electrodes. Most of the positive electrode material is composed of micron-scale active materials, which causes the surface of the positive electrode sheet to be easily uneven. At the same time, solid-state electrolytes are also difficult to flatten due to their solid-state properties. When assembling the battery, point contact or local contact occurs between the positive electrode and the solid electrolyte, resulting in fewer ion diffusion channels on the interface, high battery interface impedance value, easy to generate large polarization during cycling, low battery coulombic efficiency, rate performance and cycle stability. Poor sex. The present invention prepares a composite solid electrolyte and a composite positive electrode, sprays a small amount of organic solvent and attaches the two, and utilizes the properties of the organic polymer in the positive electrode and the solid electrolyte to dissolve in the organic solvent, so that the surfaces of the two exhibit liquid characteristics, and the surface of the two is liquid. When combined and contacted, the effect of liquid-liquid infiltration contact is achieved, which promotes the effective contact between the two, increases the ion diffusion path, reduces the interface impedance, and improves the battery performance.
与现有技术相比,本发明具有如下有益效果:Compared with the prior art, the present invention has the following beneficial effects:
(1)本发明正极电解质一体化的固态电池,其一体化结构有效降低了电池的界面阻抗并抑制了浓差极化,可具有较高的放电比容量;(1) The solid-state battery with the integrated cathode and electrolyte of the present invention has an integrated structure that effectively reduces the interface impedance of the battery and suppresses the concentration polarization, and can have a higher discharge specific capacity;
(2)一体化的正极与电解质促进了电池内部电流密度的均匀化,从而提高了电池的循环稳定性;(2) The integrated cathode and electrolyte promote the homogenization of the current density inside the battery, thereby improving the cycle stability of the battery;
(3)正极中加入的电解质浆料有利于正极侧锂离子的快速扩散,使得所组装电池的倍率性能好;(3) The electrolyte slurry added to the positive electrode is conducive to the rapid diffusion of lithium ions on the positive electrode side, so that the assembled battery has good rate performance;
(4)本发明方法工艺简单,所需设备与现有产业化的固态电池工艺基本一致,可以直接用于现有生产线生产。(4) The process of the method of the present invention is simple, the required equipment is basically the same as that of the existing industrialized solid-state battery process, and it can be directly used in the production of the existing production line.
附图说明Description of drawings
图1为本发明实施例1组装的正极电解质一体化的固态电池0.1C下的充放电曲线。FIG. 1 is the charge-discharge curve of the solid-state battery with integrated cathode and electrolyte assembled in Example 1 of the present invention at 0.1C.
图2为本发明实施例1组装的正极电解质一体化的固态电池0.5C下的充放电曲线。FIG. 2 is the charge-discharge curve of the solid-state battery with integrated cathode and electrolyte assembled in Example 1 of the present invention at 0.5C.
图3为本发明实施例1组装的正极电解质一体化的固态电池1C下的充放电曲线。FIG. 3 is the charge-discharge curve of the solid-state battery with integrated cathode and electrolyte assembled in Example 1 of the present invention at 1C.
图4为本发明实施例1组装的正极电解质一体化的固态电池2C下的充放电曲线。FIG. 4 is the charge-discharge curve of the solid-state battery with integrated cathode and electrolyte assembled in Example 1 of the present invention at 2C.
图5为本发明实施例1组装的正极电解质一体化的固态电池在0.5C下的循环性能图。FIG. 5 is a cycle performance diagram of the solid-state battery with integrated cathode and electrolyte assembled in Example 1 of the present invention at 0.5C.
图6为本发明实施例1所组装正极电解质一体化的固态电池的倍率性能图。6 is a rate performance diagram of a solid-state battery with an integrated positive electrode electrolyte assembled in Example 1 of the present invention.
图7为本发明实施例1所组装正极电解质一体化的固态电池的电化学阻抗图。7 is an electrochemical impedance diagram of a solid-state battery with an integrated positive electrode and electrolyte assembled in Example 1 of the present invention.
具体实施方式Detailed ways
下面对本发明进行详细描述,本部分的描述仅是示范性和解释性,不应对本发明的保护范围有任何的限制作用。此外,本领域技术人员根据本文件的描述,可以对本文件实施例中以及不同实施例中的特征进行相应组合。The present invention is described in detail below. The description in this section is only exemplary and explanatory, and should not have any limiting effect on the protection scope of the present invention. In addition, according to the description in this document, those skilled in the art can make corresponding combinations of features in the embodiments of this document and in different embodiments.
除非另有定义,下文中所使用的所有专业术语与本领域技术人员通常理解含义相同。本文中所使用的专业术语只是为了描述具体实施例的目的,并不是旨在限制本发明的保护范围。Unless otherwise defined, all technical terms used hereinafter have the same meaning as commonly understood by those skilled in the art. The technical terms used herein are only for the purpose of describing specific embodiments, and are not intended to limit the protection scope of the present invention.
除非另有特别说明,本发明中用到的各种原材料、试剂、仪器和设备等均可通过市场购买得到或者可通过现有方法制备得到。Unless otherwise specified, various raw materials, reagents, instruments and equipment used in the present invention can be purchased from the market or can be prepared by existing methods.
实施例1Example 1
(1)制备复合固态电解质膜:称取0.4 g LiTFSI、0.5 g PVDF、0.1 g LATP,于5 mLDMF中均匀混合,磁力搅拌6 h并超声处理1 h,利用刮涂法将料浆刮涂在玻璃板上,于80℃及真空条件下干燥24 h,除去大部分DMF溶剂,制得复合固态电解质膜;(1) Preparation of composite solid electrolyte membrane: Weigh 0.4 g of LiTFSI, 0.5 g of PVDF, and 0.1 g of LATP, mix them uniformly in 5 mL of DMF, stir magnetically for 6 h and ultrasonically treat them for 1 h. The composite solid electrolyte membrane was prepared by drying the glass plate at 80 °C under vacuum for 24 h to remove most of the DMF solvent;
(2)制备正极极片:称取0.04 g LiTFSI、0.05 g PVDF、0.001 g LATP,于5 mL NMP中均匀混合,磁力搅拌6 h并超声处理1 h,制得固态电解质浆料;称取0.08 g LiFePO4、0.01 g乙炔黑,于研钵中干磨混合均匀,加入0.5 mL电解质浆料作为粘结剂及分散剂进行湿磨,涂覆于铝箔上,在120℃及真空的条件下干燥6 h,制得正极极片;(2) Preparation of positive pole piece: Weigh 0.04 g LiTFSI, 0.05 g PVDF, 0.001 g LATP, mix them uniformly in 5 mL NMP, stir magnetically for 6 h and ultrasonically treat for 1 h to prepare solid electrolyte slurry; weigh 0.08 g g LiFePO 4 , 0.01 g acetylene black were dry-milled and mixed in a mortar, and 0.5 mL of electrolyte slurry was added as a binder and dispersant for wet milling, coated on aluminum foil, and dried at 120°C under vacuum conditions. 6 h, the positive pole piece was prepared;
(3)正极、电解质一体化并组装电池:在复合固态电解质膜及正极极片表面喷涂少量NMP,使其中的PVDF部分溶解后,将两者在1Mpa下进行压合,后置于80℃烘箱真空干燥2小时,得到一体化的正极与电解质;在惰性保护气氛下以金属锂为负极组装成电池。(3) Integrate the positive electrode and the electrolyte and assemble the battery: spray a small amount of NMP on the surface of the composite solid electrolyte membrane and the positive electrode plate to partially dissolve the PVDF, then press the two together at 1Mpa, and then place them in an oven at 80 °C Vacuum dried for 2 hours to obtain an integrated positive electrode and electrolyte; in an inert protective atmosphere, a battery was assembled with metal lithium as the negative electrode.
将组装好的电池在2.7-4.3 V的电压范围内进行电化学性能测试 (1 C=170 mA/g),结果如图1~7所示:在0.1C的倍率下放电比容量达158.4mAh/g,0.2C倍率下的放电比容量为158.0mAh/g,0.3C倍率下的放电比容量为158.1mAh/g,0.5C倍率下的放电比容量为155.8mAh/g,1C倍率下的放电比容量为146.8mAh/g,2C倍率下的放电比容量为126.7mAh/g,组装得到的电池倍率性能好;在0.5C下循环50圈后容量保持率为96.3%,组装得到的电池循环稳定性好;电解质体相阻抗为13 Ω,电荷转移阻抗为202 Ω,锂离子扩散系数为6.8×10-13 cm2 s-1,组装得到的电池阻抗小,锂离子扩散速度快。The assembled battery was tested for electrochemical performance in the voltage range of 2.7-4.3 V (1 C=170 mA/g). The results are shown in Figures 1-7: the specific discharge capacity reaches 158.4 mAh at a rate of 0.1 C. /g, the discharge specific capacity at 0.2C rate is 158.0mAh/g, the discharge specific capacity at 0.3C rate is 158.1mAh/g, the discharge specific capacity at 0.5C rate is 155.8mAh/g, the discharge specific capacity at 1C rate The specific capacity is 146.8mAh/g, the discharge specific capacity at 2C rate is 126.7mAh/g, and the assembled battery has good rate performance; after 50 cycles at 0.5C, the capacity retention rate is 96.3%, and the assembled battery has stable cycling. The electrolyte bulk impedance is 13 Ω, the charge transfer impedance is 202 Ω, and the lithium ion diffusion coefficient is 6.8×10 -13 cm 2 s -1 . The assembled battery has low impedance and fast lithium ion diffusion.
实施例2Example 2
(1)制备复合固态电解质膜:称取0.3 g LiTFSI、0.6 g PVDF-HFP、0.1 g LLZAO,于10 mL DMF中均匀混合,磁力搅拌6 h并超声处理1 h,倒入培养皿中于90℃及真空条件下干燥24 h,除去大部分DMF溶剂,制得复合固态电解质膜;(1) Preparation of composite solid electrolyte membrane: Weigh 0.3 g LiTFSI, 0.6 g PVDF-HFP, and 0.1 g LLZAO, mix them uniformly in 10 mL DMF, stir magnetically for 6 h and ultrasonicate for 1 h, pour them into a petri dish at 90 The composite solid electrolyte membrane was prepared by drying under vacuum conditions at ℃ for 24 h to remove most of the DMF solvent;
(2)制备正极极片:称取0.03 g LiTFSI、0.06 g PVDF-HFP、0.01 g LLZAO,于3 mLNMP中均匀混合,磁力搅拌6 h并超声处理1 h,制得固态电解质浆料;称取0.08gLiNi0.83Co0.11Mn0.06O2、0.01g乙炔黑,于研钵中干磨混合均匀,加入0.3 mL电解质浆料作为粘结剂及分散剂进行湿磨,涂覆于铝箔上,在120℃及真空的条件下干燥6 h,制得正极极片;(2) Preparation of positive pole piece: Weigh 0.03 g LiTFSI, 0.06 g PVDF-HFP, and 0.01 g LLZAO, mix them uniformly in 3 mL NMP, stir magnetically for 6 h and ultrasonically treat for 1 h to prepare a solid electrolyte slurry; 0.08g LiNi 0.83 Co 0.11 Mn 0.06 O 2 , 0.01g acetylene black were dry-milled in a mortar and mixed uniformly, 0.3 mL of electrolyte slurry was added as a binder and a dispersant for wet-milling, and coated on aluminum foil at 120°C and drying under vacuum conditions for 6 h to obtain a positive electrode plate;
(3)正极、电解质一体化并组装电池:在复合固态电解质膜及正极极片表面喷涂少量NMP,使其中的PVDF-HFP部分溶解后,将两者在0.5Mpa下进行压合,后置于120℃烘箱真空干燥0.5小时,得到一体化的正极与电解质;在惰性保护气氛的手套箱中以金属锂为负极组装成电池。(3) Integrate the positive electrode and the electrolyte and assemble the battery: spray a small amount of NMP on the surface of the composite solid electrolyte membrane and the positive electrode plate to partially dissolve the PVDF-HFP, then press the two at 0.5Mpa, and then place the Vacuum-drying in a 120°C oven for 0.5 hours to obtain an integrated positive electrode and electrolyte; in a glove box with an inert protective atmosphere, a battery was assembled with metal lithium as the negative electrode.
实施例3Example 3
(1)制备复合固态电解质膜:称取0.3 g LiFSI、0.5 g PEO,于10 mL 乙腈中均匀混合,磁力搅拌4 h后加入0.2 g LLZTO,继续磁力搅拌4小时并超声处理1 h,倒入培养皿中于60℃及真空条件下干燥48 h,除去大部分乙腈,制得复合固态电解质膜;(1) Preparation of composite solid electrolyte membrane: Weigh 0.3 g LiFSI and 0.5 g PEO, mix them uniformly in 10 mL acetonitrile, add 0.2 g LLZTO after magnetic stirring for 4 h, continue magnetic stirring for 4 hours and ultrasonically treat for 1 h, pour into The petri dish was dried at 60 °C under vacuum for 48 h to remove most of the acetonitrile to obtain a composite solid electrolyte membrane;
(2)制备正极极片:称取0.03 g LiFSI、0.05 g PEO、0.02 g LLZTO,于5 mL NMP中均匀混合,磁力搅拌6 h并超声处理1 h,制得固态电解质浆料;称取0.08 g LiFePO4、0.01g乙炔黑,于研钵中干磨混合均匀,加入0.5 mL电解质浆料作为粘结剂及分散剂进行湿磨,涂覆于铝箔上,在120℃及真空的条件下干燥6 h,制得复合正极极片;(2) Preparation of positive pole piece: Weigh 0.03 g LiFSI, 0.05 g PEO, 0.02 g LLZTO, mix them uniformly in 5 mL NMP, stir magnetically for 6 h and ultrasonically treat for 1 h to prepare a solid electrolyte slurry; weigh 0.08 g g LiFePO 4 , 0.01 g acetylene black, dry and mix in a mortar, add 0.5 mL of electrolyte slurry as a binder and dispersant for wet grinding, coat on aluminum foil, and dry at 120°C under vacuum conditions 6 h, the composite positive electrode was prepared;
(3)正极电解质一体化并组装电池:在复合固态电解质膜及正极极片表面喷涂少量NMP,使其中的PEO部分溶解后,将两者在0.8Mpa下进行压合,后置于100℃烘箱真空干燥1小时,得到一体化的正极与电解质;在惰性保护气氛的手套箱中以金属锂为负极组装成电池。(3) Integrate the positive electrode and the electrolyte and assemble the battery: spray a small amount of NMP on the surface of the composite solid electrolyte membrane and the positive electrode piece to dissolve the PEO in it, then press the two together at 0.8Mpa, and then place them in a 100°C oven Vacuum dried for 1 hour to obtain an integrated positive electrode and electrolyte; in a glove box in an inert protective atmosphere, a battery was assembled with metal lithium as the negative electrode.
以上所述实施例,仅为本发明较佳的具体实施方式,但本发明的保护范围并不局限于此,任何熟悉本技术领域的技术人员在本发明的技术范围内,根据本发明的技术方案及其构思加以等同替换或改变,都应涵盖在本发明的保护范围内。The above-mentioned embodiments are only preferred specific embodiments of the present invention, but the protection scope of the present invention is not limited thereto. The equivalent replacement or change of the solution and its concept shall be included within the protection scope of the present invention.
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