CN117673371B - A method for preparing a current collector for a negative electrode-free lithium metal battery, a current collector and applications thereof - Google Patents
A method for preparing a current collector for a negative electrode-free lithium metal battery, a current collector and applications thereof Download PDFInfo
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- 229910052744 lithium Inorganic materials 0.000 title claims abstract description 111
- 238000000034 method Methods 0.000 title claims abstract description 41
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- 238000000576 coating method Methods 0.000 claims abstract description 41
- 229910052751 metal Inorganic materials 0.000 claims abstract description 37
- 239000002184 metal Substances 0.000 claims abstract description 37
- -1 N-cyanovinyl pyrrolidone Chemical compound 0.000 claims abstract description 34
- 238000002360 preparation method Methods 0.000 claims abstract description 31
- WHNWPMSKXPGLAX-UHFFFAOYSA-N N-Vinyl-2-pyrrolidone Chemical compound C=CN1CCCC1=O WHNWPMSKXPGLAX-UHFFFAOYSA-N 0.000 claims abstract description 26
- 238000006116 polymerization reaction Methods 0.000 claims abstract description 23
- 238000011065 in-situ storage Methods 0.000 claims abstract description 22
- 239000002105 nanoparticle Substances 0.000 claims abstract description 17
- 239000003999 initiator Substances 0.000 claims abstract description 11
- 238000010438 heat treatment Methods 0.000 claims abstract description 9
- 239000011259 mixed solution Substances 0.000 claims abstract description 5
- 239000011261 inert gas Substances 0.000 claims abstract description 4
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 claims description 48
- OZAIFHULBGXAKX-UHFFFAOYSA-N 2-(2-cyanopropan-2-yldiazenyl)-2-methylpropanenitrile Chemical compound N#CC(C)(C)N=NC(C)(C)C#N OZAIFHULBGXAKX-UHFFFAOYSA-N 0.000 claims description 30
- 229910052759 nickel Inorganic materials 0.000 claims description 24
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 claims description 23
- 229910052802 copper Inorganic materials 0.000 claims description 21
- 239000010949 copper Substances 0.000 claims description 21
- BQCADISMDOOEFD-UHFFFAOYSA-N Silver Chemical compound [Ag] BQCADISMDOOEFD-UHFFFAOYSA-N 0.000 claims description 15
- 238000004528 spin coating Methods 0.000 claims description 12
- 239000000843 powder Substances 0.000 claims description 10
- XLOMVQKBTHCTTD-UHFFFAOYSA-N Zinc monoxide Chemical compound [Zn]=O XLOMVQKBTHCTTD-UHFFFAOYSA-N 0.000 claims description 8
- XOLBLPGZBRYERU-UHFFFAOYSA-N tin dioxide Chemical compound O=[Sn]=O XOLBLPGZBRYERU-UHFFFAOYSA-N 0.000 claims description 8
- HCHKCACWOHOZIP-UHFFFAOYSA-N Zinc Chemical compound [Zn] HCHKCACWOHOZIP-UHFFFAOYSA-N 0.000 claims description 5
- 229910001923 silver oxide Inorganic materials 0.000 claims description 5
- NDVLTYZPCACLMA-UHFFFAOYSA-N silver oxide Substances [O-2].[Ag+].[Ag+] NDVLTYZPCACLMA-UHFFFAOYSA-N 0.000 claims description 5
- 239000011787 zinc oxide Substances 0.000 claims description 5
- WMKGMCCZGTXXQU-UHFFFAOYSA-N 2,3-benzodioxine-1,4-dione Chemical compound C1=CC=C2C(=O)OOC(=O)C2=C1 WMKGMCCZGTXXQU-UHFFFAOYSA-N 0.000 claims description 3
- 238000007606 doctor blade method Methods 0.000 claims description 3
- 239000002245 particle Substances 0.000 claims description 3
- ATJFFYVFTNAWJD-UHFFFAOYSA-N Tin Chemical compound [Sn] ATJFFYVFTNAWJD-UHFFFAOYSA-N 0.000 claims 1
- WHXSMMKQMYFTQS-UHFFFAOYSA-N Lithium Chemical compound [Li] WHXSMMKQMYFTQS-UHFFFAOYSA-N 0.000 abstract description 41
- 239000011248 coating agent Substances 0.000 abstract description 27
- 230000008021 deposition Effects 0.000 abstract description 16
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- 229920000642 polymer Polymers 0.000 description 20
- 238000000151 deposition Methods 0.000 description 15
- GELKBWJHTRAYNV-UHFFFAOYSA-K lithium iron phosphate Chemical compound [Li+].[Fe+2].[O-]P([O-])([O-])=O GELKBWJHTRAYNV-UHFFFAOYSA-K 0.000 description 14
- 238000012360 testing method Methods 0.000 description 13
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- 101001121408 Homo sapiens L-amino-acid oxidase Proteins 0.000 description 5
- 102100026388 L-amino-acid oxidase Human genes 0.000 description 5
- 101100012902 Saccharomyces cerevisiae (strain ATCC 204508 / S288c) FIG2 gene Proteins 0.000 description 5
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 4
- HBBGRARXTFLTSG-UHFFFAOYSA-N Lithium ion Chemical compound [Li+] HBBGRARXTFLTSG-UHFFFAOYSA-N 0.000 description 4
- 229910001416 lithium ion Inorganic materials 0.000 description 4
- 238000004519 manufacturing process Methods 0.000 description 4
- ZQCQTPBVJCWETB-UHFFFAOYSA-N 4-fluoro-1,3-dioxol-2-one Chemical compound FC1=COC(=O)O1 ZQCQTPBVJCWETB-UHFFFAOYSA-N 0.000 description 3
- OIFBSDVPJOWBCH-UHFFFAOYSA-N Diethyl carbonate Chemical compound CCOC(=O)OCC OIFBSDVPJOWBCH-UHFFFAOYSA-N 0.000 description 3
- 239000011230 binding agent Substances 0.000 description 3
- 229920001940 conductive polymer Polymers 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 239000003792 electrolyte Substances 0.000 description 3
- 239000002904 solvent Substances 0.000 description 3
- SECXISVLQFMRJM-UHFFFAOYSA-N N-Methylpyrrolidone Chemical compound CN1CCCC1=O SECXISVLQFMRJM-UHFFFAOYSA-N 0.000 description 2
- 239000004743 Polypropylene Substances 0.000 description 2
- 239000002041 carbon nanotube Substances 0.000 description 2
- 229910021393 carbon nanotube Inorganic materials 0.000 description 2
- 239000000919 ceramic Substances 0.000 description 2
- 238000005524 ceramic coating Methods 0.000 description 2
- 239000011889 copper foil Substances 0.000 description 2
- 125000004093 cyano group Chemical group *C#N 0.000 description 2
- 238000011161 development Methods 0.000 description 2
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- 238000009776 industrial production Methods 0.000 description 2
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- 239000000243 solution Substances 0.000 description 2
- 238000003756 stirring Methods 0.000 description 2
- 238000001291 vacuum drying Methods 0.000 description 2
- HJGJHDZQLWWMRT-UHFFFAOYSA-N 2,2,2-trifluoroethyl hydrogen carbonate Chemical compound OC(=O)OCC(F)(F)F HJGJHDZQLWWMRT-UHFFFAOYSA-N 0.000 description 1
- 101000827703 Homo sapiens Polyphosphoinositide phosphatase Proteins 0.000 description 1
- 229910013870 LiPF 6 Inorganic materials 0.000 description 1
- 239000002033 PVDF binder Substances 0.000 description 1
- 102100023591 Polyphosphoinositide phosphatase Human genes 0.000 description 1
- 101100233916 Saccharomyces cerevisiae (strain ATCC 204508 / S288c) KAR5 gene Proteins 0.000 description 1
- SYRDSFGUUQPYOB-UHFFFAOYSA-N [Li+].[Li+].[Li+].[O-]B([O-])[O-].FC(=O)C(F)=O Chemical compound [Li+].[Li+].[Li+].[O-]B([O-])[O-].FC(=O)C(F)=O SYRDSFGUUQPYOB-UHFFFAOYSA-N 0.000 description 1
- 239000011149 active material Substances 0.000 description 1
- 230000032683 aging Effects 0.000 description 1
- 230000004888 barrier function Effects 0.000 description 1
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- 229910001593 boehmite Inorganic materials 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 210000004027 cell Anatomy 0.000 description 1
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- 239000002270 dispersing agent Substances 0.000 description 1
- 239000011267 electrode slurry Substances 0.000 description 1
- 125000006575 electron-withdrawing group Chemical group 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000002708 enhancing effect Effects 0.000 description 1
- 239000011888 foil Substances 0.000 description 1
- 239000010439 graphite Substances 0.000 description 1
- 229910002804 graphite Inorganic materials 0.000 description 1
- FAHBNUUHRFUEAI-UHFFFAOYSA-M hydroxidooxidoaluminium Chemical compound O[Al]=O FAHBNUUHRFUEAI-UHFFFAOYSA-M 0.000 description 1
- 238000002347 injection Methods 0.000 description 1
- 239000007924 injection Substances 0.000 description 1
- 238000011031 large-scale manufacturing process Methods 0.000 description 1
- 230000007774 longterm Effects 0.000 description 1
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 230000006911 nucleation Effects 0.000 description 1
- 238000010899 nucleation Methods 0.000 description 1
- 238000011056 performance test Methods 0.000 description 1
- 239000002985 plastic film Substances 0.000 description 1
- 229920006255 plastic film Polymers 0.000 description 1
- 229920000767 polyaniline Polymers 0.000 description 1
- 230000000379 polymerizing effect Effects 0.000 description 1
- 229920000128 polypyrrole Polymers 0.000 description 1
- 229920002981 polyvinylidene fluoride Polymers 0.000 description 1
- 239000007774 positive electrode material Substances 0.000 description 1
- 230000001737 promoting effect Effects 0.000 description 1
- 230000009257 reactivity Effects 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
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Classifications
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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
- H01M4/00—Electrodes
- H01M4/02—Electrodes composed of, or comprising, active material
- H01M4/64—Carriers or collectors
- H01M4/66—Selection of materials
- H01M4/665—Composites
- H01M4/667—Composites in the form of layers, e.g. coatings
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
- C08F226/00—Copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a single or double bond to nitrogen or by a heterocyclic ring containing nitrogen
- C08F226/06—Copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a single or double bond to nitrogen or by a heterocyclic ring containing nitrogen by a heterocyclic ring containing nitrogen
- C08F226/10—N-Vinyl-pyrrolidone
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M10/00—Secondary cells; Manufacture thereof
- H01M10/05—Accumulators with non-aqueous electrolyte
- H01M10/052—Li-accumulators
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/10—Energy storage using batteries
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- General Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Electrochemistry (AREA)
- Medicinal Chemistry (AREA)
- Polymers & Plastics (AREA)
- Organic Chemistry (AREA)
- Manufacturing & Machinery (AREA)
- Health & Medical Sciences (AREA)
- Composite Materials (AREA)
- Materials Engineering (AREA)
- Battery Electrode And Active Subsutance (AREA)
Abstract
Description
技术领域Technical Field
本发明涉及一种无负极锂金属电池用集流体制备方法及集流体和应用,属于新能源技术领域。The invention relates to a method for preparing a current collector for a negative electrode-free lithium metal battery, the current collector and application thereof, and belongs to the field of new energy technology.
背景技术Background technique
开发新型高能量密度二次电池体系是保障我国能源安全、推动我国能源产业升级的重要一环。目前广泛应用的商业化锂离子电池能量密度已接近理论上限,具有更高能量密度的新型二次电池体系亟待开发。近年来,采用低电位、高容量的金属锂代替石墨负极组装而成的锂金属电池逐渐受到研究人员的广泛关注。然而,由于金属锂的高反应活性,锂金属电池对电池的组装环境要求极为苛刻。且金属锂箔制造难度大、储存成本高,生产安全问题突出,故目前锂金属电池难以实现大规模生产。同时,锂金属电池在循环过程中易在负极侧生成枝晶状金属锂,甚至存在锂枝晶刺穿隔膜造成电池内短路从而引起电池热失控的风险,极大限制了锂金属电池的发展与应用。The development of new high-energy-density secondary battery systems is an important part of ensuring my country's energy security and promoting the upgrading of my country's energy industry. The energy density of commercial lithium-ion batteries that are currently widely used is close to the theoretical upper limit, and new secondary battery systems with higher energy density are urgently needed to be developed. In recent years, lithium metal batteries assembled with low-potential, high-capacity metallic lithium instead of graphite negative electrodes have gradually attracted widespread attention from researchers. However, due to the high reactivity of metallic lithium, lithium metal batteries have extremely demanding requirements on the assembly environment of the battery. In addition, the manufacturing of metallic lithium foil is difficult, the storage cost is high, and the production safety issues are prominent, so it is currently difficult to achieve large-scale production of lithium metal batteries. At the same time, lithium metal batteries are prone to generate dendritic metallic lithium on the negative electrode side during the cycle process, and there is even a risk that lithium dendrites pierce the diaphragm to cause a short circuit in the battery and cause thermal runaway of the battery, which greatly limits the development and application of lithium metal batteries.
无负极锂金属电池有望成为解决上述难题的理想方案。与普通锂金属电池不同,该电池体系中所有锂源均由正极活性物质提供,无需使用活泼金属锂。由于电池体系中不存在预置的负极活性组分,无负极锂金属电池的能量密度较商业化锂离子电池大幅提升。同时,这一电池体系未使用高度活泼的金属锂,故而在电池组装的过程中不需要维持严苛的组装环境,可直接兼容锂离子电池的生产线,易于实现大规模工业化生产。然而,由于常用金属集流体(如铜、镍集流体)与锂亲和性差,金属锂在其表面的沉积困难,并容易形成枝晶引起电池短路,限制了无负极锂金属电池的应用。Negative electrode-free lithium metal batteries are expected to be an ideal solution to the above problems. Unlike ordinary lithium metal batteries, all lithium sources in this battery system are provided by positive electrode active materials, and there is no need to use active metallic lithium. Since there are no pre-set negative electrode active components in the battery system, the energy density of negative electrode-free lithium metal batteries is greatly improved compared to commercial lithium-ion batteries. At the same time, this battery system does not use highly active metallic lithium, so there is no need to maintain a strict assembly environment during the battery assembly process. It can be directly compatible with the production line of lithium-ion batteries and is easy to achieve large-scale industrial production. However, due to the poor affinity of commonly used metal current collectors (such as copper and nickel current collectors) with lithium, it is difficult to deposit metallic lithium on their surfaces, and it is easy to form dendrites that cause battery short circuits, which limits the application of negative electrode-free lithium metal batteries.
中国专利申请CN114597421A中公开了一种无负极锂金属电池负极集流体及其制备方法和应用,所述负极集流体的制备方法为:将粘结剂和导电高分子聚合物与溶剂混合,得到浆料;然后将浆料涂覆在铜箔表面,真空干燥后得到所述负极集流体,其中导电高分子聚合物包括聚吡咯和/或聚苯胺中的任意一种或至少两种的组合。这种制备方法,需要先聚合制备导电高分子聚合物,然后再通过溶剂导电高分子聚合物,并加入粘结剂,涂覆到铜箔表面后,再脱除溶剂得到负极集流体,制备方法繁杂,不易操作,而且在实际操作中很容易导致负极集流体表面出现均匀度差的问题,导致电池一致性差。Chinese patent application CN114597421A discloses a negative electrode current collector for a lithium metal battery without a negative electrode, and a preparation method and application thereof. The preparation method of the negative electrode current collector is: mixing a binder and a conductive polymer with a solvent to obtain a slurry; then coating the slurry on the surface of a copper foil, and vacuum drying to obtain the negative electrode current collector, wherein the conductive polymer includes any one of polypyrrole and/or polyaniline or a combination of at least two. This preparation method requires first polymerizing a conductive polymer, then conducting the polymer through a solvent, adding a binder, and coating it on the surface of the copper foil, and then removing the solvent to obtain the negative electrode current collector. The preparation method is complicated and difficult to operate, and in actual operation, it is easy to cause the surface of the negative electrode current collector to have poor uniformity, resulting in poor battery consistency.
发明内容Summary of the invention
本发明针对现有技术存在的不足,提供一种无负极锂金属电池用集流体制备方法及集流体和应用,所述集流体可在电池化成过程中与活性锂组分形成亲锂合金位点,可诱导均匀的锂沉积,从而提高电池库伦效率、延长电池循环寿命,解决了无负极锂金属电池安全性差、使用寿命短的难题。In view of the deficiencies in the prior art, the present invention provides a method for preparing a current collector for a negative electrode-free lithium metal battery, a current collector and an application thereof. The current collector can form lithium-philic alloy sites with active lithium components during the battery formation process, and can induce uniform lithium deposition, thereby improving the battery coulombic efficiency and extending the battery cycle life, thus solving the problem of poor safety and short service life of negative electrode-free lithium metal batteries.
本发明解决上述技术问题的技术方案如下:一种无负极锂金属电池用集流体制备方法,所述制备方法为:The technical solution of the present invention to solve the above technical problems is as follows: a method for preparing a current collector for a negative electrode-free lithium metal battery, the preparation method comprising:
惰性气体保护下,将亲锂纳米颗粒和引发剂均匀的分散在N-乙烯基吡咯烷酮和N-氰乙烯基吡咯烷酮的混合溶液中形成浆料,将所述浆料均匀涂布在金属集流体表面并通过加热原位聚合,得到无负极锂金属电池用集流体。Under the protection of inert gas, lithium-philic nanoparticles and initiators are uniformly dispersed in a mixed solution of N-vinyl pyrrolidone and N-cyanovinyl pyrrolidone to form a slurry, and the slurry is uniformly coated on the surface of the metal current collector and in-situ polymerized by heating to obtain a current collector for a negative electrode-free lithium metal battery.
进一步的,所述亲锂纳米颗粒选自纳米银粉、纳米锡粉、纳米锌粉、纳米氧化银、纳米二氧化锡、纳米氧化锌中的至少一种。Furthermore, the lithium-philic nanoparticles are selected from at least one of nano-silver powder, nano-tin powder, nano-zinc powder, nano-silver oxide, nano-tin dioxide, and nano-zinc oxide.
进一步的,所述引发剂选自偶氮二异丁腈、过氧化邻苯二甲酰中的至少一种,所述引发剂用量为所述浆料总质量的0.08~0.20%。Furthermore, the initiator is selected from at least one of azobisisobutyronitrile and phthaloyl peroxide, and the amount of the initiator is 0.08-0.20% of the total mass of the slurry.
优选的,所述引发剂为偶氮二异丁腈。Preferably, the initiator is azobisisobutyronitrile.
进一步的,所述金属集流体为铜集流体、镍集流体中的一种。Furthermore, the metal current collector is one of a copper current collector and a nickel current collector.
进一步的,所述亲锂纳米颗粒选的粒径为50~100 nm,所述的亲锂纳米颗粒用量为所述浆料总质量的15~40%。Furthermore, the particle size of the lithium-philic nanoparticles is 50-100 nm, and the amount of the lithium-philic nanoparticles is 15-40% of the total mass of the slurry.
进一步的,进一步的,所述N-乙烯基吡咯烷酮用量占所述浆料总质量的35~75%;所述N-氰乙烯基吡咯烷酮用量占所述浆料总质量的5~30%。Furthermore, further, the amount of N-vinyl pyrrolidone accounts for 35-75% of the total mass of the slurry; the amount of N-cyanovinyl pyrrolidone accounts for 5-30% of the total mass of the slurry.
进一步的,加热原位聚合的温度为60-120℃,加热原位聚合时间为1-5h。Furthermore, the temperature of the heating in-situ polymerization is 60-120° C., and the heating in-situ polymerization time is 1-5 h.
进一步的,将所述浆料均匀涂布在金属集流体表面所使用的涂布方法为刮刀涂布法或旋转涂布法。Furthermore, the coating method used to uniformly coat the slurry on the surface of the metal current collector is a doctor blade coating method or a spin coating method.
本发明还公开了一种无负极锂金属电池用集流体,所述集流体为通过本发明所述制备方法制得的。The present invention also discloses a current collector for a negative electrode-free lithium metal battery, wherein the current collector is prepared by the preparation method of the present invention.
本发明还公开了一种无负极锂金属电池用集流体的应用,所述集流体应用于无负极锂金属电池。The present invention also discloses an application of a current collector for a negative electrode-free lithium metal battery, wherein the current collector is applied to the negative electrode-free lithium metal battery.
本发明的有益效果是:The beneficial effects of the present invention are:
(1)本发明所述制备方法利用原位聚合概念,向N-乙烯基吡咯烷酮中引入含有强极性的氰基结构的N-氰乙烯基吡咯烷酮,增强亲锂纳米颗粒与集流体的黏结强度,确保活性材料不脱落,从而提高电池的循环寿命,同时N-氰乙烯基吡咯烷酮还能够避免N-乙烯基吡咯烷酮聚合后的晶化现象。(1) The preparation method of the present invention utilizes the concept of in-situ polymerization to introduce N-cyanovinylpyrrolidone containing a strongly polar cyano structure into N-vinylpyrrolidone, thereby enhancing the bonding strength between the lithium-philic nanoparticles and the current collector, ensuring that the active material does not fall off, thereby improving the cycle life of the battery. At the same time, N-cyanovinylpyrrolidone can also avoid the crystallization phenomenon after the polymerization of N-vinylpyrrolidone.
(2)本发明所述制备方法采用原位聚合法得到的集流体,可在电池化成过程中与活性锂组分形成亲锂合金位点,其上的锂沉积成核势垒远低于金属集流体,故可诱导均匀的锂沉积,从而提高电池库伦效率、延长电池循环寿命。(2) The current collector obtained by the preparation method of the present invention using the in-situ polymerization method can form lithium-philic alloy sites with active lithium components during the battery formation process. The nucleation barrier of lithium deposition on the current collector is much lower than that of the metal current collector, so it can induce uniform lithium deposition, thereby improving the battery coulombic efficiency and extending the battery cycle life.
(3)本发明采用原位聚合法所制备的集流体能够减少电解液与金属集流体及锂沉积产物的接触,抑制负极侧副反应的进行,以减少锂源损失进而延长电池的使用寿命。同时,N-乙烯基吡咯烷酮和N-氰乙烯基吡咯烷酮混合液原位聚合后的聚合物,能够通过物理压制作用抑制锂枝晶的生长,降低枝晶状锂刺穿隔膜造成电池内短路的风险。(3) The current collector prepared by the in-situ polymerization method of the present invention can reduce the contact between the electrolyte and the metal current collector and the lithium deposition product, inhibit the side reaction on the negative electrode side, thereby reducing the loss of lithium source and thus extending the service life of the battery. At the same time, the polymer obtained by in-situ polymerization of the mixed solution of N-vinyl pyrrolidone and N-cyanovinyl pyrrolidone can inhibit the growth of lithium dendrites through physical suppression, reducing the risk of dendritic lithium piercing the diaphragm and causing a short circuit in the battery.
(4)本发明所述集流体制备方法工艺简单,成本低廉,可直接用于锂离子电池极片生产线,适用于大规模工业化生产。(4) The current collector preparation method of the present invention has a simple process and low cost, can be directly used in a lithium-ion battery electrode production line, and is suitable for large-scale industrial production.
附图说明BRIEF DESCRIPTION OF THE DRAWINGS
图1是本发明实施例1制备的无负极锂金属电池的库伦效率与循环稳定性图;FIG1 is a graph showing the coulombic efficiency and cycle stability of a negative electrode-free lithium metal battery prepared in Example 1 of the present invention;
图2是本发明实施例2制备的无负极锂金属电池的首圈容量-电压曲线;FIG2 is a first cycle capacity-voltage curve of a negative electrode-free lithium metal battery prepared in Example 2 of the present invention;
图3是本发明实施例3制备的浆料的光学照片;FIG3 is an optical photograph of the slurry prepared in Example 3 of the present invention;
图4是本发明实施例4制备的集流体的扫描电子显微镜照片;FIG4 is a scanning electron microscope photograph of the current collector prepared in Example 4 of the present invention;
图5是本发明实施例5制备的无负极锂金属电池首次充电后负极侧金属锂沉积的扫描电子显微镜照片;FIG5 is a scanning electron microscope photograph of metallic lithium deposition on the negative electrode side of the negative electrode-free lithium metal battery prepared in Example 5 of the present invention after the first charge;
图6是本发明实施例6制备的无负极锂金属电池首次放电后改性镍集流体表面的扫描电子显微镜照片。6 is a scanning electron microscope photograph of the surface of the modified nickel current collector after the first discharge of the negative electrode-free lithium metal battery prepared in Example 6 of the present invention.
具体实施方式Detailed ways
下面对本发明的具体实施方式做详细说明。本发明能够以很多不同于在此描述的其它方式来实施,本领域技术人员可以在不违背本发明内涵的情况下做类似改进,因此本发明不受公开的具体实施例的限制。The specific implementation of the present invention is described in detail below. The present invention can be implemented in many other ways than those described herein, and those skilled in the art can make similar improvements without violating the connotation of the present invention, so the present invention is not limited by the specific embodiments disclosed.
除非另有定义,本文所使用的所有技术和科学术语与本发明所属技术领域的技术人员通常理解的含义相同。所使用的术语只为描述具体实施方式,不为限制本发明。Unless otherwise defined, all technical and scientific terms used herein have the same meaning as those commonly understood by those skilled in the art to which the present invention belongs. The terms used are only for describing specific embodiments and are not intended to limit the present invention.
一种无负极锂金属电池用集流体制备方法,所述制备方法为:A method for preparing a current collector for a negative electrode-free lithium metal battery, the preparation method comprising:
惰性气体保护下,将亲锂纳米颗粒和引发剂均匀的分散在N-乙烯基吡咯烷酮和N-氰乙烯基吡咯烷酮的混合溶液中形成浆料,将所述浆料均匀涂布在金属集流体表面并通过加热原位聚合,得到无负极锂金属电池用集流体。Under the protection of inert gas, lithium-philic nanoparticles and initiators are uniformly dispersed in a mixed solution of N-vinyl pyrrolidone and N-cyanovinyl pyrrolidone to form a slurry, and the slurry is uniformly coated on the surface of the metal current collector and in-situ polymerized by heating to obtain a current collector for a negative electrode-free lithium metal battery.
所述N-乙烯基吡咯烷酮和N-氰乙烯基吡咯烷酮结构式如式I和式II所示:The structural formulas of N-vinyl pyrrolidone and N-cyanovinyl pyrrolidone are shown in Formula I and Formula II:
式I; Formula I;
式II。 Formula II.
具体的,所述亲锂纳米颗粒选自纳米银粉、纳米锡粉、纳米锌粉、纳米氧化银、纳米二氧化锡、纳米氧化锌中的至少一种。Specifically, the lithium-philic nanoparticles are selected from at least one of nano-silver powder, nano-tin powder, nano-zinc powder, nano-silver oxide, nano-tin dioxide, and nano-zinc oxide.
具体的,所述引发剂选自偶氮二异丁腈、过氧化邻苯二甲酰中的至少一种。Specifically, the initiator is selected from at least one of azobisisobutyronitrile and phthaloyl peroxide.
具体的,所述金属集流体为铜集流体、镍集流体中的一种。Specifically, the metal current collector is one of a copper current collector and a nickel current collector.
具体的,所述亲锂纳米颗粒选的粒径为50~100 nm,所述的亲锂纳米颗粒用量为所述浆料总质量的15~40%。Specifically, the particle size of the lithium-philic nanoparticles is 50-100 nm, and the amount of the lithium-philic nanoparticles is 15-40% of the total mass of the slurry.
具体的,所述引发剂用量为所述浆料总质量的0.08~0.20%。Specifically, the amount of the initiator is 0.08-0.20% of the total mass of the slurry.
具体的,所述N-乙烯基吡咯烷酮用量占所述浆料总质量的35~75%;所述N-氰乙烯基吡咯烷酮用量占所述浆料总质量的5~30%。Specifically, the amount of N-vinyl pyrrolidone accounts for 35-75% of the total mass of the slurry; the amount of N-cyanovinyl pyrrolidone accounts for 5-30% of the total mass of the slurry.
具体的,加热原位聚合的温度为60-120℃,加热原位聚合时间为1-5h。在该原位聚合时间下,可以确保聚合完全,同时避免聚合物长时间受热发生老化,采用本发明限定的原位聚合温度和原位聚合时间更利于得到应用效果优异的集流体。Specifically, the temperature of the in-situ polymerization is 60-120° C., and the in-situ polymerization time is 1-5 hours. Under this in-situ polymerization time, complete polymerization can be ensured, while preventing the polymer from aging due to long-term heating. The in-situ polymerization temperature and in-situ polymerization time defined in the present invention are more conducive to obtaining a current collector with excellent application effect.
具体的,将所述浆料均匀涂布在金属集流体表面所使用的涂布方法为刮刀涂布法或旋转涂布法。Specifically, the coating method used to uniformly coat the slurry on the surface of the metal current collector is a doctor blade coating method or a spin coating method.
更具体的,刮刀涂布法中采用的刮刀厚度为50μm;旋转涂布法中采用的转速为4000rpm,涂布时间为90s。More specifically, the blade thickness used in the blade coating method is 50 μm; the rotation speed used in the spin coating method is 4000 rpm, and the coating time is 90 s.
更具体的,浆料配制过程中,可以在手套箱内进行,保持温度为15-35℃。More specifically, the slurry preparation process can be carried out in a glove box and the temperature can be maintained at 15-35°C.
更具体的,配置浆料时的搅拌速度为200-600rpm,优选450rpm;搅拌时间为0.5-5h,优选2h。More specifically, the stirring speed during the preparation of the slurry is 200-600 rpm, preferably 450 rpm; the stirring time is 0.5-5 h, preferably 2 h.
本发明实施例中制备出的无负极锂金属电池用集流体进行性能测试时,是以磷酸铁锂电极为正电极组装无负极锂金属电池进行全电池测试,其中无负极锂金属电池的具体组成为:When the current collector for the negative electrode-free lithium metal battery prepared in the embodiment of the present invention is subjected to a performance test, a negative electrode-free lithium metal battery is assembled with a lithium iron phosphate electrode as a positive electrode for a full battery test, wherein the specific composition of the negative electrode-free lithium metal battery is:
以商用碳包覆的磷酸铁锂与导电炭黑(Super P)、碳纳米管(CNT)、聚偏氟乙烯按照93:2:2:3的重量比例混合后,加入N-甲基吡咯烷酮,均匀搅拌制成正极浆料。按照单面27mg/cm2的面密度进行涂布,100℃真空干燥12小时,然后碾压、裁切制成正极片;按照本发明专利提供的无负极锂金属电池用集流体的制备方法制备相应的负极极片。Commercial carbon-coated lithium iron phosphate is mixed with conductive carbon black (Super P), carbon nanotubes (CNT), and polyvinylidene fluoride in a weight ratio of 93:2:2:3, and N-methylpyrrolidone is added and stirred evenly to form a positive electrode slurry. Coating is performed according to a single-sided surface density of 27 mg/ cm2 , vacuum drying at 100°C for 12 hours, and then rolling and cutting are performed to form a positive electrode sheet; the corresponding negative electrode sheet is prepared according to the preparation method of the current collector for a negative electrode-free lithium metal battery provided by the patent of this invention.
将正、负极片以聚丙烯(PP)陶瓷隔膜隔开,其中,陶瓷隔膜朝向负极集流体的一侧涂覆陶瓷涂层(1μm勃姆石陶瓷涂层),卷绕成电芯,封装于铝塑膜中,100℃真空烘烤48h,注入含1.0mol/L LiPF6(六氟磷酸锂)和0.1mol/L LiODFB(二氟草酸硼酸锂)的碳酸二三氟乙醇酯(TFEC)/碳酸二乙酯(DEC)/氟代碳酸乙烯酯(FEC)电解液,其中PC/DEC/FEC体积比2:1:1,封口制成电池。将注液后电池在45℃下开路搁置48h,使电解液完全浸润。The positive and negative electrodes were separated by a polypropylene (PP) ceramic separator, where a ceramic coating (1 μm boehmite ceramic coating) was applied on the side of the ceramic separator facing the negative current collector, and then wound into a battery cell, packaged in an aluminum-plastic film, and vacuum-baked at 100°C for 48 hours. The electrolyte of trifluoroethanol carbonate (TFEC)/diethyl carbonate (DEC)/fluoroethylene carbonate (FEC) containing 1.0 mol/L LiPF 6 (lithium hexafluorophosphate) and 0.1 mol/L LiODFB (lithium difluorooxalate borate) was injected, where the volume ratio of PC/DEC/FEC was 2:1:1, and the battery was sealed. After the injection, the battery was placed in an open circuit at 45°C for 48 hours to allow the electrolyte to completely penetrate.
实施例1Example 1
一种无负极锂金属电池用集流体的制备:Preparation of a current collector for a negative electrode-free lithium metal battery:
1)氮气保护下,取1500 mg纳米银粉、7 mg偶氮二异丁腈、3000mg N-乙烯基吡咯烷酮和500 mg N-氰乙烯基吡咯烷酮,置于螺口瓶中,磁力搅拌450rpm,搅拌分散2.0h,形成灰黑色浆液,其中,纳米银粉的直径为70 nm。1) Under nitrogen protection, 1500 mg of nano-silver powder, 7 mg of azobisisobutyronitrile, 3000 mg of N-vinyl pyrrolidone and 500 mg of N-cyanovinyl pyrrolidone were placed in a screw-cap bottle and stirred with a magnetic stirrer at 450 rpm for 2.0 h to form a gray-black slurry in which the diameter of the nano-silver powder was 70 nm.
2)将步骤1)制备的浆料均匀涂布在金属集流体表面并于80℃下,热烘干聚合3.0h,即可得到改性的集流体。其中,金属集流体为铜集流体,浆料涂布方法为刮刀涂布法,刮刀涂布法中采用的刮刀厚度为50 μm。2) The slurry prepared in step 1) is evenly coated on the surface of the metal current collector and heat-dried and polymerized at 80°C for 3.0 hours to obtain a modified current collector. The metal current collector is a copper current collector, and the slurry coating method is a blade coating method. The blade thickness used in the blade coating method is 50 μm.
图1为本实施例中制备的无负极锂金属电池的库伦效率与循环稳定性图,其中,图1中■的曲线为本实施例制备的无负极锂金属电池在不同循环圈数下的放电比容量曲线,图1中□的曲线为本实施例制备的无负极锂金属电池在不同循环圈数下的库伦效率曲线。本实施例中所制备浆料均匀细腻,呈灰黑色;铜集流体表面改性涂层平整,聚合物基体与无机填料分布均匀;以磷酸铁锂电极为正电极组装无负极锂金属电池进行全电池测试,电池首圈放电比容量为151.33 mAh g-1,首圈库伦效率为94.00%;从图1可以看出,循环过程中库伦效率均接近100%,循环50圈后仍有73.96%的容量保持率;电池充电完成后铜集流体表面锂沉积形貌致密,无锂枝晶生成,且改性涂层在电池放电完成后仍能均匀附着在铜集流体的表面。FIG1 is a graph of the coulombic efficiency and cycle stability of the negative electrode-free lithium metal battery prepared in this embodiment, wherein the curve of ■ in FIG1 is the discharge specific capacity curve of the negative electrode-free lithium metal battery prepared in this embodiment at different cycle numbers, and the curve of □ in FIG1 is the coulombic efficiency curve of the negative electrode-free lithium metal battery prepared in this embodiment at different cycle numbers. The slurry prepared in this embodiment is uniform and fine, and is gray-black; the surface modified coating of the copper current collector is flat, and the polymer matrix and the inorganic filler are evenly distributed; the negative electrode-free lithium metal battery is assembled with the lithium iron phosphate electrode as the positive electrode for full battery testing, and the battery first cycle discharge specific capacity is 151.33 mAh g -1 , and the first cycle coulombic efficiency is 94.00%; it can be seen from FIG1 that the coulombic efficiency is close to 100% during the cycle, and there is still a capacity retention rate of 73.96% after 50 cycles; after the battery is charged, the lithium deposition morphology on the surface of the copper current collector is dense, no lithium dendrites are generated, and the modified coating can still be evenly attached to the surface of the copper current collector after the battery is discharged.
实施例2Example 2
一种无负极锂金属电池用集流体的制备:Preparation of a current collector for a negative electrode-free lithium metal battery:
1)氮气保护下,取1000 mg纳米锡粉、5 mg偶氮二异丁腈、3300mg N-乙烯基吡咯烷酮和700 mg N-氰乙烯基吡咯烷酮,置于螺口瓶中,磁力搅拌450rpm,搅拌分散2.0h,形成银灰色浆液;其中,纳米锡粉的直径为60 nm。1) Under nitrogen protection, 1000 mg of nano-tin powder, 5 mg of azobisisobutyronitrile, 3300 mg of N-vinyl pyrrolidone and 700 mg of N-cyanovinyl pyrrolidone were placed in a screw-capped bottle, and magnetically stirred at 450 rpm for 2.0 h to form a silver-grey slurry; the diameter of the nano-tin powder was 60 nm.
2)将步骤1)制备的浆料均匀涂布在金属集流体表面并于90℃下,热烘干聚合4.0h,即可得到改性的集流体。其中,金属集流体为铜集流体,浆料涂布方法为旋转涂布法,旋转涂布法中采用的转速为4000 rpm,涂布时间为90 s。2) The slurry prepared in step 1) is evenly coated on the surface of the metal current collector and heat-dried and polymerized at 90°C for 4.0 hours to obtain a modified current collector. The metal current collector is a copper current collector, and the slurry coating method is a spin coating method. The rotation speed used in the spin coating method is 4000 rpm and the coating time is 90 s.
图2为本实施例中制备的无负极锂金属电池的首圈容量-电压曲线,图2中向上趋势的曲线为充电时电池比容量-电压曲线,图2中向下趋势的曲线为放电时电池比容量-电压曲线。本实施例中所制备浆料均匀细腻,呈银灰色;铜集流体表面改性涂层平整,聚合物基体与无机填料分布均匀;以磷酸铁锂电极为正电极组装无负极锂金属电池进行全电池测试,从图2可以看出,电池首圈放电比容量为148.2 mAh g-1,首圈库伦效率为90.75%;循环过程中库伦效率均接近100%,循环50圈后仍有70.59%的容量保持率;电池充电完成后铜集流体表面锂沉积形貌致密,无锂枝晶生成,且改性涂层在电池放电完成后仍能均匀附着在铜集流体的表面。FIG2 is the first cycle capacity-voltage curve of the negative electrode-free lithium metal battery prepared in this embodiment. The upward trend curve in FIG2 is the battery specific capacity-voltage curve during charging, and the downward trend curve in FIG2 is the battery specific capacity-voltage curve during discharge. The slurry prepared in this embodiment is uniform and fine, and is silver-gray; the surface modified coating of the copper current collector is flat, and the polymer matrix and the inorganic filler are evenly distributed; the negative electrode-free lithium metal battery is assembled with the lithium iron phosphate electrode as the positive electrode for full battery testing. As can be seen from FIG2, the battery first cycle discharge specific capacity is 148.2 mAh g -1 , and the first cycle coulomb efficiency is 90.75%; the coulomb efficiency during the cycle is close to 100%, and there is still a capacity retention rate of 70.59% after 50 cycles; after the battery is charged, the lithium deposition morphology on the surface of the copper current collector is dense, no lithium dendrites are generated, and the modified coating can still be evenly attached to the surface of the copper current collector after the battery is discharged.
实施例3Example 3
一种无负极锂金属电池用集流体的制备:Preparation of a current collector for a negative electrode-free lithium metal battery:
1)氮气保护下,取1000 mg纳米氧化银、5 mg偶氮二异丁腈、3000mg N-乙烯基吡咯烷酮和1000 mg N-氰乙烯基吡咯烷酮,置于螺口瓶中,磁力搅拌450rpm,搅拌分散2.0h,形成银灰色浆液。其中,纳米氧化银的直径为70 nm。1) Under nitrogen protection, 1000 mg of nano silver oxide, 5 mg of azobisisobutyronitrile, 3000 mg of N-vinyl pyrrolidone and 1000 mg of N-cyanovinyl pyrrolidone were placed in a screw-mouth bottle, and stirred at 450 rpm for 2.0 h to form a silver-grey slurry. The diameter of the nano silver oxide was 70 nm.
2)将步骤1)制备的浆料均匀涂布在金属集流体表面并于90℃下,热烘干聚合4.0h,即可得到改性的集流体。其中,金属集流体为镍集流体,浆料涂布方法为旋转涂布法。旋转涂布法中采用的转速为4000 rpm,涂布时间为90 s。2) The slurry prepared in step 1) is evenly coated on the surface of the metal current collector and heat-dried and polymerized at 90°C for 4.0 hours to obtain a modified current collector. The metal current collector is a nickel current collector, and the slurry coating method is a spin coating method. The rotation speed used in the spin coating method is 4000 rpm and the coating time is 90 s.
图3为本实施例中制备的金属集流体改性用浆料的光学照片。本实施例中所制备浆料均匀细腻,呈灰黑色;镍集流体表面改性涂层平整,聚合物基体与无机填料分布均匀;以磷酸铁锂电极为对电极组装无负极锂金属电池进行全电池测试,电池首圈放电比容量为150.3 mAh g-1,首圈库伦效率为91.15%;循环过程中库伦效率均接近100%,循环50圈后仍有73.28%的容量保持率;电池充电完成后镍集流体表面锂沉积形貌致密,无锂枝晶生成,且改性涂层在电池放电完成后仍能均匀附着在镍集流体的表面。Figure 3 is an optical photograph of the slurry for metal current collector modification prepared in this embodiment. The slurry prepared in this embodiment is uniform and fine, and is gray-black in color; the modified coating on the surface of the nickel current collector is flat, and the polymer matrix and the inorganic filler are evenly distributed; the full battery test is performed by assembling a negative electrode-free lithium metal battery with a lithium iron phosphate electrode as the counter electrode, and the battery's first cycle discharge capacity is 150.3 mAh g -1 , and the first cycle coulomb efficiency is 91.15%; the coulomb efficiency is close to 100% during the cycle, and there is still a capacity retention rate of 73.28% after 50 cycles; after the battery is charged, the lithium deposition morphology on the surface of the nickel current collector is dense, no lithium dendrites are generated, and the modified coating can still be evenly attached to the surface of the nickel current collector after the battery is discharged.
实施例4Example 4
一种无负极锂金属电池用集流体的制备:Preparation of a current collector for a negative electrode-free lithium metal battery:
1)氮气保护下,取1200 mg纳米氧化锌、5 mg偶氮二异丁腈、3000mg N-乙烯基吡咯烷酮和800 mg N-氰乙烯基吡咯烷酮,置于螺口瓶中,磁力搅拌450rpm,搅拌分散2.0h,形成白色浆液。其中,纳米氧化锌的直径为60 nm。1) Under nitrogen protection, 1200 mg of nano zinc oxide, 5 mg of azobisisobutyronitrile, 3000 mg of N-vinyl pyrrolidone and 800 mg of N-cyanovinyl pyrrolidone were placed in a screw-mouth bottle, and stirred at 450 rpm for 2.0 h to form a white slurry. The diameter of the nano zinc oxide was 60 nm.
2)将步骤1)制备的浆料均匀涂布在金属集流体表面并于80℃下,热烘干聚合4.0h,即可得到改性的集流体。其中,金属集流体为镍集流体,浆料涂布方法为刮刀涂布法,刮刀涂布法中采用的刮刀厚度为50 μm。2) The slurry prepared in step 1) is evenly coated on the surface of the metal current collector and heat-dried and polymerized at 80°C for 4.0 hours to obtain a modified current collector. The metal current collector is a nickel current collector, and the slurry coating method is a blade coating method. The blade thickness used in the blade coating method is 50 μm.
图4为本实施例中制备的改性后金属集流体的扫描电子显微镜照片。本实施例中所制备浆料均匀细腻,呈白色;镍集流体表面改性涂层平整,聚合物基体与无机填料分布均匀;以磷酸铁锂电极为正电极组装无负极锂金属电池进行全电池测试,电池首圈放电比容量为146.7 mAh g-1,首圈库伦效率为88.54%;循环过程中库伦效率均接近100%,循环50圈后仍有69.36%的容量保持率;电池充电完成后镍集流体表面锂沉积形貌致密,无锂枝晶生成,且改性涂层在电池放电完成后仍能均匀附着在镍集流体的表面。Figure 4 is a scanning electron microscope photo of the modified metal current collector prepared in this embodiment. The slurry prepared in this embodiment is uniform and fine, and is white; the modified coating on the surface of the nickel current collector is flat, and the polymer matrix and the inorganic filler are evenly distributed; the full battery test is performed by assembling a negative electrode-free lithium metal battery with a lithium iron phosphate electrode as the positive electrode, and the battery first cycle discharge capacity is 146.7 mAh g -1 , and the first cycle coulomb efficiency is 88.54%; the coulomb efficiency is close to 100% during the cycle, and there is still a capacity retention rate of 69.36% after 50 cycles; after the battery is charged, the lithium deposition morphology on the surface of the nickel current collector is dense, no lithium dendrites are generated, and the modified coating can still be evenly attached to the surface of the nickel current collector after the battery is discharged.
实施例5Example 5
一种无负极锂金属电池用集流体的制备:Preparation of a current collector for a negative electrode-free lithium metal battery:
1)氮气保护下,取1000 mg纳米二氧化锡、5 mg偶氮二异丁腈、3500mg N-乙烯基吡咯烷酮和500 mg N-氰乙烯基吡咯烷酮,置于螺口瓶中,磁力搅拌450rpm,搅拌分散2.0h,形成灰白色浆液。其中,纳米二氧化锡的直径为80 nm。1) Under nitrogen protection, 1000 mg of nano-tin dioxide, 5 mg of azobisisobutyronitrile, 3500 mg of N-vinyl pyrrolidone and 500 mg of N-cyanovinyl pyrrolidone were placed in a screw-mouth bottle, and stirred at 450 rpm for 2.0 h to form an off-white slurry. The diameter of the nano-tin dioxide was 80 nm.
2)将步骤1)制备的浆料均匀涂布在金属集流体表面并于80℃下,热烘干聚合4.0h,即可得到改性的金属集流体。其中,金属集流体为铜集流体,浆料涂布方法为刮刀涂布法,刮刀涂布法中采用的刮刀厚度为50 μm。2) The slurry prepared in step 1) is evenly coated on the surface of the metal current collector and heat-dried and polymerized at 80°C for 4.0 hours to obtain a modified metal current collector. The metal current collector is a copper current collector, and the slurry coating method is a blade coating method. The blade thickness used in the blade coating method is 50 μm.
图5为本实施例中制备的无负极锂金属电池首次充电后负极侧金属锂沉积的扫描电子显微镜照片。本实施例中所制备浆料均匀细腻,呈灰白色;铜集流体表面改性涂层平整,聚合物基体与无机填料分布均匀;以磷酸铁锂电极为正电极组装无负极锂金属电池进行全电池测试,电池首圈放电比容量为149.78 mAh g-1,首圈库伦效率为90.14%;循环过程中库伦效率均接近100%,循环50圈后仍有73.35%的容量保持率;电池充电完成后铜集流体表面锂沉积形貌致密,无锂枝晶生成,且改性涂层在电池放电完成后仍能均匀附着在铜集流体的表面。Figure 5 is a scanning electron microscope photo of the metal lithium deposition on the negative electrode side of the negative electrode-free lithium metal battery prepared in this embodiment after the first charge. The slurry prepared in this embodiment is uniform and fine, and is grayish white; the modified coating on the surface of the copper current collector is flat, and the polymer matrix and the inorganic filler are evenly distributed; the negative electrode-free lithium metal battery is assembled with the lithium iron phosphate electrode as the positive electrode for full battery testing, and the battery first cycle discharge capacity is 149.78 mAh g -1 , and the first cycle coulomb efficiency is 90.14%; the coulomb efficiency is close to 100% during the cycle, and there is still a capacity retention rate of 73.35% after 50 cycles; after the battery is charged, the lithium deposition morphology on the surface of the copper current collector is dense, no lithium dendrites are generated, and the modified coating can still be evenly attached to the surface of the copper current collector after the battery is discharged.
实施例6Example 6
一种无负极锂金属电池用集流体的制备:Preparation of a current collector for a negative electrode-free lithium metal battery:
1)氮气保护下,取1000 mg纳米锌粉、5 mg偶氮二异丁腈、3600mg N-乙烯基吡咯烷酮和400 mg N-氰乙烯基吡咯烷酮,置于螺口瓶中,磁力搅拌450rpm,搅拌分散2.0h,形成灰白色浆液。其中,纳米锌粉的直径为70 nm。1) Under nitrogen protection, 1000 mg of nano zinc powder, 5 mg of azobisisobutyronitrile, 3600 mg of N-vinyl pyrrolidone and 400 mg of N-cyanovinyl pyrrolidone were placed in a screw-cap bottle, and stirred at 450 rpm for 2.0 h to form an off-white slurry. The diameter of the nano zinc powder was 70 nm.
2)将步骤1)制备的浆料均匀涂布在金属集流体表面并于70℃下,热烘干聚合5.0h,即可得到改性的集流体。其中,金属集流体为镍集流体,浆料涂布方法为旋转涂布法,旋转涂布法中采用的转速为4000 rpm,涂布时间为90 s。2) The slurry prepared in step 1) is evenly coated on the surface of the metal current collector and heat-dried and polymerized at 70°C for 5.0 hours to obtain a modified current collector. The metal current collector is a nickel current collector, and the slurry coating method is a spin coating method. The rotation speed used in the spin coating method is 4000 rpm and the coating time is 90 s.
图6为本实施例中制备的无负极锂金属电池首次放电后改性镍集流体表面的扫描电子显微镜照片。本实施例中所制备浆料均匀细腻,呈灰白色;镍集流体表面改性涂层平整,聚合物基体与无机填料分布均匀;以磷酸铁锂电极为正电极组装无负极锂金属电池进行全电池测试,电池首圈放电比容量为147.53 mAh g-1,首圈库伦效率为90.47%;循环过程中库伦效率均接近100%,循环50圈后仍有72.68%的容量保持率;电池充电完成后镍集流体表面锂沉积形貌致密,无锂枝晶生成,且改性涂层在电池放电完成后仍能均匀附着在镍集流体的表面。Figure 6 is a scanning electron microscope photo of the surface of the modified nickel current collector after the first discharge of the negative electrode-free lithium metal battery prepared in this embodiment. The slurry prepared in this embodiment is uniform and fine, and is off-white; the modified coating on the surface of the nickel current collector is flat, and the polymer matrix and the inorganic filler are evenly distributed; the negative electrode-free lithium metal battery is assembled with lithium iron phosphate electrode as the positive electrode for full battery testing, and the battery first cycle discharge capacity is 147.53 mAh g -1 , and the first cycle coulomb efficiency is 90.47%; the coulomb efficiency is close to 100% during the cycle, and there is still a capacity retention rate of 72.68% after 50 cycles; after the battery is charged, the lithium deposition morphology on the surface of the nickel current collector is dense, no lithium dendrites are generated, and the modified coating can still be evenly attached to the surface of the nickel current collector after the battery is discharged.
实施例7Example 7
一种无负极锂金属电池用集流体的制备:Preparation of a current collector for a negative electrode-free lithium metal battery:
1)氮气保护下,取850 mg纳米锌粉、10 mg偶氮二异丁腈、3800mg N-乙烯基吡咯烷酮和450 mg N-氰乙烯基吡咯烷酮,置于螺口瓶中,磁力搅拌450rpm,搅拌分散2.0h,形成灰黑色浆液,其中,纳米锌粉的直径为70 nm。1) Under nitrogen protection, 850 mg of nano zinc powder, 10 mg of azobisisobutyronitrile, 3800 mg of N-vinyl pyrrolidone and 450 mg of N-cyanovinyl pyrrolidone were placed in a screw-cap bottle and stirred with a magnetic stirrer at 450 rpm for 2.0 h to form a gray-black slurry, in which the diameter of the nano zinc powder was 70 nm.
2)氮气保护下,将步骤1)制备的浆料均匀涂布在金属集流体表面并于60℃下,热烘干聚合5.0h,即可得到改性的集流体。其中,金属集流体为铜集流体,浆料涂布方法为刮刀涂布法,刮刀涂布法中采用的刮刀厚度为50 μm。2) Under nitrogen protection, the slurry prepared in step 1) is evenly coated on the surface of the metal current collector and heat-dried and polymerized at 60°C for 5.0 hours to obtain a modified current collector. The metal current collector is a copper current collector, and the slurry coating method is a blade coating method. The blade thickness used in the blade coating method is 50 μm.
本实施例中所制备浆料均匀细腻,呈灰黑色;铜集流体表面改性涂层平整,聚合物基体与无机填料分布均匀;以磷酸铁锂电极为正电极组装无负极锂金属电池进行全电池测试,电池首圈放电比容量为150.63 mAh g-1,首圈库伦效率为93.00%;循环过程中库伦效率均接近100%,循环50圈后仍有73.06%的容量保持率;电池充电完成后铜集流体表面锂沉积形貌致密,无锂枝晶生成,且改性涂层在电池放电完成后仍能均匀附着在铜集流体的表面。The slurry prepared in this embodiment is uniform and fine, and is gray-black in color; the modified coating on the surface of the copper current collector is flat, and the polymer matrix and the inorganic filler are evenly distributed; a full-battery test is performed on a negative-electrode-free lithium metal battery assembled with a lithium iron phosphate electrode as the positive electrode, and the battery has a first-cycle discharge capacity of 150.63 mAh g -1 and a first-cycle coulomb efficiency of 93.00%; the coulomb efficiency is close to 100% during the cycle, and there is still a capacity retention rate of 73.06% after 50 cycles; after the battery is charged, the lithium deposition morphology on the surface of the copper current collector is dense, no lithium dendrites are generated, and the modified coating can still be evenly attached to the surface of the copper current collector after the battery is discharged.
实施例8Example 8
一种无负极锂金属电池用集流体的制备:Preparation of a current collector for a negative electrode-free lithium metal battery:
1)氮气保护下,取800 mg纳米二氧化锡、8 mg偶氮二异丁腈、2000mg N-乙烯基吡咯烷酮和1200 mg N-氰乙烯基吡咯烷酮,置于螺口瓶中,磁力搅拌450rpm,搅拌分散2.0h,形成灰白色浆液。其中,纳米二氧化锡的直径为80 nm。1) Under nitrogen protection, 800 mg of nano-tin dioxide, 8 mg of azobisisobutyronitrile, 2000 mg of N-vinyl pyrrolidone and 1200 mg of N-cyanovinyl pyrrolidone were placed in a screw-mouth bottle, and stirred at 450 rpm for 2.0 h to form an off-white slurry. The diameter of the nano-tin dioxide was 80 nm.
2)将步骤1)制备的浆料均匀涂布在金属集流体表面并于120℃下,热烘干聚合1.0h,即可得到改性的集流体。其中,金属集流体为镍集流体,浆料涂布方法为旋转涂布法,旋转涂布法中采用的转速为4000 rpm,涂布时间为90 s。2) The slurry prepared in step 1) is evenly coated on the surface of the metal current collector and heat-dried and polymerized at 120°C for 1.0h to obtain a modified current collector. The metal current collector is a nickel current collector, and the slurry coating method is a spin coating method. The rotation speed used in the spin coating method is 4000 rpm and the coating time is 90 s.
本实施例中所制备浆料均匀细腻,呈灰白色;镍集流体表面改性涂层平整,聚合物基体与无机填料分布均匀;以磷酸铁锂电极为正电极组装无负极锂金属电池进行全电池测试,电池首圈放电比容量为149.63 mAh g-1,首圈库伦效率为93.57%;循环过程中库伦效率均接近100%,循环50圈后仍有73.88%的容量保持率;电池充电完成后镍集流体表面锂沉积形貌致密,无锂枝晶生成,且改性涂层在电池放电完成后仍能均匀附着在镍集流体的表面。The slurry prepared in this embodiment is uniform and fine, and is off-white in color; the modified coating on the surface of the nickel current collector is flat, and the polymer matrix and the inorganic filler are evenly distributed; a full-battery test is performed on a negative-electrode-free lithium metal battery assembled with a lithium iron phosphate electrode as the positive electrode, and the battery has a first-cycle discharge capacity of 149.63 mAh g -1 and a first-cycle coulomb efficiency of 93.57%; the coulomb efficiency is close to 100% during the cycle, and there is still a capacity retention rate of 73.88% after 50 cycles; after the battery is charged, the lithium deposition morphology on the surface of the nickel current collector is dense, no lithium dendrites are generated, and the modified coating can still be evenly attached to the surface of the nickel current collector after the battery is discharged.
实施例9Example 9
一种无负极锂金属电池用集流体的制备:Preparation of a current collector for a negative electrode-free lithium metal battery:
1)氮气保护下,取2000 mg纳米银粉、5 mg偶氮二异丁腈、2000mg N-乙烯基吡咯烷酮和1500 mg N-氰乙烯基吡咯烷酮,置于螺口瓶中,磁力搅拌450rpm,搅拌分散2.0h,形成白色浆液。其中,纳米银粉的直径为60 nm。1) Under nitrogen protection, 2000 mg of nano silver powder, 5 mg of azobisisobutyronitrile, 2000 mg of N-vinyl pyrrolidone and 1500 mg of N-cyanovinyl pyrrolidone were placed in a screw-mouth bottle, and stirred at 450 rpm for 2.0 h to form a white slurry. The diameter of the nano silver powder was 60 nm.
2)将步骤1)制备的浆料均匀涂布在金属集流体表面并于80℃下,热烘干聚合4.0h,即可得到改性的集流体。其中,金属集流体为镍集流体,浆料涂布方法为刮刀涂布法,刮刀涂布法中采用的刮刀厚度为50 μm。2) The slurry prepared in step 1) is evenly coated on the surface of the metal current collector and heat-dried and polymerized at 80°C for 4.0 hours to obtain a modified current collector. The metal current collector is a nickel current collector, and the slurry coating method is a blade coating method. The blade thickness used in the blade coating method is 50 μm.
本实施例中所制备浆料均匀细腻,呈白色;镍集流体表面改性涂层平整,聚合物基体与无机填料分布均匀;以磷酸铁锂电极为正电极组装无负极锂金属电池进行全电池测试,电池首圈放电比容量为150.2 mAh g-1,首圈库伦效率为92.65%;循环过程中库伦效率均接近100%,循环50圈后仍有73.22%的容量保持率;电池充电完成后镍集流体表面锂沉积形貌致密,无锂枝晶生成,且改性涂层在电池放电完成后仍能均匀附着在镍集流体的表面。The slurry prepared in this embodiment is uniform and fine, and is white in color; the modified coating on the surface of the nickel current collector is flat, and the polymer matrix and the inorganic filler are evenly distributed; a full-battery test is performed on a negative-electrode-free lithium metal battery assembled with a lithium iron phosphate electrode as the positive electrode, and the battery has a first-cycle discharge capacity of 150.2 mAh g -1 and a first-cycle coulomb efficiency of 92.65%; the coulomb efficiency is close to 100% during the cycle, and there is still a capacity retention rate of 73.22% after 50 cycles; after the battery is charged, the lithium deposition morphology on the surface of the nickel current collector is dense, no lithium dendrites are generated, and the modified coating can still be evenly attached to the surface of the nickel current collector after the battery is discharged.
对比例1Comparative Example 1
采用实施例1相同的方法制备集流体,不同之处在于:不加入N-氰乙烯基吡咯烷酮,直接加入4000mg N-乙烯基吡咯烷酮。The current collector was prepared in the same manner as in Example 1, except that 4000 mg of N-vinyl pyrrolidone was directly added instead of N-cyanovinyl pyrrolidone.
本对比例1以磷酸铁锂电极为正电极组装无负极锂金属电池进行全电池测试,电池首圈放电比容量为115.25 mAh g-1,首圈库伦效率为87.00%;循环过程中库伦效率约为91%,循环50圈后有52.33%的容量保持率。In this comparative example 1, a negative electrode-free lithium metal battery was assembled with lithium iron phosphate electrode as the positive electrode for full battery testing. The battery had a first-cycle discharge capacity of 115.25 mAh g -1 and a first-cycle coulomb efficiency of 87.00%. The coulomb efficiency during the cycle was about 91%, and after 50 cycles, the capacity retention rate was 52.33%.
从对比例1和实施例1的数据比对可以看出,如果浆料中不加入N-氰乙烯基吡咯烷酮,制备的集流体应用到电池中时,电池性能下降,因为在原位聚合过程中,N-乙烯基吡咯烷酮和N-氰乙烯基吡咯烷酮即作为无机亲锂纳米颗粒分散剂,又作为粘结剂,当单一使用N-乙烯基吡咯烷酮时,其发生聚合度过高,导致所形成的聚合物与金属集流体的粘结性能发生下降导致的;而当引入适量的含有氰基强吸电子基团的氰乙烯基吡咯烷酮时,可以起到调控原位聚合度的作用,同时还起到增强聚合物与集流体粘结性能的作用。From the comparison of the data of Comparative Example 1 and Example 1, it can be seen that if N-cyanovinyl pyrrolidone is not added to the slurry, the battery performance will decrease when the prepared current collector is applied to the battery. This is because in the in-situ polymerization process, N-vinyl pyrrolidone and N-cyanovinyl pyrrolidone act as both inorganic lithium-philic nanoparticle dispersants and binders. When N-vinyl pyrrolidone is used alone, its polymerization degree is too high, resulting in a decrease in the bonding performance between the formed polymer and the metal current collector. However, when an appropriate amount of cyanovinyl pyrrolidone containing a cyano strong electron-withdrawing group is introduced, it can play a role in regulating the in-situ polymerization degree and at the same time enhance the bonding performance between the polymer and the current collector.
对比例2Comparative Example 2
采用实施例1相同的方法制备集流体,不同之处在于:增大N-氰乙烯基吡咯烷酮的加入量比例,即步骤1)为:取1500 mg纳米银粉、7 mg偶氮二异丁腈、1800mg N-乙烯基吡咯烷酮和1700 mg N-氰乙烯基吡咯烷酮,置于螺口瓶中,磁力搅拌450rpm,搅拌分散2.0h,形成灰黑色浆液,其中,纳米银粉的直径为70 nm。步骤2)与实施例1相同。The current collector was prepared by the same method as in Example 1, except that the amount of N-cyanovinylpyrrolidone added was increased, i.e., step 1) was: 1500 mg of nano silver powder, 7 mg of azobisisobutyronitrile, 1800 mg of N-vinylpyrrolidone and 1700 mg of N-cyanovinylpyrrolidone were placed in a screw-mouth bottle, magnetically stirred at 450 rpm, stirred and dispersed for 2.0 h to form a gray-black slurry, wherein the diameter of the nano silver powder was 70 nm. Step 2) was the same as in Example 1.
本对比例2以磷酸铁锂电极为正电极组装无负极锂金属电池进行全电池测试,电池首圈放电比容量为118.98mAh g-1,首圈库伦效率为86.00%;循环过程中库伦效率约为93%,循环50圈后有48.47%的容量保持率。In this comparative example 2, a negative electrode-free lithium metal battery was assembled with lithium iron phosphate electrode as the positive electrode for full battery testing. The battery had a first-cycle discharge capacity of 118.98 mAh g -1 and a first-cycle coulomb efficiency of 86.00%. The coulomb efficiency during the cycle was about 93%, and the capacity retention rate was 48.47% after 50 cycles.
从对比例2和实施例1的数据比对可以看出,如果浆料中N-氰乙烯基吡咯烷酮的加入量过多,也会导致电池性能下降,因为N-氰乙烯基吡咯烷酮的用量过多,因为N-氰乙烯基吡咯烷酮的结构限制,化合物聚合物过低,不能完全将无机亲电纳米颗粒完全包覆粘结于金属集流体上,从而导致电池性能下降。From the comparison of the data of Comparative Example 2 and Example 1, it can be seen that if too much N-cyanovinyl pyrrolidone is added to the slurry, the battery performance will also be reduced. Because the amount of N-cyanovinyl pyrrolidone is too much, due to the structural limitations of N-cyanovinyl pyrrolidone, the compound polymer is too low and the inorganic electrophilic nanoparticles cannot be completely coated and bonded to the metal current collector, resulting in a reduction in battery performance.
对比例3Comparative Example 3
一种无负极锂金属电池用集流体的制备:Preparation of a current collector for a negative electrode-free lithium metal battery:
1)聚合物的制备1) Preparation of polymer
3000 mg N-乙烯基吡咯烷酮、500 mg N-氰乙烯基吡咯烷酮、7 mg偶氮二异丁腈在80℃下进行聚合反应,聚合反应时间为3.0h,得到聚合体。3000 mg of N-vinyl pyrrolidone, 500 mg of N-cyanovinyl pyrrolidone and 7 mg of azobisisobutyronitrile were polymerized at 80° C. The polymerization time was 3.0 h to obtain a polymer.
2)浆料的配制2) Preparation of slurry
将聚合体溶解在N-甲基吡咯烷酮中,并加入1500 mg纳米银粉,分散均匀得到浆料。The polymer was dissolved in N-methylpyrrolidone, and 1500 mg of nano silver powder was added and dispersed evenly to obtain a slurry.
3)集流体的制备3) Preparation of current collector
将浆料均匀涂布到铜集流体表面,然后烘干,得到集流体。The slurry is evenly coated on the surface of the copper current collector and then dried to obtain the current collector.
本对比例4以磷酸铁锂电极为正电极组装无负极锂金属电池进行全电池测试,电池首圈放电比容量为140.02mAh g-1,首圈库伦效率为89.00%;循环过程中库伦效率约为96%,循环50圈后有63.54%的容量保持率。In this comparative example 4, a negative electrode-free lithium metal battery was assembled with lithium iron phosphate electrode as the positive electrode for full battery testing. The battery had a first-cycle discharge capacity of 140.02 mAh g -1 and a first-cycle coulomb efficiency of 89.00%. The coulomb efficiency during the cycle was about 96%, and after 50 cycles, the capacity retention rate was 63.54%.
从对比例3和实施例1的数据比对可以看出:实施例1中采用本发明的原位聚合方法制备的集流体,在电池中的应用效果更好,因为采用原位聚合的方式,生成的聚合物更均一,从而可以提高电池的一致性,采用本对比例3的这种传统方法,容易存在聚合物和亲锂纳米颗粒之间不均匀的问题,从而影响在电池中的应用效果,而且制备方法繁琐,重复性差。From the comparison of the data of Comparative Example 3 and Example 1, it can be seen that the current collector prepared by the in-situ polymerization method of the present invention in Example 1 has a better application effect in the battery, because the polymer generated by the in-situ polymerization method is more uniform, thereby improving the consistency of the battery. The traditional method of Comparative Example 3 is prone to the problem of unevenness between the polymer and the lithium-philic nanoparticles, thereby affecting the application effect in the battery, and the preparation method is cumbersome and has poor repeatability.
以上所述实施例的各技术特征可以进行任意的组合,为使描述简洁,未对上述实施例中的各个技术特征所有可能的组合穷举,然而,只要这些技术特征的组合不存在矛盾,都应当认为是本说明书记载的范围。The technical features of the above-described embodiments may be arbitrarily combined. To make the description concise, not all possible combinations of the technical features in the above-described embodiments are exhaustively listed. However, as long as there is no contradiction in the combination of these technical features, they should be considered to be within the scope of this specification.
对于本领域的普通技术人员来说,在不脱离本发明构思的前提下,还可以做出若干变形和改进,这些都属于本发明的保护范围,本发明的保护范围以所附权利要求为准。For those skilled in the art, several modifications and improvements may be made without departing from the concept of the present invention, all of which belong to the protection scope of the present invention. The protection scope of the present invention shall be based on the attached claims.
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