CN116111183A - Preparation method of solid ceramic electrolyte membrane applied to all-solid lithium battery - Google Patents
Preparation method of solid ceramic electrolyte membrane applied to all-solid lithium battery Download PDFInfo
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- CN116111183A CN116111183A CN202310217764.5A CN202310217764A CN116111183A CN 116111183 A CN116111183 A CN 116111183A CN 202310217764 A CN202310217764 A CN 202310217764A CN 116111183 A CN116111183 A CN 116111183A
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- 239000007787 solid Substances 0.000 title claims abstract description 36
- 239000012528 membrane Substances 0.000 title claims abstract description 34
- 229910021525 ceramic electrolyte Inorganic materials 0.000 title claims abstract description 30
- WHXSMMKQMYFTQS-UHFFFAOYSA-N Lithium Chemical compound [Li] WHXSMMKQMYFTQS-UHFFFAOYSA-N 0.000 title claims abstract description 27
- 229910052744 lithium Inorganic materials 0.000 title claims abstract description 27
- 238000002360 preparation method Methods 0.000 title claims description 7
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 30
- 239000000843 powder Substances 0.000 claims abstract description 28
- 238000000034 method Methods 0.000 claims abstract description 25
- 239000003792 electrolyte Substances 0.000 claims abstract description 22
- 239000002002 slurry Substances 0.000 claims abstract description 19
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- 238000007873 sieving Methods 0.000 claims abstract 2
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- 238000010438 heat treatment Methods 0.000 claims description 11
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- 229910000664 lithium aluminum titanium phosphates (LATP) Inorganic materials 0.000 claims description 9
- NIQCNGHVCWTJSM-UHFFFAOYSA-N Dimethyl phthalate Chemical compound COC(=O)C1=CC=CC=C1C(=O)OC NIQCNGHVCWTJSM-UHFFFAOYSA-N 0.000 claims description 8
- HBBGRARXTFLTSG-UHFFFAOYSA-N Lithium ion Chemical compound [Li+] HBBGRARXTFLTSG-UHFFFAOYSA-N 0.000 claims description 8
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- DOIRQSBPFJWKBE-UHFFFAOYSA-N dibutyl phthalate Chemical compound CCCCOC(=O)C1=CC=CC=C1C(=O)OCCCC DOIRQSBPFJWKBE-UHFFFAOYSA-N 0.000 claims description 4
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- GVGUFUZHNYFZLC-UHFFFAOYSA-N dodecyl benzenesulfonate;sodium Chemical compound [Na].CCCCCCCCCCCCOS(=O)(=O)C1=CC=CC=C1 GVGUFUZHNYFZLC-UHFFFAOYSA-N 0.000 claims description 2
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- 229940080264 sodium dodecylbenzenesulfonate Drugs 0.000 claims description 2
- GCLGEJMYGQKIIW-UHFFFAOYSA-H sodium hexametaphosphate Chemical compound [Na]OP1(=O)OP(=O)(O[Na])OP(=O)(O[Na])OP(=O)(O[Na])OP(=O)(O[Na])OP(=O)(O[Na])O1 GCLGEJMYGQKIIW-UHFFFAOYSA-H 0.000 claims description 2
- 235000019982 sodium hexametaphosphate Nutrition 0.000 claims description 2
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- 239000001577 tetrasodium phosphonato phosphate Substances 0.000 claims description 2
- STCOOQWBFONSKY-UHFFFAOYSA-N tributyl phosphate Chemical compound CCCCOP(=O)(OCCCC)OCCCC STCOOQWBFONSKY-UHFFFAOYSA-N 0.000 claims description 2
- DQWPFSLDHJDLRL-UHFFFAOYSA-N triethyl phosphate Chemical compound CCOP(=O)(OCC)OCC DQWPFSLDHJDLRL-UHFFFAOYSA-N 0.000 claims description 2
- ZIBGPFATKBEMQZ-UHFFFAOYSA-N triethylene glycol Chemical compound OCCOCCOCCO ZIBGPFATKBEMQZ-UHFFFAOYSA-N 0.000 claims description 2
- LYCAIKOWRPUZTN-UHFFFAOYSA-N Ethylene glycol Chemical compound OCCO LYCAIKOWRPUZTN-UHFFFAOYSA-N 0.000 claims 2
- DUIOKRXOKLLURE-UHFFFAOYSA-N 2-octylphenol Chemical compound CCCCCCCCC1=CC=CC=C1O DUIOKRXOKLLURE-UHFFFAOYSA-N 0.000 claims 1
- 229920000298 Cellophane Polymers 0.000 claims 1
- LZZYPRNAOMGNLH-UHFFFAOYSA-M Cetrimonium bromide Chemical compound [Br-].CCCCCCCCCCCCCCCC[N+](C)(C)C LZZYPRNAOMGNLH-UHFFFAOYSA-M 0.000 claims 1
- OVXRPXGVKBHGQO-UHFFFAOYSA-N abietic acid methyl ester Natural products C1CC(C(C)C)=CC2=CCC3C(C(=O)OC)(C)CCCC3(C)C21 OVXRPXGVKBHGQO-UHFFFAOYSA-N 0.000 claims 1
- 235000015895 biscuits Nutrition 0.000 claims 1
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- OVXRPXGVKBHGQO-UYWIDEMCSA-N methyl (1r,4ar,4br,10ar)-1,4a-dimethyl-7-propan-2-yl-2,3,4,4b,5,6,10,10a-octahydrophenanthrene-1-carboxylate Chemical compound C1CC(C(C)C)=CC2=CC[C@H]3[C@@](C(=O)OC)(C)CCC[C@]3(C)[C@H]21 OVXRPXGVKBHGQO-UYWIDEMCSA-N 0.000 claims 1
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- RSWGJHLUYNHPMX-UHFFFAOYSA-N Abietic-Saeure Natural products C12CCC(C(C)C)=CC2=CCC2C1(C)CCCC2(C)C(O)=O RSWGJHLUYNHPMX-UHFFFAOYSA-N 0.000 description 1
- FVXHSJCDRRWIRE-UHFFFAOYSA-H P(=O)([O-])([O-])[O-].[Ge+2].[Al+3].[Li+].P(=O)([O-])([O-])[O-] Chemical compound P(=O)([O-])([O-])[O-].[Ge+2].[Al+3].[Li+].P(=O)([O-])([O-])[O-] FVXHSJCDRRWIRE-UHFFFAOYSA-H 0.000 description 1
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- 229910052782 aluminium Inorganic materials 0.000 description 1
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- SWLVFNYSXGMGBS-UHFFFAOYSA-N ammonium bromide Chemical compound [NH4+].[Br-] SWLVFNYSXGMGBS-UHFFFAOYSA-N 0.000 description 1
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M10/00—Secondary cells; Manufacture thereof
- H01M10/05—Accumulators with non-aqueous electrolyte
- H01M10/056—Accumulators with non-aqueous electrolyte characterised by the materials used as electrolytes, e.g. mixed inorganic/organic electrolytes
- H01M10/0561—Accumulators with non-aqueous electrolyte characterised by the materials used as electrolytes, e.g. mixed inorganic/organic electrolytes the electrolyte being constituted of inorganic materials only
- H01M10/0562—Solid materials
-
- 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
-
- 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
-
- 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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- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- General Chemical & Material Sciences (AREA)
- General Physics & Mathematics (AREA)
- Condensed Matter Physics & Semiconductors (AREA)
- Inorganic Chemistry (AREA)
- Physics & Mathematics (AREA)
- Compositions Of Oxide Ceramics (AREA)
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- Conductive Materials (AREA)
Abstract
本发明涉及电池技术领域,具体涉及一种应用于全固态锂电池的固态陶瓷电解质膜的制备方法,其包括如下步骤:将制备好的电解质粉体进行球磨过筛,然后依次加入分散剂,增塑剂,粘结剂等进行球磨以获得均匀的流延浆料;将其进行流延,控制刮刀高度在5μm‑1mm,得到流延膜;将室温干燥后的流延膜进行叠层热压,得到素胚;将素胚置于马弗炉分段升温烧结,最终得到致密陶瓷电解质膜。本发明采用的水基流延成型工艺使用水作为唯一溶剂,安全、绿色、环保,浆料的稳定性好,制得的陶瓷电解质膜具有优异的烧结能力、离子电导率和力学性能;工艺简单,且生产成本较低,容易实现大规模生产,可用于固态锂电池、燃料电池技术等领域。
The invention relates to the field of battery technology, in particular to a method for preparing a solid ceramic electrolyte membrane applied to an all-solid lithium battery, which comprises the following steps: ball milling and sieving the prepared electrolyte powder, and then sequentially adding a dispersant to increase the Plasticizers, binders, etc. are ball milled to obtain a uniform cast slurry; cast it, and control the height of the scraper at 5μm-1mm to obtain a cast film; the cast film dried at room temperature is laminated and hot-pressed , to obtain a plain embryo; the plain embryo is placed in a muffle furnace and sintered in stages to obtain a dense ceramic electrolyte membrane. The water-based tape casting process adopted in the present invention uses water as the only solvent, which is safe, green, and environmentally friendly, and the stability of the slurry is good. The prepared ceramic electrolyte membrane has excellent sintering ability, ion conductivity and mechanical properties; the process is simple , and the production cost is low, it is easy to realize large-scale production, and can be used in solid-state lithium battery, fuel cell technology and other fields.
Description
技术领域technical field
本发明涉及燃料电池技术领域,具体涉及一种应用于全固态锂电池的固态陶瓷电解质膜的制备方法。The invention relates to the technical field of fuel cells, in particular to a method for preparing a solid ceramic electrolyte membrane applied to an all-solid lithium battery.
背景技术Background technique
近年来,由于电动汽车的发展,人类生活对大容量储能的需求与日俱增,关于锂电池的研究再次引发热潮。安全性高、功率高、容量大以及循环寿命长的二次锂电池成为锂电池发展的新方向。经过多年发展,锂离子电池的输出电压和能量密度明显高于其它类型的电池。锂电池除了要满足最基本的长续航能力和大功率充放电的需求外,电池的安全性也尤为重要。目前商用的锂离子电池由于存在有机电解液易燃、容易产生锂枝晶等问题,一旦电池发生短路,其内部会放出大量的热,从而使有机电解液燃烧并引发严重的安全事故。为了提升锂电池的安全性并进一步拓展其应用场景,迫切需要开发具有良好安全性、高倍率性能、长循环寿命的锂电池。基于固态电解质的全固态锂电池有望解决传统液态锂离子电池存在的安全性问题。与传统液态锂离子电池相比,全固态电池最突出的优点是高安全性和高能量密度。因此,固态电解质成为了科研人员研究锂离子电池的首选目标。In recent years, due to the development of electric vehicles, the demand for large-capacity energy storage in human life is increasing day by day, and the research on lithium batteries has once again sparked an upsurge. Secondary lithium batteries with high safety, high power, large capacity and long cycle life have become a new direction for the development of lithium batteries. After years of development, the output voltage and energy density of lithium-ion batteries are significantly higher than other types of batteries. In addition to meeting the basic needs of long battery life and high-power charging and discharging, lithium batteries also have to be safe. Due to the flammability of the organic electrolyte and the easy generation of lithium dendrites in the current commercial lithium-ion batteries, once the battery is short-circuited, a large amount of heat will be released inside, which will cause the organic electrolyte to burn and cause serious safety accidents. In order to improve the safety of lithium batteries and further expand their application scenarios, it is urgent to develop lithium batteries with good safety, high rate performance, and long cycle life. All-solid-state lithium batteries based on solid-state electrolytes are expected to solve the safety problems of traditional liquid lithium-ion batteries. Compared with traditional liquid lithium-ion batteries, the most prominent advantages of all-solid-state batteries are high safety and high energy density. Therefore, solid-state electrolytes have become the first choice for researchers to study lithium-ion batteries.
NASICON型锂离子电解质,结构简式为LiA2(PO4)3,其中A为Ti4+、Zr4+、Ge4+、Hf4+、Sn4 +等四价阳离子,其骨架结构是由AO6八面体与PO4四面体共同形成,每个AO6八面体与6个PO4四面体相连接,每个PO4四面体与4个AO6八面体相连接,这些多面体通过相互接触的顶角氧原子相连,组成三维交错的骨架结构,形成利于Li+传输的离子传输通道,在不改变晶相结构的前提下使用低价的阳离子(如Al、Ga、In、Sc、Y、La、Cr、Fe、Zn、Ca等)取代部分的A4+,一方面可以改变离子传输通道的大小使其与Li+半径大小匹配,另一方面由于电荷平衡可以引入更多可迁移的Li+,从而在两方面提高材料的离子电导率。在这些材料中,磷酸钛铝锂(LATP)、磷酸锆铝锂(LAZP)和磷酸锗铝锂(LAGP)的性能最为突出。NASICON type lithium ion electrolyte, the simplified structure is LiA 2 (PO 4 ) 3 , where A is tetravalent cations such as Ti 4+ , Zr 4+ , Ge 4+ , Hf 4+ , Sn 4+ , and its skeleton structure is composed of AO 6 octahedron and PO 4 tetrahedron are jointly formed, each AO 6 octahedron is connected with 6 PO 4 tetrahedrons, each PO 4 tetrahedron is connected with 4 AO 6 octahedrons, and these polyhedrons are connected by mutual contact The oxygen atoms at the top corners are connected to form a three-dimensional staggered skeleton structure, forming an ion transport channel that is conducive to Li + transport, and using low-priced cations (such as Al, Ga, In, Sc, Y, La) without changing the crystal phase structure. , Cr, Fe, Zn, Ca, etc.) to replace part of A 4+ , on the one hand, the size of the ion transport channel can be changed to match the size of the Li + radius, and on the other hand, more mobile Li + can be introduced due to the charge balance , thereby improving the ionic conductivity of the material in two ways. Among these materials, lithium aluminum titanium phosphate (LATP), lithium aluminum zirconium phosphate (LAZP) and lithium aluminum germanium phosphate (LAGP) have the most outstanding performance.
目前,陶瓷电解质材料常见的成型方法有等离子喷涂法、溅射法、冷热压法、流延法等,其中流延法因适用于商业化大规模生产而被广泛应用。流延工艺包括水基和非水基流延两种。非水基流延制备的膜片结构均匀,柔韧性好,已在工业生产中应用多年。但是,非水基流延过程需使用大量有毒的有机物作为溶剂,生产成本高,排放后造成环境污染,有害人体健康。与此相比,水基流延采用水作为唯一溶剂,成本低,无污染,便于工业化生产。因此,研究以水作为溶剂代替有机溶剂的流延技术已经成为未来的趋势。At present, the common forming methods of ceramic electrolyte materials include plasma spraying method, sputtering method, hot and cold pressing method, tape casting method, etc. Among them, tape casting method is widely used because it is suitable for commercial mass production. The tape casting process includes water-based and non-water-based casting. The membrane prepared by non-water-based casting has uniform structure and good flexibility, and has been used in industrial production for many years. However, the non-water-based casting process needs to use a large amount of toxic organic substances as solvents, which has high production costs, causes environmental pollution after discharge, and is harmful to human health. Compared with this, water-based casting uses water as the only solvent, which has low cost, no pollution, and is convenient for industrial production. Therefore, it has become a future trend to study the casting technology using water as a solvent instead of organic solvents.
发明内容Contents of the invention
为了解决现有的有机流延浆料不环保、高成本问题,本发明公开了一种应用于全固态锂电池的固态陶瓷电解质膜的制备方法。In order to solve the problems of non-environmental protection and high cost of the existing organic casting slurry, the invention discloses a preparation method of a solid ceramic electrolyte membrane applied to an all-solid lithium battery.
为了达到上述技术效果,本发明是通过以下技术方案实现的:一种应用于全固态锂电池的固态陶瓷电解质膜的制备方法,其特征在于,包括以下步骤:In order to achieve the above technical effects, the present invention is achieved through the following technical solutions: a method for preparing a solid ceramic electrolyte membrane applied to an all-solid lithium battery, characterized in that it comprises the following steps:
Step1:制备水基流延浆料;Step1: Prepare water-based casting slurry;
Step2:流延;Step2: casting;
Step3:热压;Step3: hot pressing;
Step4:烧结。Step4: Sintering.
进一步的,所述Step1中,在一定量的电解质粉体中加入适量去离子水混合均匀,加入预先配置好的分散剂后进行一次球磨;加入增塑剂进行二次球磨;加入粘结剂的水溶液进行三次球磨;球磨后的浆料在20~80kpa进行真空脱泡5~15min,制备水基流延浆料;Further, in the Step1, add an appropriate amount of deionized water to a certain amount of electrolyte powder and mix evenly, add a pre-configured dispersant and perform a ball mill; add a plasticizer for a second ball mill; add a binder The aqueous solution is ball-milled three times; the ball-milled slurry is subjected to vacuum degassing at 20-80kpa for 5-15 minutes to prepare a water-based casting slurry;
所述Step2中,将制备好的电解质浆料进行过筛以去除杂质或大颗粒,然后使用自动涂布机在高温玻璃纸上以8~15cm/min的速度进行流延,其中刮刀高度为5μm~1mm,制备电解质流延膜;In the Step2, the prepared electrolyte slurry is sieved to remove impurities or large particles, and then cast on high-temperature glassine paper at a speed of 8-15 cm/min using an automatic coating machine, wherein the height of the scraper is 5 μm- 1mm, to prepare electrolyte casting membrane;
所述Step3中,将经室温干燥24h的流延裁剪成所需尺寸并剥离下来,根据所需厚度以不同的层数进行叠层,然后在60~120℃热压5~30min,制备陶瓷素胚;In Step 3, cut the tape that has been dried at room temperature for 24 hours into the required size and peel it off, laminate with different layers according to the required thickness, and then hot press at 60-120°C for 5-30 minutes to prepare ceramic elements Embryo;
所述Step4中,所述陶瓷素坯置于马弗炉中加热和保温的具体过程按照1~5℃/min的升温速率升温至300~600℃、保温1~12h,再以1~5℃/min的升温速率升温至700~1200℃、保温1~12h。In the Step4, the specific process of placing the ceramic green body in a muffle furnace for heating and heat preservation is to raise the temperature to 300-600°C at a heating rate of 1-5°C/min, keep it warm for 1-12 hours, and then heat it up at a temperature of 1-5°C. Raise the temperature to 700~1200℃ at a heating rate of /min, and keep it warm for 1~12h.
进一步的,所述Step1中,以电解质粉体的重量为基准,电解质粉体(固含量)的质量百分含量为30%~60%,溶剂的含量为30%~45%,分散剂的含量为0.8%~2%,粘结剂的含量为4%~8%,增塑剂的含量为3%~10%,脱泡剂的含量为0.3%~1%。Further, in the Step1, based on the weight of the electrolyte powder, the mass percentage of the electrolyte powder (solid content) is 30% to 60%, the content of the solvent is 30% to 45%, and the content of the dispersant The content of the binder is 4% to 8%, the content of the plasticizer is 3% to 10%, and the content of the defoaming agent is 0.3% to 1%.
进一步的,所述电解质粉体为NASICON型锂离子电解质,其结构简式为LiA2(PO4)3,其中A包括但不限于Ti4+、Zr4+、Ge4+、Hf4+、Sn4+其中一种四价阳离子,所述电解质粉体采用LATP粉末材料、LAZP粉末材料、LAGP粉末材料其中一种或多种;Further, the electrolyte powder is a NASICON type lithium ion electrolyte, and its simplified structure is LiA 2 (PO 4 ) 3 , where A includes but not limited to Ti 4+ , Zr 4+ , Ge 4+ , Hf 4+ , One of the tetravalent cations of Sn 4+ , the electrolyte powder adopts one or more of LATP powder materials, LAZP powder materials, and LAGP powder materials;
所述LATP粉末材料为Li1+xAlxTi2-x(PO4)3(其中x在0.1~0.5之间)中的一种或多种;The LATP powder material is one or more of Li 1+x Al x Ti 2-x (PO 4 ) 3 (where x is between 0.1 and 0.5);
所述LAZP粉末材料为Li1+xAlxZr2-x(PO4)3(其中x在0.1~0.5之间)中的一种或多种;The LAZP powder material is one or more of Li 1+x Al x Zr 2-x (PO 4 ) 3 (where x is between 0.1 and 0.5);
所述LAGP粉末材料为Li1+xAlxGe2-x(PO4)3(其中x在0.1~0.5之间)中的一种或多种。The LAGP powder material is one or more of Li 1+x Al x Ge 2-x (PO 4 ) 3 (where x is between 0.1 and 0.5).
进一步的,所述分散剂为三乙醇胺、聚丙烯酸钠、磷酸三乙酯、十二烷基苯磺酸钠、十二烷基硫酸钠、六偏磷酸钠、聚丙烯酸、十六烷基三甲基溴化铵、聚乙二醇、聚丙烯酸钾、辛基苯酚聚氧乙烯醚或磺酸盐氟分散剂中的一种或者多种。Further, the dispersant is triethanolamine, sodium polyacrylate, triethyl phosphate, sodium dodecylbenzenesulfonate, sodium dodecyl sulfate, sodium hexametaphosphate, polyacrylic acid, cetyl trimethyl One or more of ammonium bromide, polyethylene glycol, potassium polyacrylate, octylphenol polyoxyethylene ether or sulfonate fluorine dispersant.
进一步的,所述粘结剂为聚偏氟乙烯、丁苯乳胶、苯丙乳胶、聚乙烯醇、聚乙烯醇缩丁醛、海藻酸钠、聚丙烯酰胺、聚甲基丙烯酸甲酯、丙烯酸丁脂、乙烯-醋酸乙烯酯共聚物、聚醋酸乙烯酯、聚氨酯、羟乙基纤维素、甲基羟乙基纤维素、羧甲基纤维素钠、聚丙烯酰胺、聚氧化乙烯以聚四氟乙烯中的一种或者多种。Further, the binder is polyvinylidene fluoride, styrene-butadiene latex, styrene-acrylic latex, polyvinyl alcohol, polyvinyl butyral, sodium alginate, polyacrylamide, polymethyl methacrylate, butyl acrylate Grease, ethylene-vinyl acetate copolymer, polyvinyl acetate, polyurethane, hydroxyethyl cellulose, methyl hydroxyethyl cellulose, sodium carboxymethyl cellulose, polyacrylamide, polyethylene oxide and polytetrafluoroethylene one or more of them.
进一步的,所述增塑剂为邻苯二甲酸二丁酯、邻苯二甲酸丁苄酯、硬脂酸丁酯、邻苯二甲酸二甲酯、磷酸三甲苯酯、聚乙二醇、松香酸甲酯、多元醇、邻苯二甲酸二甲酯、二缩三乙二醇、磷酸三丁酯、聚烷基乙二醇中的一种或多种。Further, the plasticizer is dibutyl phthalate, butyl benzyl phthalate, butyl stearate, dimethyl phthalate, tricresyl phosphate, polyethylene glycol, rosin One or more of methyl ester, polyol, dimethyl phthalate, triethylene glycol, tributyl phosphate, and polyalkylene glycol.
进一步的,所述溶剂为去离子水。Further, the solvent is deionized water.
有益效果Beneficial effect
本发明采用的水基流延成型工艺使用水作为唯一溶剂,安全、绿色、环保,浆料的稳定性好,制得的陶瓷电解质膜具有优异的烧结能力、离子电导率和力学性能;工艺简单,且生产成本低,容易实现大规模生产,可用于固态锂电池、燃料电池技术等领域。The water-based tape casting process adopted in the present invention uses water as the only solvent, which is safe, green, and environmentally friendly. The stability of the slurry is good, and the prepared ceramic electrolyte membrane has excellent sintering ability, ion conductivity and mechanical properties; the process is simple , and the production cost is low, and it is easy to realize large-scale production, and can be used in solid-state lithium battery, fuel cell technology and other fields.
本发明通过水基流延制备的陶瓷电解质膜面积大,均一性好;而且在一定程度上提高了陶瓷电解质膜的烧结能力、离子电导率和力学性能;采用水作为唯一溶剂有效改善了陶瓷电解质膜制备过程中的环保难题,并且通过流延工艺,制备过程得到简化,加工成本有效降低。The ceramic electrolyte membrane prepared by water-based casting in the present invention has large area and good uniformity; and to a certain extent, the sintering ability, ion conductivity and mechanical properties of the ceramic electrolyte membrane are improved; water is used as the only solvent to effectively improve the ceramic electrolyte Environmental protection problems in the film preparation process, and through the casting process, the preparation process is simplified and the processing cost is effectively reduced.
当然,实施本发明的任一产品并不一定需要同时达到以上所述的所有优点。Of course, any product implementing the present invention does not necessarily need to achieve all the above-mentioned advantages at the same time.
附图说明Description of drawings
为了更清楚地说明本发明实施例的技术方案,下面将对实施例描述所需要使用的附图作简单地介绍,下面描述中的附图仅仅是本发明的一些实施例,对于本领域普通技术人员来讲,在不付出创造性劳动的前提下,还可以根据这些附图获得其他的附图。In order to more clearly illustrate the technical solutions of the embodiments of the present invention, the following will briefly introduce the accompanying drawings that are required for the description of the embodiments. The accompanying drawings in the following description are only some embodiments of the present invention. As far as people are concerned, other drawings can also be obtained based on these drawings on the premise of not paying creative work.
图1为本发明一种应用于全固态锂电池的固态陶瓷电解质膜的制备方法的流程图;Fig. 1 is a flow chart of a method for preparing a solid ceramic electrolyte membrane applied to an all-solid lithium battery of the present invention;
图2为本发明提供的致密电解质素胚的图片。Fig. 2 is a picture of the dense electrolyte prime embryo provided by the present invention.
图3为本发明提供的电解质膜片烧结后的图片。Fig. 3 is a picture of the sintered electrolyte membrane provided by the present invention.
图4为本发明实施例1在0.01Hz~1MHz范围内的EIS图。Fig. 4 is an EIS diagram in the range of 0.01 Hz to 1 MHz in Example 1 of the present invention.
图5为本发明实施例2在0.01Hz~1MHz范围内的EIS图。Fig. 5 is an EIS diagram in the range of 0.01 Hz to 1 MHz in Example 2 of the present invention.
图6为本发明实施例3在0.01Hz~1MHz范围内的EIS图。Fig. 6 is an EIS diagram in the range of 0.01 Hz to 1 MHz in Example 3 of the present invention.
具体实施方式Detailed ways
下面将结合本发明实施例中的附图,对本发明实施例中的技术方案进行清楚、完整地描述,显然,所描述的实施例仅仅是本发明一部分实施例,而不是全部的实施例。基于本发明中的实施例,本领域普通技术人员在没有做出创造性劳动前提下所获得的所有其它实施例,都属于本发明保护的范围。The following will clearly and completely describe the technical solutions in the embodiments of the present invention with reference to the accompanying drawings in the embodiments of the present invention. Obviously, the described embodiments are only some, not all, embodiments of the present invention. Based on the embodiments of the present invention, all other embodiments obtained by persons of ordinary skill in the art without making creative efforts belong to the protection scope of the present invention.
实施例1Example 1
一种应用于全固态锂电池的固态陶瓷电解质膜的制备方法,包括以下步骤:A method for preparing a solid ceramic electrolyte membrane applied to an all-solid lithium battery, comprising the following steps:
(1)将制备的LATP粉体10g进行球磨12h,过筛(200目)。(1) 10 g of the prepared LATP powder was ball milled for 12 hours, and sieved (200 mesh).
(2)将三乙醇胺(TEA)分散剂预先配置为质量分数为15%的水溶液,超声处理6h;将适量的聚乙烯醇(PVA)粘结剂分批加入水溶液中,在60℃水浴中搅拌24h,预先配置为质量分数为15%的水溶液。(2) The triethanolamine (TEA) dispersant is pre-configured as an aqueous solution with a mass fraction of 15%, and ultrasonically treated for 6 hours; an appropriate amount of polyvinyl alcohol (PVA) binder is added to the aqueous solution in batches, and stirred in a water bath at 60°C 24h, pre-configured as an aqueous solution with a mass fraction of 15%.
(3)以LATP电解质粉体为原料,加入5g水和预先配置好的分散剂1.5g球磨4h;加入聚乙二醇增塑剂1.3g,继续球磨12h。(3) Using LATP electrolyte powder as raw material, add 5g of water and 1.5g of pre-prepared dispersant for ball milling for 4 hours; add 1.3g of polyethylene glycol plasticizer, and continue ball milling for 12 hours.
(4)得到的浆料加入预先配置好的聚乙烯醇粘结剂7.5g,球磨6h。然后进行真空脱泡50kpa,持续15min。(4) Add 7.5 g of pre-prepared polyvinyl alcohol binder to the obtained slurry, and ball mill for 6 hours. Then carry out vacuum degassing at 50kpa for 15min.
(5)将(4)得到的浆料过筛(200目)。调节刮刀500μm的高度,流延速度10cm/min。(5) Sieve the slurry obtained in (4) (200 mesh). The height of the scraper was adjusted to 500 μm, and the casting speed was 10 cm/min.
(6)流延得到的薄膜在室温条件下干燥,选择3层进行热压,热压温度90℃,压力10MPa,时间15min;将热压后的膜片裁剪成直径为16mm的圆片。(6) The film obtained by casting was dried at room temperature, and three layers were selected for hot-pressing at a temperature of 90° C., a pressure of 10 MPa, and a time of 15 minutes; the hot-pressed film was cut into discs with a diameter of 16 mm.
(7)热压后的素胚置于马弗炉内,按照2℃/min的升温速率升温至550℃、保温12h,再以2℃/min的升温速率升温至850℃、保温6h,经程序降温后得到致密陶瓷电解质膜。(7) The hot-pressed plain embryo is placed in a muffle furnace, heated to 550°C at a heating rate of 2°C/min, and kept for 12 hours, then raised to 850°C at a heating rate of 2°C/min, and kept for 6 hours. A dense ceramic electrolyte membrane was obtained after programmed cooling.
对制备好的LATP固态电解质膜在室温下0.01Hz~1MHz范围内进行阻抗测试,如图4所示,其离子电导率为2.06×10-4S/cm。The prepared LATP solid electrolyte membrane was tested for impedance at room temperature in the range of 0.01 Hz to 1 MHz, as shown in Figure 4, its ionic conductivity was 2.06×10 -4 S/cm.
实施例2Example 2
一种应用于全固态锂电池的固态陶瓷电解质膜的制备方法,包括以下步骤:A method for preparing a solid ceramic electrolyte membrane applied to an all-solid lithium battery, comprising the following steps:
(1)将制备得到的LAZP粉体10g进行球磨12h,过筛(200目)。(1) 10 g of the prepared LAZP powder was ball milled for 12 hours, and sieved (200 mesh).
(2)将三乙醇胺(TEA)分散剂预先配置为质量分数为15%的水溶液,超声处理6h;将适量的聚乙烯醇(PVA)粘结剂分批加入水溶液中,在60℃水浴中搅拌24h,预先配置为质量分数为15%的水溶液。(2) The triethanolamine (TEA) dispersant is pre-configured as an aqueous solution with a mass fraction of 15%, and ultrasonically treated for 6 hours; an appropriate amount of polyvinyl alcohol (PVA) binder is added to the aqueous solution in batches, and stirred in a water bath at 60°C 24h, pre-configured as an aqueous solution with a mass fraction of 15%.
(3)以LAZP电解质粉体为原料,加入5g水和预先配置好的分散剂1.7g球磨6h;加入聚乙二醇增塑剂1.53g,继续球磨12h。(3) Using LAZP electrolyte powder as the raw material, add 5g of water and 1.7g of pre-prepared dispersant for ball milling for 6 hours; add 1.53g of polyethylene glycol plasticizer, and continue ball milling for 12 hours.
(4)得到的浆料加入预先配置好的聚乙烯醇粘结剂8.52g,球磨6h。然后进行真空脱泡50kpa,持续15min。(4) Add 8.52 g of pre-prepared polyvinyl alcohol binder to the obtained slurry, and ball mill for 6 hours. Then carry out vacuum degassing at 50kpa for 15min.
(5)将(4)得到的浆料过筛(200目)。调节刮刀300μm的高度,流延速度8cm/min。(5) Sieve the slurry obtained in (4) (200 mesh). Adjust the height of the scraper to 300 μm, and the casting speed to 8 cm/min.
(6)流延得到的薄膜在室温条件下干燥,选择5层进行热压,热压温度90℃,压力10MPa,时间15min;将热压后的膜片裁剪成直径为16mm的圆片。(6) The film obtained by casting was dried at room temperature, and 5 layers were selected for hot-pressing at a temperature of 90° C., a pressure of 10 MPa, and a time of 15 minutes; the hot-pressed film was cut into discs with a diameter of 16 mm.
(7)热压后的素胚置于马弗炉内,按照2℃/min的升温速率升温至550℃、保温12h,再以2℃/min的升温速率升温至900℃、保温2h,经程序降温后得到致密陶瓷电解质膜。(7) The hot-pressed plain embryo is placed in a muffle furnace, heated to 550°C at a heating rate of 2°C/min, and kept for 12 hours, then raised to 900°C at a heating rate of 2°C/min, and kept for 2 hours. A dense ceramic electrolyte membrane was obtained after programmed cooling.
对制备好的LAZP固态电解质膜在室温下0.01Hz~1MHz范围内进行阻抗测试,如图5所示,其离子电导率为5.42×10-6S/cm。The prepared LAZP solid electrolyte membrane was tested for impedance at room temperature in the range of 0.01 Hz to 1 MHz, as shown in Figure 5, its ionic conductivity was 5.42×10 -6 S/cm.
实施例3Example 3
一种应用于全固态锂电池的固态陶瓷电解质膜的制备方法,包括以下步骤:A method for preparing a solid ceramic electrolyte membrane applied to an all-solid lithium battery, comprising the following steps:
(1)将制备得到LAGP粉体10g进行球磨12h,过筛(200目)。(1) 10 g of the prepared LAGP powder was ball milled for 12 hours, and sieved (200 mesh).
(2)将三乙醇胺(TEA)分散剂预先配置为质量分数为15%的水溶液,超声处理6h;将适量的聚乙烯醇(PVA)粘结剂分批加入水溶液中,在60℃水浴中搅拌12h,预先配置为质量分数为15%的水溶液。(2) The triethanolamine (TEA) dispersant is pre-configured as an aqueous solution with a mass fraction of 15%, and ultrasonically treated for 6 hours; an appropriate amount of polyvinyl alcohol (PVA) binder is added to the aqueous solution in batches, and stirred in a water bath at 60°C 12h, pre-configured as an aqueous solution with a mass fraction of 15%.
(3)以电解质粉体为原料,加入5g水和预先配置好的分散剂1.95g球磨3h;加入聚乙二醇增塑剂2.3g和聚丙二醇消泡剂0.15g,继续球磨12h。(3) Using electrolyte powder as raw material, add 5g of water and 1.95g of pre-prepared dispersant for ball milling for 3 hours; add 2.3g of polyethylene glycol plasticizer and 0.15g of polypropylene glycol defoamer, and continue ball milling for 12 hours.
(4)得到的浆料加入预先配置好的聚乙烯醇粘结剂8g,球磨6h。然后进行真空脱泡50kpa,持续15min。(4) Add 8 g of pre-prepared polyvinyl alcohol binder to the obtained slurry, and ball mill for 6 hours. Then carry out vacuum degassing at 50kpa for 15min.
(5)将(4)得到的浆料过筛(200目)。调节刮刀300μm的高度,流延速度8cm/min。(5) Sieve the slurry obtained in (4) (200 mesh). Adjust the height of the scraper to 300 μm, and the casting speed to 8 cm/min.
(6)流延得到的薄膜在室温条件下干燥,选择5层进行热压,热压温度95℃,压力8MPa,时间20min;将热压后的膜片裁剪成直径为16mm的圆片。(6) The film obtained by casting was dried at room temperature, and 5 layers were selected for hot-pressing at a temperature of 95° C., a pressure of 8 MPa, and a time of 20 minutes; the hot-pressed film was cut into discs with a diameter of 16 mm.
(7)热压后的素胚置于马弗炉内,按照2℃/min的升温速率升温至550℃、保温12h,再以2℃/min的升温速率升温至900℃、保温12h,经程序降温后得到致密陶瓷电解质膜。(7) The hot-pressed plain embryo is placed in a muffle furnace, heated to 550°C at a heating rate of 2°C/min, and kept for 12 hours, then raised to 900°C at a heating rate of 2°C/min, and held for 12 hours. A dense ceramic electrolyte membrane was obtained after programmed cooling.
对制备好的LAGP固态电解质膜在室温下0.01Hz~1MHz范围内进行阻抗测试,如图6所示,其离子电导率为3.14×10-4S/cm。The prepared LAGP solid electrolyte membrane was tested for impedance at room temperature in the range of 0.01 Hz to 1 MHz, as shown in Figure 6, its ionic conductivity was 3.14×10 -4 S/cm.
综上所述,水基流延制备的陶瓷电解质膜面积大,均一性好;而且在一定程度上提高了陶瓷电解质膜的烧结能力、离子电导率和力学性能;采用水作为唯一溶剂有效改善了陶瓷电解质膜制备过程中的环保难题,并且通过流延工艺,制备过程得到简化,加工成本有效降低。In summary, the ceramic electrolyte membrane prepared by water-based casting has a large area and good uniformity; and to a certain extent, the sintering ability, ion conductivity and mechanical properties of the ceramic electrolyte membrane are improved; the use of water as the only solvent effectively improves the Environmental protection problems in the preparation process of the ceramic electrolyte membrane, and through the casting process, the preparation process is simplified and the processing cost is effectively reduced.
以上所述,仅是本发明的较佳实施例而已,并非对本发明作任何形式上的限制,虽然本发明已以较佳实施例揭露如上,然而并非用以限定本发明,任何熟悉本专业的技术人员,在不脱离本发明技术方案范围内,当可利用上述揭示的技术内容做出些许更动或修饰为等同变化的等效实施例,但凡是未脱离本发明技术方案的内容,依据本发明的技术实质对以上实施例所作的任何简单修改、等同变化与修饰,均仍属于本发明技术方案的范围内。The above description is only a preferred embodiment of the present invention, and does not limit the present invention in any form. Although the present invention has been disclosed as above with preferred embodiments, it is not intended to limit the present invention. Anyone familiar with this field Those skilled in the art, without departing from the scope of the technical solution of the present invention, may use the technical content disclosed above to make some changes or modify them into equivalent embodiments with equivalent changes. Technical Essence of the Invention Any simple modifications, equivalent changes and modifications made to the above embodiments still fall within the scope of the technical solutions of the present invention.
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