CN115588820A - A low-cost lithium battery separator with high electrolyte wettability and preparation method thereof - Google Patents
A low-cost lithium battery separator with high electrolyte wettability and preparation method thereof Download PDFInfo
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- 229910052744 lithium Inorganic materials 0.000 title claims abstract description 28
- WHXSMMKQMYFTQS-UHFFFAOYSA-N Lithium Chemical compound [Li] WHXSMMKQMYFTQS-UHFFFAOYSA-N 0.000 title claims abstract description 27
- 239000003792 electrolyte Substances 0.000 title claims abstract description 24
- 238000002360 preparation method Methods 0.000 title claims description 13
- 229920000642 polymer Polymers 0.000 claims abstract description 58
- 239000002002 slurry Substances 0.000 claims abstract description 48
- 239000002033 PVDF binder Substances 0.000 claims abstract description 40
- 229920002981 polyvinylidene fluoride Polymers 0.000 claims abstract description 39
- 238000000576 coating method Methods 0.000 claims abstract description 38
- 229920003229 poly(methyl methacrylate) Polymers 0.000 claims abstract description 34
- 239000004926 polymethyl methacrylate Substances 0.000 claims abstract description 34
- 239000011248 coating agent Substances 0.000 claims abstract description 29
- 239000000080 wetting agent Substances 0.000 claims abstract description 21
- 239000002270 dispersing agent Substances 0.000 claims abstract description 20
- 239000011230 binding agent Substances 0.000 claims abstract description 18
- 239000002562 thickening agent Substances 0.000 claims abstract description 18
- 239000011812 mixed powder Substances 0.000 claims abstract description 17
- 239000002518 antifoaming agent Substances 0.000 claims abstract description 15
- 229910021642 ultra pure water Inorganic materials 0.000 claims abstract description 15
- 239000012498 ultrapure water Substances 0.000 claims abstract description 15
- 229920001519 homopolymer Polymers 0.000 claims abstract description 12
- 239000000463 material Substances 0.000 claims abstract description 11
- 239000000203 mixture Substances 0.000 claims abstract description 8
- 238000003756 stirring Methods 0.000 claims description 51
- -1 alkyl quaternary ammonium salt Chemical class 0.000 claims description 42
- RTZKZFJDLAIYFH-UHFFFAOYSA-N Diethyl ether Chemical compound CCOCC RTZKZFJDLAIYFH-UHFFFAOYSA-N 0.000 claims description 20
- VVQNEPGJFQJSBK-UHFFFAOYSA-N Methyl methacrylate Chemical compound COC(=O)C(C)=C VVQNEPGJFQJSBK-UHFFFAOYSA-N 0.000 claims description 11
- 238000000034 method Methods 0.000 claims description 11
- 229920000098 polyolefin Polymers 0.000 claims description 11
- 239000002202 Polyethylene glycol Substances 0.000 claims description 10
- 235000014113 dietary fatty acids Nutrition 0.000 claims description 10
- 239000000194 fatty acid Substances 0.000 claims description 10
- 229930195729 fatty acid Natural products 0.000 claims description 10
- 239000011259 mixed solution Substances 0.000 claims description 10
- 238000002156 mixing Methods 0.000 claims description 10
- 229920001223 polyethylene glycol Polymers 0.000 claims description 10
- 239000004094 surface-active agent Substances 0.000 claims description 10
- 239000007788 liquid Substances 0.000 claims description 9
- 229920002503 polyoxyethylene-polyoxypropylene Polymers 0.000 claims description 9
- 239000000843 powder Substances 0.000 claims description 9
- 239000002994 raw material Substances 0.000 claims description 7
- 229920003171 Poly (ethylene oxide) Polymers 0.000 claims description 6
- 230000005251 gamma ray Effects 0.000 claims description 6
- HDLBOHGQTWKFRG-CVBJKYQLSA-N 3-azaniumylpropylazanium;(z)-octadec-9-enoate Chemical compound NCCCN.CCCCCCCC\C=C/CCCCCCCC(O)=O.CCCCCCCC\C=C/CCCCCCCC(O)=O HDLBOHGQTWKFRG-CVBJKYQLSA-N 0.000 claims description 5
- 229920001651 Cyanoacrylate Polymers 0.000 claims description 5
- MWCLLHOVUTZFKS-UHFFFAOYSA-N Methyl cyanoacrylate Chemical compound COC(=O)C(=C)C#N MWCLLHOVUTZFKS-UHFFFAOYSA-N 0.000 claims description 5
- XTXRWKRVRITETP-UHFFFAOYSA-N Vinyl acetate Chemical compound CC(=O)OC=C XTXRWKRVRITETP-UHFFFAOYSA-N 0.000 claims description 5
- NLCKLZIHJQEMCU-UHFFFAOYSA-N cyano prop-2-enoate Chemical class C=CC(=O)OC#N NLCKLZIHJQEMCU-UHFFFAOYSA-N 0.000 claims description 5
- 150000004665 fatty acids Chemical class 0.000 claims description 5
- 239000004816 latex Substances 0.000 claims description 5
- 229920000126 latex Polymers 0.000 claims description 5
- 239000002736 nonionic surfactant Substances 0.000 claims description 5
- UPHWVVKYDQHTCF-UHFFFAOYSA-N octadecylazanium;acetate Chemical compound CC(O)=O.CCCCCCCCCCCCCCCCCCN UPHWVVKYDQHTCF-UHFFFAOYSA-N 0.000 claims description 5
- 229920002401 polyacrylamide Polymers 0.000 claims description 5
- 229920005862 polyol Polymers 0.000 claims description 5
- 150000003077 polyols Chemical class 0.000 claims description 5
- 229920001451 polypropylene glycol Polymers 0.000 claims description 5
- SCPYDCQAZCOKTP-UHFFFAOYSA-N silanol Chemical compound [SiH3]O SCPYDCQAZCOKTP-UHFFFAOYSA-N 0.000 claims description 5
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 claims description 4
- 150000001412 amines Chemical class 0.000 claims description 4
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 claims description 2
- 229920002873 Polyethylenimine Chemical class 0.000 claims description 2
- 239000004721 Polyphenylene oxide Substances 0.000 claims description 2
- 229920002125 Sokalan® Polymers 0.000 claims description 2
- 150000008431 aliphatic amides Chemical group 0.000 claims description 2
- 150000008051 alkyl sulfates Chemical group 0.000 claims description 2
- 239000004205 dimethyl polysiloxane Substances 0.000 claims description 2
- 229920003063 hydroxymethyl cellulose Polymers 0.000 claims description 2
- 229940031574 hydroxymethyl cellulose Drugs 0.000 claims description 2
- 229910052742 iron Inorganic materials 0.000 claims description 2
- 229920000435 poly(dimethylsiloxane) Polymers 0.000 claims description 2
- 239000004584 polyacrylic acid Substances 0.000 claims description 2
- 229920000570 polyether Polymers 0.000 claims description 2
- 238000005096 rolling process Methods 0.000 claims description 2
- 229910052708 sodium Inorganic materials 0.000 claims description 2
- 239000011734 sodium Substances 0.000 claims description 2
- 229920005822 acrylic binder Polymers 0.000 claims 1
- 238000001914 filtration Methods 0.000 claims 1
- 230000001678 irradiating effect Effects 0.000 claims 1
- 230000008961 swelling Effects 0.000 abstract description 5
- 230000009286 beneficial effect Effects 0.000 abstract description 3
- 239000000126 substance Substances 0.000 abstract description 2
- 239000000853 adhesive Substances 0.000 description 20
- 230000001070 adhesive effect Effects 0.000 description 19
- 230000000052 comparative effect Effects 0.000 description 8
- 239000013530 defoamer Substances 0.000 description 7
- NIXOWILDQLNWCW-UHFFFAOYSA-N acrylic acid group Chemical group C(C=C)(=O)O NIXOWILDQLNWCW-UHFFFAOYSA-N 0.000 description 4
- 229910052799 carbon Inorganic materials 0.000 description 4
- 229920005569 poly(vinylidene fluoride-co-hexafluoropropylene) Polymers 0.000 description 4
- 229920002134 Carboxymethyl cellulose Polymers 0.000 description 3
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 3
- 239000004698 Polyethylene Substances 0.000 description 3
- DPXJVFZANSGRMM-UHFFFAOYSA-N acetic acid;2,3,4,5,6-pentahydroxyhexanal;sodium Chemical group [Na].CC(O)=O.OCC(O)C(O)C(O)C(O)C=O DPXJVFZANSGRMM-UHFFFAOYSA-N 0.000 description 3
- 235000010948 carboxy methyl cellulose Nutrition 0.000 description 3
- 239000001768 carboxy methyl cellulose Substances 0.000 description 3
- 239000003795 chemical substances by application Substances 0.000 description 3
- 239000006255 coating slurry Substances 0.000 description 3
- 239000003292 glue Substances 0.000 description 3
- 150000002466 imines Chemical class 0.000 description 3
- 230000004048 modification Effects 0.000 description 3
- 238000012986 modification Methods 0.000 description 3
- 229920000573 polyethylene Polymers 0.000 description 3
- 235000019812 sodium carboxymethyl cellulose Nutrition 0.000 description 3
- 229920001027 sodium carboxymethylcellulose Polymers 0.000 description 3
- 239000000243 solution Substances 0.000 description 3
- 239000002131 composite material Substances 0.000 description 2
- 239000011146 organic particle Substances 0.000 description 2
- 230000008569 process Effects 0.000 description 2
- 238000007761 roller coating Methods 0.000 description 2
- ODURFHDFZAVGHC-KTKRTIGZSA-N (z)-2-aminooctadec-9-enoic acid Chemical class CCCCCCCC\C=C/CCCCCCC(N)C(O)=O ODURFHDFZAVGHC-KTKRTIGZSA-N 0.000 description 1
- 239000003522 acrylic cement Substances 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 229920001577 copolymer Polymers 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 230000009477 glass transition Effects 0.000 description 1
- HCDGVLDPFQMKDK-UHFFFAOYSA-N hexafluoropropylene Chemical group FC(F)=C(F)C(F)(F)F HCDGVLDPFQMKDK-UHFFFAOYSA-N 0.000 description 1
- 238000009776 industrial production Methods 0.000 description 1
- 238000009413 insulation Methods 0.000 description 1
- 230000010220 ion permeability Effects 0.000 description 1
- 150000002500 ions Chemical class 0.000 description 1
- 150000002641 lithium Chemical class 0.000 description 1
- 239000011148 porous material Substances 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Classifications
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M50/00—Constructional details or processes of manufacture of the non-active parts of electrochemical cells other than fuel cells, e.g. hybrid cells
- H01M50/40—Separators; Membranes; Diaphragms; Spacing elements inside cells
- H01M50/409—Separators, membranes or diaphragms characterised by the material
- H01M50/411—Organic material
- H01M50/414—Synthetic resins, e.g. thermoplastics or thermosetting resins
-
- 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
- H01M50/00—Constructional details or processes of manufacture of the non-active parts of electrochemical cells other than fuel cells, e.g. hybrid cells
- H01M50/40—Separators; Membranes; Diaphragms; Spacing elements inside cells
- H01M50/403—Manufacturing processes of separators, membranes or diaphragms
-
- 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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- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Manufacturing & Machinery (AREA)
- Cell Separators (AREA)
Abstract
Description
技术领域technical field
本发明涉及锂电池隔膜技术领域,尤其涉及一种高电解液浸润性的低成本锂电池隔膜及其制备方法。The invention relates to the technical field of lithium battery separators, in particular to a low-cost lithium battery separator with high electrolyte wettability and a preparation method thereof.
背景技术Background technique
锂电池的结构包括正极、负极、电解液和隔膜。隔膜的主要作用是将电池的正极与负极隔开,以避免正负极之间短路。因此,隔膜需要保持较好的离子通过性以及电子绝缘性。在工业生产中,由聚烯烃材料制备的隔膜一般称之为基膜,然而由于基膜可能存在各种性能上的不足之处,往往会对基膜表面进行涂覆处理,以补足其各种性能缺陷。The structure of a lithium battery includes a positive electrode, a negative electrode, an electrolyte, and a separator. The main function of the separator is to separate the positive and negative electrodes of the battery to avoid short circuits between the positive and negative electrodes. Therefore, the separator needs to maintain good ion permeability and electronic insulation. In industrial production, the diaphragm made of polyolefin materials is generally called the base film. However, because the base film may have various performance deficiencies, the surface of the base film is often coated to make up for its various properties. Performance flaws.
为提高隔膜与极片之间的粘结能力,往往会在基膜表面涂覆有机涂层以提高其粘结性,较为成熟的是采用PVDF类物质作为有机涂层。在实际的使用中,往往涂覆的并不是PVDF的均聚物,涂覆的一般是PVDF-HFP(聚偏氟乙烯和六氟丙烯)的共聚物,其原因是PVDF的均聚物的溶胀性能较差且离子电导率较低,因此利用HPF对PVDF共聚物改性后再进行涂覆。但是,采用PVDF-HFP材料的成本很高,对企业负担比较大。In order to improve the bonding ability between the separator and the pole piece, an organic coating is often applied on the surface of the base film to improve its bonding property. The more mature one is to use PVDF as the organic coating. In actual use, it is often not the homopolymer of PVDF that is coated, but the copolymer of PVDF-HFP (polyvinylidene fluoride and hexafluoropropylene) is usually coated because of the swelling of the homopolymer of PVDF The performance is poor and the ionic conductivity is low, so the PVDF copolymer is modified by HPF before coating. However, the cost of using PVDF-HFP materials is very high, which is a relatively large burden on enterprises.
而PMMA(聚甲基丙烯酸甲酯,俗称亚克力)由于亲和电解液、价格便宜和玻璃化温度易控,成为可替代PVDF-HFP的材料之一。但是,单纯采用PMMA材料进行涂覆则存在过度溶胀的问题,PMMA过度溶胀后会堵塞隔膜孔隙,使隔膜的离子电导率降低。PMMA (polymethyl methacrylate, commonly known as acrylic) has become one of the materials that can replace PVDF-HFP due to its affinity electrolyte, low price and easy control of glass transition temperature. However, there is a problem of excessive swelling when simply using PMMA material for coating. Excessive swelling of PMMA will block the pores of the diaphragm and reduce the ionic conductivity of the diaphragm.
因此,我们提出了一种高电解液浸润性的低成本锂电池隔膜及其制备方法用于解决上述问题。Therefore, we propose a low-cost lithium battery separator with high electrolyte wettability and its preparation method to solve the above problems.
发明内容Contents of the invention
本发明的目的是为了解决现有技术中存在的缺点,而提出的一种高电解液浸润性的低成本锂电池隔膜及其制备方法。The purpose of the present invention is to solve the shortcomings in the prior art, and propose a low-cost lithium battery diaphragm with high electrolyte wettability and a preparation method thereof.
一种高电解液浸润性的低成本锂电池隔膜,包括基膜以及涂覆于基膜任意一侧或两侧的聚合物涂层,聚合物涂层包括PVDF和PMMA材料;A low-cost lithium battery separator with high electrolyte wettability, including a base film and a polymer coating coated on either side or both sides of the base film, the polymer coating includes PVDF and PMMA materials;
聚合物浆料,由以下重量百分比的原料组成:混合粉体6%~13%、相容剂5%~15%、分散剂0.3%~1.2%、增稠剂2.5%~7%、粘结剂5%~13.5%、润湿剂0.1%~0.35%、消泡剂0.1%~0.35%,其余为超纯水;The polymer slurry is composed of the following raw materials in weight percentage: mixed powder 6%-13%, compatibilizer 5%-15%, dispersant 0.3%-1.2%, thickener 2.5%-7%, adhesive Agent 5%~13.5%, wetting agent 0.1%~0.35%, defoamer 0.1%~0.35%, and the rest is ultrapure water;
所述混合粉体为PVDF和PMMA的混合物,重量比为PVDF:PMMA=5~30:70~95。The mixed powder is a mixture of PVDF and PMMA, and the weight ratio is PVDF:PMMA=5-30:70-95.
优选的,所述基膜为聚烯烃隔膜。Preferably, the base film is a polyolefin separator.
优选的,所述分散剂为脂肪族酰胺类,所述增稠剂为羟甲基纤维素钠类,所述粘结剂为聚丙烯酸类,所述润湿剂为烷基硫酸盐类,所述消泡剂为聚醚型消泡剂。Preferably, the dispersant is aliphatic amides, the thickener is sodium hydroxymethylcellulose, the binder is polyacrylic acid, and the wetting agent is alkyl sulfate. Described defoamer is polyether type defoamer.
优选的,所述分散剂为聚丙烯酰胺、十八碳烯胺醋酸盐、烷基季铵盐、氨基丙胺二油酸酯、聚乙二醇型多元醇、聚乙烯亚胺衍生物、油氨基油酸酯中的一种,所述粘结剂为氰基丙烯酸酯衍生物粘结剂、氰基丙烯酸酯聚乙二醇粘结剂、丙烯酸粘结剂、醋酸乙烯基聚合物乳胶粘结剂中的一种,所述润湿剂为聚氧乙烯型表面活性剂、脂肪酸表面活性剂、硅醇类非离子表面活性剂中的一种,所述消泡剂为高碳醇脂肪酸酯复合物、聚氧乙烯聚氧丙烯季戊四醇醚、聚氧乙烯聚氧丙醇胺醚、聚氧丙烯甘油醚、聚氧丙烯聚氧乙烯甘油醚和聚二甲基硅氧烷中的一种。Preferably, the dispersant is polyacrylamide, octadecylamine acetate, alkyl quaternary ammonium salt, aminopropylamine dioleate, polyethylene glycol polyol, polyethyleneimine derivative, oil One of amino oleic acid esters, the adhesive is cyanoacrylate derivative adhesive, cyanoacrylate polyethylene glycol adhesive, acrylic adhesive, vinyl acetate polymer latex adhesive One of the wetting agents, the wetting agent is one of polyoxyethylene surfactants, fatty acid surfactants, and silanol nonionic surfactants, and the defoaming agent is a high-carbon alcohol fatty acid ester Compound, polyoxyethylene polyoxypropylene pentaerythritol ether, polyoxyethylene polyoxypropanolamine ether, polyoxypropylene glyceryl ether, polyoxypropylene polyoxyethylene glyceryl ether and polydimethylsiloxane.
优选的,所述相容剂,由以下重量份的原料组成:PVDF均聚物粉体40~80、甲基丙烯酸甲酯液体20~60。Preferably, the compatibilizer is composed of the following raw materials in parts by weight: 40-80 parts of PVDF homopolymer powder, and 20-60 parts of methyl methacrylate liquid.
一种高电解液浸润性的低成本锂电池隔膜的制备方法,包括以下步骤:A method for preparing a low-cost lithium battery diaphragm with high electrolyte wettability, comprising the following steps:
S1、制备聚合物浆料:S1, prepare polymer slurry:
S1-1、按质量比取0.3%~1.2%的分散剂和6%~13%的混合粉体投入超纯水预混,获得第一中间体;S1-1. Take 0.3%-1.2% dispersant and 6%-13% mixed powder according to the mass ratio and put them into ultrapure water for pre-mixing to obtain the first intermediate;
S1-2、向所述第一中间体中按质量比加入5%~13.5%的粘结剂和2.5%~7%的增稠剂继续搅拌,获得第二中间体;S1-2. Add 5% to 13.5% of binder and 2.5% to 7% of thickener to the first intermediate by mass ratio and continue stirring to obtain a second intermediate;
S1-3、向所述第二中间体中按质量比加入0.1%~0.35%的润湿剂和0.1%~0.35%的消泡剂搅拌,并过滤除铁之后获得聚合物浆料;S1-3. Add 0.1%-0.35% wetting agent and 0.1%-0.35% defoamer to the second intermediate by mass ratio, stir, and filter to remove iron to obtain polymer slurry;
S2、制备相容剂:S2, preparation compatibilizer:
S2-1、将PVDF均聚物粉体及甲基丙烯酸甲酯液体按40~80:20~60的比例投入超纯水中进行搅拌混合获得混合溶液;S2-1. Put the PVDF homopolymer powder and methyl methacrylate liquid in the ratio of 40-80:20-60 into ultrapure water for stirring and mixing to obtain a mixed solution;
S2-2、将前述的混合溶液置于伽马射线环境下,充分照射后取出,获得相容剂;S2-2. Place the aforementioned mixed solution in a gamma ray environment, take it out after sufficient irradiation, and obtain a compatibilizer;
S3、对前述聚合物浆料进行改性:将5~15份相容剂投入85~95份的聚合物浆料中搅拌混合后静置,获得所述改性聚合物浆料;S3. Modifying the aforementioned polymer slurry: putting 5-15 parts of compatibilizer into 85-95 parts of polymer slurry, stirring and mixing, and then standing still to obtain the modified polymer slurry;
S4、制备隔膜:将所制得的改性聚合物浆料均匀涂覆于隔膜上,烘烤,收卷备用。S4. Preparing the separator: uniformly coating the prepared modified polymer slurry on the separator, baking, and rolling up for later use.
优选的,S1-1步骤中,预混时间为10~120min,转速为400~900rpm。Preferably, in step S1-1, the premixing time is 10-120 minutes, and the rotation speed is 400-900 rpm.
优选的,S1-2步骤中,混合时间为20~80min,转速为350~700rpm。Preferably, in step S1-2, the mixing time is 20-80 minutes, and the rotation speed is 350-700 rpm.
优选的,S1-3中步骤中,混合时间为20~80min,转速为150~550rpm。Preferably, in the step of S1-3, the mixing time is 20-80 minutes, and the rotation speed is 150-550 rpm.
优选的,S4步骤中,采用微凹版辊涂布工艺,通过涂布机将改性聚合物浆料均匀辊涂于隔膜上。Preferably, in step S4, a micro-gravure roll coating process is used to uniformly roll-coat the modified polymer slurry on the separator through a coating machine.
本发明的有益效果是:The beneficial effects of the present invention are:
1.相较于传统的PMMA单质涂覆的锂电池涂覆隔膜而言,本发明通过少量PVDF均聚物,有效地抑制了PMMA的过度溶胀情况,从而提高了离子电导率,且相较于传统的PVDF-HFP材料降低了成本。1. Compared with the traditional PMMA single substance coated lithium battery coating diaphragm, the present invention effectively suppresses the excessive swelling of PMMA through a small amount of PVDF homopolymer, thereby improving the ion conductivity, and compared with Traditional PVDF-HFP material reduces cost.
2.本发明开发了一种利于PVDF和PMMA相容的相容剂,该相容剂以PVDF为主链,经过伽马射线照射在PVDF主链接枝MMA支链,使得PVDF和PMMA在浆料中能获得更好的相容性,提高了浆料的稳定性和涂覆的均匀性。2. The present invention has developed a kind of compatibilizer that is beneficial to PVDF and PMMA compatibility, and this compatibilizer is main chain with PVDF, through gamma ray irradiation at PVDF main chain graft MMA branch, makes PVDF and PMMA in slurry It can obtain better compatibility, improve the stability of slurry and the uniformity of coating.
3.本发明采用的是水系涂覆制备隔膜,相较于油系涂覆而言,污染更小,成本更低。3. The present invention uses water-based coating to prepare the diaphragm, which has less pollution and lower cost than oil-based coating.
具体实施方式detailed description
下面结合具体实施例对本发明作进一步解说。The present invention will be further explained below in conjunction with specific embodiments.
实施例一:Embodiment one:
一种高电解液浸润性的低成本锂电池隔膜,包括基膜以及涂覆于基膜任意一侧或两侧的聚合物涂层,聚合物涂层包括PVDF和PMMA材料;基膜为聚烯烃隔膜。A low-cost lithium battery separator with high electrolyte wettability, including a base film and a polymer coating coated on either side or both sides of the base film, the polymer coating includes PVDF and PMMA materials; the base film is polyolefin diaphragm.
聚合物浆料,由以下重量百分比的原料组成:混合粉体6%、相容剂5%、分散剂0.3%、增稠剂2.5%、粘结剂5%、润湿剂0.1%、消泡剂0.1%,混合粉体为PVDF和PMMA的混合物,PVDF:PMMA=5:95。The polymer slurry is composed of the following raw materials in weight percentage: 6% mixed powder, 5% compatibilizer, 0.3% dispersant, 2.5% thickener, 5% binder, 0.1% wetting agent, defoaming agent Agent 0.1%, mixed powder is a mixture of PVDF and PMMA, PVDF:PMMA=5:95.
在上述的聚合物浆料中,采用的分散剂为聚丙烯酰胺、十八碳烯胺醋酸盐、烷基季铵盐、氨基丙胺二油酸酯、聚乙二醇型多元醇、聚乙烯亚胺衍生物、油氨基油酸酯中的一种。In the above polymer slurry, the dispersant used is polyacrylamide, octadecylamine acetate, alkyl quaternary ammonium salt, aminopropylamine dioleate, polyethylene glycol polyol, polyethylene One of imine derivatives and oleyl amino oleate.
增稠剂为羧甲基纤维素钠类(CMC胶液)。The thickener is sodium carboxymethylcellulose (CMC glue).
粘结剂为氰基丙烯酸酯衍生物粘结剂、氰基丙烯酸酯聚乙二醇粘结剂、丙烯酸粘结剂、醋酸乙烯基聚合物乳胶粘结剂中的一种。The adhesive is one of cyanoacrylate derivative adhesives, cyanoacrylate polyethylene glycol adhesives, acrylic adhesives, and vinyl acetate polymer latex adhesives.
润湿剂为聚氧乙烯型表面活性剂、脂肪酸表面活性剂、硅醇类非离子表面活性剂中的一种。The wetting agent is one of polyoxyethylene surfactants, fatty acid surfactants, and silanol nonionic surfactants.
消泡剂为高碳醇脂肪酸酯复合物、聚氧乙烯聚氧丙烯季戊四醇醚、聚氧乙烯聚氧丙醇胺醚、聚氧丙烯甘油醚、聚氧丙烯聚氧乙烯甘油醚和聚二甲基硅氧烷中的一种。The defoaming agent is high carbon alcohol fatty acid ester compound, polyoxyethylene polyoxypropylene pentaerythritol ether, polyoxyethylene polyoxypropylene alcohol amine ether, polyoxypropylene glyceryl ether, polyoxypropylene polyoxyethylene glyceryl ether and polydimethyl One of the base siloxanes.
一种高电解液浸润性的低成本锂电池隔膜的制备方法,包括以下步骤:A method for preparing a low-cost lithium battery diaphragm with high electrolyte wettability, comprising the following steps:
S1、制备聚合物浆料:S1, prepare polymer slurry:
S1-1、按质量比取0.3%的分散剂和6%的混合粉体投入超纯水中搅拌10分钟,搅拌转速为400rpm,获得第一中间体;S1-1. Take 0.3% dispersant and 6% mixed powder according to the mass ratio and put them into ultrapure water and stir for 10 minutes at a stirring speed of 400rpm to obtain the first intermediate;
S1-2、向获得的第一中间体中加入5%的粘结剂和2.5%的增稠剂继续搅拌20分钟,搅拌速度为350rpm,获得第二中间体;S1-2. Add 5% binder and 2.5% thickener to the obtained first intermediate and continue stirring for 20 minutes at a stirring speed of 350 rpm to obtain the second intermediate;
S1-3、向获得的第二中间体中加入0.1%的润湿剂和0.1%的消泡剂继续搅拌20分钟,搅拌速度为150rpm,获得聚合物浆料。S1-3. Add 0.1% wetting agent and 0.1% defoamer to the obtained second intermediate and continue stirring for 20 minutes at a stirring speed of 150 rpm to obtain polymer slurry.
S2、制备相容剂:S2, preparation compatibilizer:
S2-1、将PVDF均聚物粉体及MMA(甲基丙烯酸甲酯)液体按45:55的比例投入超纯水中进行搅拌混合获得混合溶液,搅拌时间为20分钟,搅拌转速为500rpm;S2-1. Put PVDF homopolymer powder and MMA (methyl methacrylate) liquid into ultrapure water at a ratio of 45:55 and stir to obtain a mixed solution. The stirring time is 20 minutes, and the stirring speed is 500 rpm;
S2-2、将前述的混合溶液置于伽马射线环境下,充分照射后取出,获得相容剂。S2-2. Place the aforementioned mixed solution in a gamma ray environment, take it out after sufficient irradiation, and obtain a compatibilizer.
S3、对前述聚合物浆料进行改性:取5份相容剂和95份聚合物浆料进行混合搅拌,搅拌时间为20分钟,搅拌速度为500rpm,获得改性聚合物浆料。S3. Modification of the aforementioned polymer slurry: 5 parts of compatibilizer and 95 parts of polymer slurry were mixed and stirred for 20 minutes at a stirring speed of 500 rpm to obtain modified polymer slurry.
S4、制备隔膜:采用微凹版辊涂布工艺,通过涂布机将所制得的改性聚合物浆料均匀辊涂于聚烯烃隔膜上,经过70℃烘箱烘烤过后收卷备用。S4. Preparation of the separator: using a micro-gravure roll coating process, the prepared modified polymer slurry was uniformly rolled on the polyolefin separator by a coating machine, and then rolled up after being baked in a 70°C oven for later use.
本实施例以及下述实施例中的搅拌速度及搅拌时间仅做参考用,只需保证充分混合即可。The stirring speed and stirring time in this example and the following examples are for reference only, and it is only necessary to ensure sufficient mixing.
实施例二:Embodiment two:
一种高电解液浸润性的低成本锂电池隔膜,包括基膜以及涂覆于基膜任意一侧或两侧的聚合物涂层,聚合物涂层包括PVDF和PMMA材料;基膜为聚烯烃隔膜。A low-cost lithium battery separator with high electrolyte wettability, including a base film and a polymer coating coated on either side or both sides of the base film, the polymer coating includes PVDF and PMMA materials; the base film is polyolefin diaphragm.
聚合物浆料,由以下重量百分比的原料组成:混合粉体8%、相容剂10%、分散剂0.92%、增稠剂10.5%、粘结剂3.8%、润湿剂0.25%、消泡剂0.25%,混合粉体为PVDF和PMMA的混合物,PVDF:PMMA=10:90。The polymer slurry is composed of the following raw materials in weight percentage: 8% mixed powder, 10% compatibilizer, 0.92% dispersant, 10.5% thickener, 3.8% binder, 0.25% wetting agent, defoaming agent Agent 0.25%, mixed powder is a mixture of PVDF and PMMA, PVDF:PMMA=10:90.
在上述的聚合物浆料中,采用的分散剂为聚丙烯酰胺、十八碳烯胺醋酸盐、烷基季铵盐、氨基丙胺二油酸酯、聚乙二醇型多元醇、聚乙烯亚胺衍生物、油氨基油酸酯中的一种。In the above polymer slurry, the dispersant used is polyacrylamide, octadecylamine acetate, alkyl quaternary ammonium salt, aminopropylamine dioleate, polyethylene glycol polyol, polyethylene One of imine derivatives and oleyl amino oleate.
增稠剂为羧甲基纤维素钠类(CMC胶液)。The thickener is sodium carboxymethylcellulose (CMC glue).
粘结剂为氰基丙烯酸酯衍生物粘结剂、氰基丙烯酸酯聚乙二醇粘结剂、丙烯酸粘结剂、醋酸乙烯基聚合物乳胶粘结剂中的一种。The adhesive is one of cyanoacrylate derivative adhesives, cyanoacrylate polyethylene glycol adhesives, acrylic adhesives, and vinyl acetate polymer latex adhesives.
润湿剂为聚氧乙烯型表面活性剂、脂肪酸表面活性剂、硅醇类非离子表面活性剂中的一种。The wetting agent is one of polyoxyethylene surfactants, fatty acid surfactants, and silanol nonionic surfactants.
消泡剂为高碳醇脂肪酸酯复合物、聚氧乙烯聚氧丙烯季戊四醇醚、聚氧乙烯聚氧丙醇胺醚、聚氧丙烯甘油醚、聚氧丙烯聚氧乙烯甘油醚和聚二甲基硅氧烷中的一种。The defoaming agent is high carbon alcohol fatty acid ester compound, polyoxyethylene polyoxypropylene pentaerythritol ether, polyoxyethylene polyoxypropylene alcohol amine ether, polyoxypropylene glyceryl ether, polyoxypropylene polyoxyethylene glyceryl ether and polydimethyl One of the base siloxanes.
一种高电解液浸润性的低成本锂电池隔膜的制备方法,包括以下步骤:A method for preparing a low-cost lithium battery diaphragm with high electrolyte wettability, comprising the following steps:
S1、制备聚合物浆料:S1, prepare polymer slurry:
S1-1、按质量比取0.92%的分散剂和8%的混合粉体投入超纯水中搅拌60分钟,搅拌转速为600rpm,获得第一中间体;S1-1. Put 0.92% dispersant and 8% mixed powder into ultrapure water according to mass ratio and stir for 60 minutes at a stirring speed of 600rpm to obtain the first intermediate;
S1-2、向获得的第一中间体中加入3.8%的粘结剂和10.5%的增稠剂继续搅拌40分钟,搅拌速度为600rpm,获得第二中间体;S1-2. Add 3.8% binder and 10.5% thickener to the obtained first intermediate and continue stirring for 40 minutes at a stirring speed of 600 rpm to obtain the second intermediate;
S1-3、向获得的第二中间体中加入0.25%的润湿剂和0.25%的消泡剂继续搅拌30分钟,搅拌速度为200rpm,获得聚合物浆料。S1-3. Add 0.25% wetting agent and 0.25% defoamer to the obtained second intermediate and continue stirring for 30 minutes at a stirring speed of 200 rpm to obtain polymer slurry.
S2、制备相容剂:S2, preparation compatibilizer:
S2-1、将PVDF均聚物粉体及MMA(甲基丙烯酸甲酯)液体按55:45的比例投入超纯水中进行搅拌混合获得混合溶液,搅拌时间为20分钟,搅拌转速为500rpm;S2-1. Put PVDF homopolymer powder and MMA (methyl methacrylate) liquid into ultrapure water at a ratio of 55:45 and stir to obtain a mixed solution. The stirring time is 20 minutes, and the stirring speed is 500 rpm;
S2-2、将前述的混合溶液置于伽马射线环境下,充分照射后取出,获得相容剂。S2-2. Place the aforementioned mixed solution in a gamma ray environment, take it out after sufficient irradiation, and obtain a compatibilizer.
S3、对前述聚合物浆料进行改性:取10份相容剂和90份聚合物浆料进行混合搅拌,搅拌时间为20分钟,搅拌速度为500rpm,获得改性聚合物浆料。S3. Modification of the aforementioned polymer slurry: 10 parts of compatibilizer and 90 parts of polymer slurry were mixed and stirred for 20 minutes at a stirring speed of 500 rpm to obtain modified polymer slurry.
S4、制备隔膜:采用微凹版辊涂布工艺,通过涂布机将所制得的改性聚合物浆料浆料均匀辊涂于聚烯烃隔膜上,经过70℃烘箱烘烤过后收卷备用。S4. Preparation of the diaphragm: using a micro-gravure roll coating process, the prepared modified polymer slurry was evenly rolled onto the polyolefin diaphragm by a coating machine, and then rolled up after baking in a 70°C oven for later use.
实施例三:Embodiment three:
一种高电解液浸润性的低成本锂电池隔膜,包括基膜以及涂覆于基膜任意一侧或两侧的聚合物涂层,聚合物涂层包括PVDF和PMMA材料;基膜为聚烯烃隔膜。A low-cost lithium battery separator with high electrolyte wettability, including a base film and a polymer coating coated on either side or both sides of the base film, the polymer coating includes PVDF and PMMA materials; the base film is polyolefin diaphragm.
聚合物浆料,由以下重量百分比的原料组成:混合粉体13%、相容剂20%、分散剂1.2%、增稠剂13.5%、粘结剂7%、润湿剂0.35%、消泡剂0.35%,混合粉体为PVDF和PMMA的混合物,PVDF:PMMA=30:70。Polymer slurry is composed of the following raw materials in weight percentage: 13% mixed powder, 20% compatibilizer, 1.2% dispersant, 13.5% thickener, 7% binder, 0.35% wetting agent, defoaming agent Agent 0.35%, mixed powder is a mixture of PVDF and PMMA, PVDF:PMMA=30:70.
在上述的聚合物浆料中,采用的分散剂为聚丙烯酰胺、十八碳烯胺醋酸盐、烷基季铵盐、氨基丙胺二油酸酯、聚乙二醇型多元醇、聚乙烯亚胺衍生物、油氨基油酸酯中的一种。In the above polymer slurry, the dispersant used is polyacrylamide, octadecylamine acetate, alkyl quaternary ammonium salt, aminopropylamine dioleate, polyethylene glycol polyol, polyethylene One of imine derivatives and oleyl amino oleate.
增稠剂为羧甲基纤维素钠类(CMC胶液)。The thickener is sodium carboxymethylcellulose (CMC glue).
粘结剂为氰基丙烯酸酯衍生物粘结剂、氰基丙烯酸酯聚乙二醇粘结剂、丙烯酸粘结剂、醋酸乙烯基聚合物乳胶粘结剂中的一种。The adhesive is one of cyanoacrylate derivative adhesives, cyanoacrylate polyethylene glycol adhesives, acrylic adhesives, and vinyl acetate polymer latex adhesives.
润湿剂为聚氧乙烯型表面活性剂、脂肪酸表面活性剂、硅醇类非离子表面活性剂中的一种。The wetting agent is one of polyoxyethylene surfactants, fatty acid surfactants, and silanol nonionic surfactants.
消泡剂为高碳醇脂肪酸酯复合物、聚氧乙烯聚氧丙烯季戊四醇醚、聚氧乙烯聚氧丙醇胺醚、聚氧丙烯甘油醚、聚氧丙烯聚氧乙烯甘油醚和聚二甲基硅氧烷中的一种。The defoaming agent is high carbon alcohol fatty acid ester compound, polyoxyethylene polyoxypropylene pentaerythritol ether, polyoxyethylene polyoxypropylene alcohol amine ether, polyoxypropylene glyceryl ether, polyoxypropylene polyoxyethylene glyceryl ether and polydimethyl One of the base siloxanes.
一种高电解液浸润性的低成本锂电池隔膜的制备方法,包括以下步骤:A method for preparing a low-cost lithium battery diaphragm with high electrolyte wettability, comprising the following steps:
S1、制备聚合物浆料:S1, prepare polymer slurry:
S1-1、按质量比取1.2%的分散剂和13%的混合粉体1投入超纯水中搅拌120分钟,搅拌转速为900rpm,获得第一中间体;S1-1. Take 1.2% dispersant and 13% mixed powder 1 according to the mass ratio and put them into ultrapure water and stir for 120 minutes at a stirring speed of 900 rpm to obtain the first intermediate;
S1-2、向获得的第一中间体中加入7%的粘结剂和13.5%的增稠剂继续搅拌80分钟,搅拌速度为700rpm,获得第二中间体;S1-2. Add 7% binder and 13.5% thickener to the obtained first intermediate and continue to stir for 80 minutes at a stirring speed of 700rpm to obtain the second intermediate;
S1-3、向获得的第二中间体中加入0.35%的润湿剂和0.35%的消泡剂继续搅拌80分钟,搅拌速度为550rpm,获得聚合物浆料。S1-3. Add 0.35% wetting agent and 0.35% defoamer to the obtained second intermediate and continue stirring for 80 minutes at a stirring speed of 550 rpm to obtain polymer slurry.
S2、制备相容剂:S2, preparation compatibilizer:
S2-1、将PVDF均聚物粉体及MMA(甲基丙烯酸甲酯)液体按80:20的比例投入超纯水中进行搅拌混合获得混合溶液,搅拌时间为20分钟,搅拌转速为500rpm;S2-1. Put PVDF homopolymer powder and MMA (methyl methacrylate) liquid into ultrapure water at a ratio of 80:20 and stir to obtain a mixed solution. The stirring time is 20 minutes and the stirring speed is 500 rpm;
S2-2、将前述的混合溶液置于伽马射线环境下,充分照射后取出,获得相容剂。S2-2. Place the aforementioned mixed solution in a gamma ray environment, take it out after sufficient irradiation, and obtain a compatibilizer.
S3、对前述聚合物浆料进行改性:取15份相容剂和85份聚合物浆料进行混合搅拌,搅拌时间为20分钟,搅拌速度为500rpm,获得改性聚合物浆料。S3. Modification of the aforementioned polymer slurry: 15 parts of compatibilizer and 85 parts of polymer slurry were mixed and stirred for 20 minutes at a stirring speed of 500 rpm to obtain modified polymer slurry.
S4、制备隔膜:采用微凹版辊涂布工艺,通过涂布机将所制得的改性聚合物浆料浆料均匀辊涂于聚烯烃隔膜上,经过70℃烘箱烘烤过后收卷备用。S4. Preparation of the diaphragm: using a micro-gravure roll coating process, the prepared modified polymer slurry was evenly rolled onto the polyolefin diaphragm by a coating machine, and then rolled up after baking in a 70°C oven for later use.
对比例一:Comparative example one:
针对上述实施例,提供一种对比例一,该对比例是采用纯PMMA有机颗粒进行涂覆。Aiming at the above-mentioned embodiments, a comparative example 1 is provided, in which pure PMMA organic particles are used for coating.
制备浆料:Prepare slurry:
按质量比将0.92%的分散剂和8%的PMMA粉体投入超纯水中搅拌60分钟,搅拌转速为600rpm,向获得的溶液中加入3.8%的粘结剂和10.5%的增稠剂继续搅拌40分钟,搅拌速度为600rpm,继续向其中加入0.25%的润湿剂和0.25%的消泡剂继续搅拌30分钟,搅拌速度为200rpm,获得PMMA涂覆浆料。Put 0.92% dispersant and 8% PMMA powder into ultrapure water according to the mass ratio and stir for 60 minutes, the stirring speed is 600rpm, add 3.8% binder and 10.5% thickener to the obtained solution to continue Stir for 40 minutes at a stirring speed of 600 rpm, continue to add 0.25% of a wetting agent and 0.25% of an antifoaming agent and continue stirring for 30 minutes at a stirring speed of 200 rpm to obtain a PMMA coating slurry.
制备隔膜:Prepare the diaphragm:
采用微凹版辊涂布工艺,通过涂布机将所制得的PMMA吐古浆料均匀辊涂于聚烯烃隔膜上,经过70℃烘箱烘烤过后收卷备用。Using the micro-gravure roller coating process, the prepared PMMA Tugu slurry is evenly rolled on the polyolefin separator through a coating machine, and it is rolled up after being baked in a 70°C oven for later use.
对比例二:Comparative example two:
针对上述实施例,提供一种对比例2,该对比例是采用PVDF均聚物有机颗粒进行涂覆。In view of the above-mentioned embodiments, a comparative example 2 is provided, which uses PVDF homopolymer organic particles for coating.
制备浆料:Prepare slurry:
按质量比将0.92%的分散剂和8%的PVDF粉体投入超纯水中搅拌60分钟,搅拌转速为600rpm,向获得的溶液中加入3.8%的粘结剂和10.5%的增稠剂继续搅拌40分钟,搅拌速度为600rpm,继续向其中加入0.25%的润湿剂和0.25%的消泡剂继续搅拌30分钟,搅拌速度为200rpm,获得PMMA涂覆浆料。Put 0.92% dispersant and 8% PVDF powder into ultrapure water according to the mass ratio and stir for 60 minutes at a stirring speed of 600rpm, add 3.8% binder and 10.5% thickener to the obtained solution to continue Stir for 40 minutes at a stirring speed of 600 rpm, continue to add 0.25% of a wetting agent and 0.25% of an antifoaming agent and continue stirring for 30 minutes at a stirring speed of 200 rpm to obtain a PMMA coating slurry.
制备隔膜:Prepare the diaphragm:
采用微凹版辊涂布工艺,通过涂布机将所制得的PVDF涂覆浆料均匀辊涂于聚烯烃隔膜上,经过70℃烘箱烘烤过后收卷备用。Using the micro-gravure roller coating process, the prepared PVDF coating slurry is evenly rolled on the polyolefin separator through a coating machine, and it is rolled up after being baked in a 70°C oven for later use.
实施例1-3、对比例1-2制备的复合隔膜的各项性能对比见表一:The performance comparisons of the composite diaphragms prepared in Examples 1-3 and Comparative Examples 1-2 are shown in Table 1:
表一、实施例1-3、对比例1-2制备的复合隔膜的各项性能对比Table 1. Comparison of various properties of the composite diaphragms prepared in Examples 1-3 and Comparative Examples 1-2
由实验可知在实施例1-3的制备条件下,相同涂覆厚度下,相对于对比例1而言实施例1-3显然具有更好的抗穿刺强度,而相较于对比例2而言,实施例1-3又具有更好的吸液率和剥离强度,因为其吸液率更高,因此隔膜具有更好的离子电导率。It can be seen from experiments that under the preparation conditions of Examples 1-3 and the same coating thickness, Compared with Comparative Example 1, Examples 1-3 obviously have better puncture resistance, while compared with Comparative Example 2 , Examples 1-3 again have better liquid uptake and peel strength because of their higher liquid uptake and thus better ionic conductivity of the separator.
以上所述,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揭露的技术范围内,根据本发明的技术方案及其发明构思加以等同替换或改变,都应涵盖在本发明的保护范围之内。The above is only a preferred embodiment of the present invention, but the scope of protection of the present invention is not limited thereto, any person familiar with the technical field within the technical scope disclosed in the present invention, according to the technical solution of the present invention Any equivalent replacement or change of the inventive concepts thereof shall fall within the protection scope of the present invention.
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