CN103824989B - A kind of PEG/PVC composite diaphragm and its preparation method and application - Google Patents
A kind of PEG/PVC composite diaphragm and its preparation method and application Download PDFInfo
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- CN103824989B CN103824989B CN201410099679.4A CN201410099679A CN103824989B CN 103824989 B CN103824989 B CN 103824989B CN 201410099679 A CN201410099679 A CN 201410099679A CN 103824989 B CN103824989 B CN 103824989B
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- 239000002131 composite material Substances 0.000 title claims abstract description 14
- 238000002360 preparation method Methods 0.000 title claims abstract description 11
- 239000007822 coupling agent Substances 0.000 claims abstract description 13
- 239000000945 filler Substances 0.000 claims abstract description 9
- XUIMIQQOPSSXEZ-UHFFFAOYSA-N Silicon Chemical compound [Si] XUIMIQQOPSSXEZ-UHFFFAOYSA-N 0.000 claims abstract description 8
- 229910052710 silicon Inorganic materials 0.000 claims abstract description 8
- 239000010703 silicon Substances 0.000 claims abstract description 8
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims description 17
- ZMXDDKWLCZADIW-UHFFFAOYSA-N N,N-Dimethylformamide Chemical compound CN(C)C=O ZMXDDKWLCZADIW-UHFFFAOYSA-N 0.000 claims description 14
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 13
- 239000000243 solution Substances 0.000 claims description 10
- 238000006116 polymerization reaction Methods 0.000 claims description 6
- 239000011347 resin Substances 0.000 claims description 6
- 229920005989 resin Polymers 0.000 claims description 6
- 239000007864 aqueous solution Substances 0.000 claims description 5
- 239000007788 liquid Substances 0.000 claims description 4
- WYURNTSHIVDZCO-UHFFFAOYSA-N Tetrahydrofuran Chemical compound C1CCOC1 WYURNTSHIVDZCO-UHFFFAOYSA-N 0.000 claims description 3
- JHIVVAPYMSGYDF-UHFFFAOYSA-N cyclohexanone Chemical group O=C1CCCCC1 JHIVVAPYMSGYDF-UHFFFAOYSA-N 0.000 claims description 3
- 238000004132 cross linking Methods 0.000 claims description 2
- 239000010413 mother solution Substances 0.000 claims description 2
- 238000001556 precipitation Methods 0.000 claims description 2
- 229920000915 polyvinyl chloride Polymers 0.000 claims 15
- 239000004800 polyvinyl chloride Substances 0.000 claims 15
- 239000006166 lysate Substances 0.000 claims 3
- 230000001112 coagulating effect Effects 0.000 claims 1
- 238000007654 immersion Methods 0.000 claims 1
- WFKAJVHLWXSISD-UHFFFAOYSA-N isobutyramide Chemical compound CC(C)C(N)=O WFKAJVHLWXSISD-UHFFFAOYSA-N 0.000 claims 1
- 238000007711 solidification Methods 0.000 claims 1
- 230000008023 solidification Effects 0.000 claims 1
- 239000003792 electrolyte Substances 0.000 abstract description 16
- 239000011148 porous material Substances 0.000 abstract description 13
- 239000002994 raw material Substances 0.000 abstract description 11
- 238000002156 mixing Methods 0.000 abstract description 3
- 230000002209 hydrophobic effect Effects 0.000 abstract description 2
- 238000005260 corrosion Methods 0.000 abstract 1
- 230000007797 corrosion Effects 0.000 abstract 1
- 239000000463 material Substances 0.000 abstract 1
- 150000003376 silicon Chemical class 0.000 abstract 1
- 229920001223 polyethylene glycol Polymers 0.000 description 12
- 239000002253 acid Substances 0.000 description 7
- 238000003756 stirring Methods 0.000 description 7
- 239000005909 Kieselgur Substances 0.000 description 6
- 238000000034 method Methods 0.000 description 6
- 238000005516 engineering process Methods 0.000 description 4
- 238000009736 wetting Methods 0.000 description 4
- 230000008901 benefit Effects 0.000 description 3
- 239000000084 colloidal system Substances 0.000 description 3
- 239000003292 glue Substances 0.000 description 3
- 238000010438 heat treatment Methods 0.000 description 3
- 239000000203 mixture Substances 0.000 description 3
- 239000000377 silicon dioxide Substances 0.000 description 3
- 238000005266 casting Methods 0.000 description 2
- 238000009826 distribution Methods 0.000 description 2
- 125000002887 hydroxy group Chemical group [H]O* 0.000 description 2
- 239000012452 mother liquor Substances 0.000 description 2
- 238000005191 phase separation Methods 0.000 description 2
- 230000008569 process Effects 0.000 description 2
- 230000001105 regulatory effect Effects 0.000 description 2
- 238000001878 scanning electron micrograph Methods 0.000 description 2
- 239000002904 solvent Substances 0.000 description 2
- FXHOOIRPVKKKFG-UHFFFAOYSA-N N,N-Dimethylacetamide Chemical compound CN(C)C(C)=O FXHOOIRPVKKKFG-UHFFFAOYSA-N 0.000 description 1
- 239000008118 PEG 6000 Substances 0.000 description 1
- 229920002538 Polyethylene Glycol 20000 Polymers 0.000 description 1
- 229920002584 Polyethylene Glycol 6000 Polymers 0.000 description 1
- RTAQQCXQSZGOHL-UHFFFAOYSA-N Titanium Chemical compound [Ti] RTAQQCXQSZGOHL-UHFFFAOYSA-N 0.000 description 1
- 238000005345 coagulation Methods 0.000 description 1
- 230000015271 coagulation Effects 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 230000001276 controlling effect Effects 0.000 description 1
- MTHSVFCYNBDYFN-UHFFFAOYSA-N diethylene glycol Chemical compound OCCOCCO MTHSVFCYNBDYFN-UHFFFAOYSA-N 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005429 filling process Methods 0.000 description 1
- 229910021485 fumed silica Inorganic materials 0.000 description 1
- 239000003365 glass fiber Substances 0.000 description 1
- 229920001477 hydrophilic polymer Polymers 0.000 description 1
- 230000008676 import Effects 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000001000 micrograph Methods 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 125000005375 organosiloxane group Chemical group 0.000 description 1
- 238000005192 partition Methods 0.000 description 1
- 235000012239 silicon dioxide Nutrition 0.000 description 1
- 238000013517 stratification Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- YLQBMQCUIZJEEH-UHFFFAOYSA-N tetrahydrofuran Natural products C=1C=COC=1 YLQBMQCUIZJEEH-UHFFFAOYSA-N 0.000 description 1
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
- 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
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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
- 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
- H01M50/446—Composite material consisting of a mixture of organic and inorganic materials
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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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- Chemical & Material Sciences (AREA)
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- Chemical Kinetics & Catalysis (AREA)
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- General Chemical & Material Sciences (AREA)
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Abstract
本发明涉及一种PEG/PVC复合隔板及其制备方法和应用。该隔板其原料按质量分数计包括:PEG 1%‑30%,PVC 15%‑50%,硅填料20%‑70%,偶联剂0.01%‑1%。制备方法为:以PVC为主,构筑三维微孔网状结构,保证隔板的基本机械强度和耐腐蚀性;共混加入PEG以调节三维网状的孔隙大小和改善疏水PVC材料表面的电解液亲和性;再辅以偶联剂改性硅填料,进一步强化隔板的机械性能、电解液亲和性能、孔隙曲折性。所制得的隔板在秉承了微孔PVC隔板的较强机械性能和平均孔径小特点的基础上,更好地改善了与胶体电解液的亲和性。The invention relates to a PEG/PVC composite separator and a preparation method and application thereof. The raw materials of the separator include PEG 1%-30%, PVC 15%-50%, silicon filler 20%-70%, and coupling agent 0.01%-1%. The preparation method is: mainly use PVC to build a three-dimensional microporous network structure to ensure the basic mechanical strength and corrosion resistance of the separator; blending and adding PEG to adjust the pore size of the three-dimensional network and improve the electrolyte on the surface of the hydrophobic PVC material Affinity; supplemented with a coupling agent modified silicon filler, the mechanical properties, electrolyte affinity, and pore tortuosity of the separator are further enhanced. On the basis of adhering to the strong mechanical properties and small average pore diameter of the microporous PVC separator, the prepared separator better improves the affinity with the colloidal electrolyte.
Description
技术领域technical field
本发明属于化学电源领域,具体涉及一种PEG/PVC复合隔板及其制备方法和应用。The invention belongs to the field of chemical power sources, and in particular relates to a PEG/PVC composite separator and a preparation method and application thereof.
背景技术Background technique
阀控式铅酸蓄电池依靠两种不同的方式固定电解液,一种是采用玻璃纤维隔板的AGM技术,另一种是采用微孔PVC隔板的胶体固定技术。两种技术的隔板各有自己的优缺点:AGM隔板孔隙率高、电阻小、电解液亲和性好、价格低廉,但孔径太大、机械强度偏低、易导致酸分层;微孔PVC隔板机械强度高、孔径小,但相对于AGM隔板来说孔隙率偏低、电阻偏大、电解液亲和性不够好、价格昂贵。采用胶体技术的电池由于具有寿命长,运行稳定等AGM电池不具备的优点,因此应用越来越广泛。但是,出于成本考虑,AGM电池还是被广泛的使用着。国内甚至出现了结合AGM隔板和胶体电解液的低成本胶体电池,这种电池由于隔板太厚,胶体电解液难以灌入,灌胶后电池内部存在大量空气,最终电池性能没有达到预想的好效果。Valve-regulated lead-acid batteries rely on two different methods to fix the electrolyte, one is AGM technology using glass fiber separators, and the other is colloid fixing technology using microporous PVC separators. The separators of the two technologies have their own advantages and disadvantages: the AGM separator has high porosity, low resistance, good electrolyte affinity, and low price, but the pore size is too large, the mechanical strength is low, and it is easy to cause acid stratification; The porous PVC separator has high mechanical strength and small pore size, but compared with the AGM separator, the porosity is relatively low, the resistance is relatively large, the affinity of the electrolyte is not good enough, and the price is expensive. Batteries using colloidal technology are more and more widely used because of their advantages such as long life and stable operation that AGM batteries do not have. However, due to cost considerations, AGM batteries are still widely used. There are even low-cost colloidal batteries combined with AGM separators and colloidal electrolytes in China. Because the separators are too thick, the colloidal electrolytes are difficult to pour in. After the glue is filled, there is a lot of air inside the battery, and the final battery performance does not meet expectations. Good effect.
隔板作为在电池中发挥重要作用的“第三极板”,在胶体阀控式铅酸蓄电池中承担了更多的任务。优质的胶体电池隔板除了应具有孔隙率高、机械强度好、孔径小、体积小、耐强酸等基本特征外,还特别要求具有良好的胶体电解液亲和性。胶体电解液亲和性包括两个方面:一方面是在灌胶过程中应具有良好的润湿性,能快速灌胶、排出隔板中的空气;另一方面是在胶体形成凝胶的过程中,隔板能参与构筑三维凝胶结构,使隔板与电解液凝胶牢固结合,避免随着水的分解在隔板与电解液凝胶界面处产生裂缝。As the "third plate" that plays an important role in the battery, the separator takes on more tasks in the colloidal valve-regulated lead-acid battery. In addition to the basic characteristics of high porosity, good mechanical strength, small pore size, small volume, and strong acid resistance, high-quality gel battery separators are also required to have good affinity for colloidal electrolytes. The affinity of the colloidal electrolyte includes two aspects: on the one hand, it should have good wettability during the glue filling process, which can quickly fill the glue and discharge the air in the separator; on the other hand, it should be in the process of forming a gel Among them, the separator can participate in the construction of a three-dimensional gel structure, so that the separator and the electrolyte gel can be firmly combined to avoid cracks at the interface between the separator and the electrolyte gel as the water decomposes.
现在国内外胶体铅酸蓄电池普遍使用微孔PVC隔板,能满足隔板对孔径大小、机械强度、孔隙率、耐强酸的要求,隔板中所含的沉淀二氧化硅也能赋予本身疏水的PVC隔板一定的润湿性和胶体亲和性。但是二氧化硅的加入是有限的,微孔PVC隔板只是部分具有电解液亲和性,隔板本身相对于AGM隔板还是电阻太大,并且这种隔板制备工艺复杂、价格昂贵,目前需依赖进口。At present, colloidal lead-acid batteries at home and abroad generally use microporous PVC separators, which can meet the requirements of the separator for pore size, mechanical strength, porosity, and strong acid resistance. The precipitated silica contained in the separator can also endow itself with hydrophobic properties. PVC separator has certain wettability and colloid affinity. However, the addition of silicon dioxide is limited, and the microporous PVC separator is only partially compatible with the electrolyte. Compared with the AGM separator, the separator itself still has too much resistance, and the preparation process of this separator is complicated and expensive. Need to rely on imports.
发明内容Contents of the invention
本发明基于国内胶体电池行业的现状,针对胶体电池隔板提出的特殊要求,研制出了生产成本大大低于进口微孔PVC隔板的PEG/PVC复合隔板。此种PEG/PVC复合隔板在保证隔板基本性能的前提下,具备良好胶体电解液亲和性。Based on the current situation of the domestic colloidal battery industry, and aiming at the special requirements of the colloidal battery separator, the present invention develops a PEG/PVC composite separator whose production cost is much lower than that of imported microporous PVC separators. This kind of PEG/PVC composite separator has good colloidal electrolyte affinity under the premise of ensuring the basic performance of the separator.
一种PEG/PVC复合隔板,其原料按质量分数计为:PEG 1%-30%,PVC 15%-50%,硅填料 20%-70%,以上各原料质量分数之和为100%。A PEG/PVC composite partition, the raw materials of which are calculated by mass fraction: PEG 1%-30%, PVC 15%-50%, silicon filler 20%-70%, and the sum of the mass fractions of the above raw materials is 100%.
所述的PEG为聚合度在6000以上的PEG。The PEG is PEG with a degree of polymerization above 6000.
所述的PVC为聚合度在1200-1800的PVC糊树脂、聚合度在1800以上的PVC树脂、交联度为1%-10%的PVC树脂中的一种或多种。The PVC is one or more of PVC paste resins with a polymerization degree of 1200-1800, PVC resins with a polymerization degree of more than 1800, and PVC resins with a crosslinking degree of 1%-10%.
所述的硅填料为比表面为200-500m2/g的气相二氧化硅、200目以上的硅藻土、200目以上的沉淀二氧化硅中的一种或多种。The silicon filler is one or more of fumed silica with a specific surface area of 200-500m 2 /g, diatomite with a mesh size above 200, and precipitated silica with a mesh size above 200.
一种制备如上所述的PEG/PVC复合隔板的方法,将PVC、PEG、硅填料、偶联剂混合,加入溶解液制成铸板液,于20℃-100℃加热搅拌2-5h后,注入密封容器中;然后置于20℃-70℃水浴中静置脱泡2-4h,通过刮刀将铸板液刮板成片,在空气中静置预分相10-600s;然后在凝固浴水溶液中浸没沉淀得到初级隔板,最后将初级隔板热压成波纹形状并烘干制得隔板。A method for preparing the above-mentioned PEG/PVC composite separator, mixing PVC, PEG, silicon filler, and coupling agent, adding a solution to make a casting liquid, heating and stirring at 20°C-100°C for 2-5h , into a sealed container; then put it in a water bath at 20°C-70°C for 2-4h, scrape the casting liquid into pieces with a scraper, and stand in the air for pre-phase separation for 10-600s; then solidify The primary separator is obtained by immersing the precipitation in the bath solution, and finally the primary separator is hot-pressed into a corrugated shape and dried to obtain the separator.
所述的偶联剂为有机硅氧烷、钛酸酯偶联剂中的一种或两种,其用量为硅填料质量的0.1-1%。The coupling agent is one or both of organosiloxane and titanate coupling agent, and its dosage is 0.1-1% of the silicon filler mass.
所述的溶解液为二甲基甲酰胺、二甲基乙酰胺、四氢呋喃、环己酮中的一种。The dissolving solution is one of dimethylformamide, dimethylacetamide, tetrahydrofuran and cyclohexanone.
所述的凝固浴溶液为溶解液质量含量为0%-50%的水溶液。The coagulation bath solution is an aqueous solution with a mass content of 0%-50% of the solution.
如上所述的PEG/PVC复合隔板的应用,用于铅酸胶体蓄电池。The application of the PEG/PVC composite separator as mentioned above is used for lead-acid gel batteries.
本发明的显著优点是:Significant advantage of the present invention is:
(1)通过共混添加亲水聚合物PEG,使得隔板中的PVC网络表面具有良好的亲水性;(1) The hydrophilic polymer PEG is added by blending, so that the surface of the PVC network in the separator has good hydrophilicity;
(2)隔板中所含的PEG表面的羟基和硅填料表面的羟基能和电解液中的胶体大量键合,共同构筑凝胶,使得隔板与电解液凝胶长时间牢牢结合在一起;(2) The hydroxyl groups on the surface of PEG contained in the separator and the hydroxyl groups on the surface of the silicon filler can bond with the colloid in the electrolyte in large quantities to form a gel together, so that the separator and the electrolyte gel can be firmly combined for a long time ;
(3)通过对PVC/PEG/溶剂/非溶剂四组分体系相分离过程的调控,能够获得孔隙率高、孔径小且迂回合理的孔隙结构。(3) By controlling the phase separation process of the PVC/PEG/solvent/non-solvent four-component system, a pore structure with high porosity, small pore size and reasonable circuitousness can be obtained.
附图说明Description of drawings
图1 为实施例1制备的隔板表面扫描电镜图;Fig. 1 is the SEM image of the separator surface prepared in Example 1;
图2 为实施例2制备的隔板表面扫描电镜图;Fig. 2 is the SEM image of the separator surface prepared in Example 2;
图3 为实施例3制备的隔板表面扫描电镜图。FIG. 3 is a scanning electron microscope image of the separator surface prepared in Example 3.
具体实施方式detailed description
下面通过具体实施例对本发明的技术方案做进一步说明。本发明采用的原材料可在市场购得,或可用本领域已知的方法合成。The technical solutions of the present invention will be further described below through specific examples. The raw materials used in the present invention can be purchased in the market, or can be synthesized by methods known in the art.
实施例1Example 1
PVC23wt%,PEG9wt%,硅藻土68wt%。PVC23wt%, PEG9wt%, diatomaceous earth 68wt%.
1.称取5gPVC和2gPEG6000溶解于45gDMF溶液中,加入0.39g质量含量为1%的偶联剂(KH-550)母液,100℃加热搅拌2 h;1. Weigh 5g of PVC and 2g of PEG6000 and dissolve in 45g of DMF solution, add 0.39g of mother liquor of coupling agent (KH-550) with a mass content of 1%, and heat and stir at 100°C for 2 hours;
2.称取15g硅藻土加入,继续加热搅拌1h;2. Weigh 15g of diatomaceous earth and add, continue heating and stirring for 1h;
3.将混合物倒入密封容器,置于40℃水浴中静置脱泡3h;3. Pour the mixture into a sealed container and place it in a water bath at 40°C for 3 hours for defoaming;
4.用500μm刮刀刮制成片,静置600s;4. Scrape with a 500μm scraper to make a sheet, and let it stand for 600s;
5.浸入70℃水中脱模成片,3h后取出,60℃烘干;5. Immerse in water at 70°C to release the mold into pieces, take it out after 3 hours, and dry at 60°C;
所得隔板表面形貌如图1所示,具有较高的孔隙率和比较均匀的孔径分布,孔径大多在1μm到10μm之间。孔隙率为80.0%,拉伸强度为5Mp,水滴到隔板上的初始接触角为56°,被水润湿时间为2.5s。The surface morphology of the obtained separator is shown in FIG. 1 , which has a relatively high porosity and a relatively uniform pore size distribution, and the pore size is mostly between 1 μm and 10 μm. The porosity is 80.0%, the tensile strength is 5Mp, the initial contact angle of water droplets on the separator is 56°, and the wetting time by water is 2.5s.
实施例2Example 2
PVC30wt%,PEG18wt%,硅藻土52wt%。PVC30wt%, PEG18wt%, diatomaceous earth 52wt%.
1.称取10gPVC和6gPEG10000溶解于90gDMF溶液中,加入0.13g质量含量为1%的偶联剂(KH-550)母液,70℃加热搅拌3h;1. Weigh 10g of PVC and 6g of PEG10000 and dissolve in 90g of DMF solution, add 0.13g of 1% coupling agent (KH-550) mother liquor, heat and stir at 70°C for 3h;
2.称取17g硅藻土加入,继续加热搅拌1h;2. Weigh 17g of diatomaceous earth and add, continue to heat and stir for 1h;
3.将混合物倒入密封容器,置于20℃水浴中静置脱泡4h;3. Pour the mixture into a sealed container and place it in a water bath at 20°C for defoaming for 4 hours;
4.用750μm刮刀刮制成片,静置300s;4. Scrape with a 750μm scraper to make a sheet, and let it stand for 300s;
5.浸入25℃质量含量为20%的DMF水溶液中,脱模成片,3h后取出60℃烘干;5. Immerse in 25°C DMF aqueous solution with a mass content of 20%, demold it into pieces, take it out after 3 hours and dry it at 60°C;
所得隔板表面形貌如图2所示,具有较高的孔隙率和比较均匀的孔径分布,为1μm到10μm之间。孔隙率为79.5%,拉伸强度为5Mp,水滴到隔板上的初始接触角为35°,被水润湿时间为1.5s。The surface morphology of the obtained separator is shown in FIG. 2 , which has a relatively high porosity and a relatively uniform pore size distribution, which is between 1 μm and 10 μm. The porosity is 79.5%, the tensile strength is 5Mp, the initial contact angle of water droplets on the separator is 35°, and the wetting time by water is 1.5s.
实施例3Example 3
PVC49wt%,PEG18wt%,硅藻土33wt%。PVC49wt%, PEG18wt%, diatomaceous earth 33wt%.
1.称取30gPVC和11gPEG20000溶解于120gDMF溶液中,加入0.13g质量含量为1%的偶联剂(KH-550)母液,50℃加热搅拌5h;1. Weigh 30g of PVC and 11g of PEG20000 and dissolve in 120g of DMF solution, add 0.13g of 1% coupling agent (KH-550) mother solution, heat and stir at 50°C for 5h;
2.称取20g硅藻土加入,继续加热搅拌1h;2. Weigh 20g of diatomaceous earth and add, continue heating and stirring for 1h;
3.将混合物倒入密封容器,置于70℃水浴中静置脱泡3h;3. Pour the mixture into a sealed container and place it in a water bath at 70°C for 3 hours for defoaming;
4.用750μm刮刀刮制成片,静置10s;4. Scrape with a 750μm scraper to make a sheet, and let it stand for 10s;
5.浸入90℃水溶液脱模成片,3h后取出60℃烘干;5. Immerse in a 90°C aqueous solution to release the mold into pieces, take it out after 3 hours and dry it at 60°C;
所得隔板表面形貌如图3所示,孔隙率为77.0%,拉伸强度为6Mp,水滴到隔板上的初始接触角为58°,被水润湿时间为2s。The surface morphology of the obtained separator is shown in Figure 3. The porosity is 77.0%, the tensile strength is 6Mp, the initial contact angle of water droplets on the separator is 58°, and the wetting time by water is 2s.
三个实施例最终得到的隔板孔隙率在75%以上,最大孔径不到10μm,拉伸强度达5Mp以上,厚度可以制成0.5mm-1mm,被水润湿时间小于3s,应用于胶体电池后,电池使用性能达到采用进口隔板装配的电池水准。The final separator obtained in the three examples has a porosity of more than 75%, a maximum pore diameter of less than 10 μm, a tensile strength of more than 5Mp, a thickness of 0.5mm-1mm, and a water-wetting time of less than 3s. It is used in colloidal batteries Finally, the performance of the battery reaches the level of batteries assembled with imported separators.
以上所述仅为本发明的较佳实施例,凡依本发明申请专利范围所做的均等变化与修饰,皆应属本发明的涵盖范围。The above descriptions are only preferred embodiments of the present invention, and all equivalent changes and modifications made according to the scope of the patent application of the present invention shall fall within the scope of the present invention.
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