CN101787141A - Method for preparing proton exchange membrane with polyvinylidene fluoride grafted and grafting copolymerized with 2-acrylamido-2-methylpropanesulfonic acid - Google Patents
Method for preparing proton exchange membrane with polyvinylidene fluoride grafted and grafting copolymerized with 2-acrylamido-2-methylpropanesulfonic acid Download PDFInfo
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- 239000012528 membrane Substances 0.000 title claims abstract description 49
- 239000002033 PVDF binder Substances 0.000 title claims abstract description 31
- 229920002981 polyvinylidene fluoride Polymers 0.000 title claims abstract description 31
- XHZPRMZZQOIPDS-UHFFFAOYSA-N 2-Methyl-2-[(1-oxo-2-propenyl)amino]-1-propanesulfonic acid Chemical compound OS(=O)(=O)CC(C)(C)NC(=O)C=C XHZPRMZZQOIPDS-UHFFFAOYSA-N 0.000 title claims abstract description 15
- 229920000536 2-Acrylamido-2-methylpropane sulfonic acid Polymers 0.000 title claims description 11
- 238000000034 method Methods 0.000 title description 6
- 238000003756 stirring Methods 0.000 claims abstract description 10
- DZSVIVLGBJKQAP-UHFFFAOYSA-N 1-(2-methyl-5-propan-2-ylcyclohex-2-en-1-yl)propan-1-one Chemical group CCC(=O)C1CC(C(C)C)CC=C1C DZSVIVLGBJKQAP-UHFFFAOYSA-N 0.000 claims abstract description 7
- SECXISVLQFMRJM-UHFFFAOYSA-N N-Methylpyrrolidone Chemical compound CN1CCCC1=O SECXISVLQFMRJM-UHFFFAOYSA-N 0.000 claims abstract description 7
- 238000002360 preparation method Methods 0.000 claims abstract description 7
- 238000005266 casting Methods 0.000 claims abstract description 4
- 239000011521 glass Substances 0.000 claims abstract description 4
- 229920000578 graft copolymer Polymers 0.000 claims abstract description 4
- 239000000243 solution Substances 0.000 claims description 19
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 14
- ROOXNKNUYICQNP-UHFFFAOYSA-N ammonium persulfate Chemical compound [NH4+].[NH4+].[O-]S(=O)(=O)OOS([O-])(=O)=O ROOXNKNUYICQNP-UHFFFAOYSA-N 0.000 claims description 10
- 239000008367 deionised water Substances 0.000 claims description 7
- 229910021641 deionized water Inorganic materials 0.000 claims description 7
- 229910001870 ammonium persulfate Inorganic materials 0.000 claims description 5
- POWFTOSLLWLEBN-UHFFFAOYSA-N tetrasodium;silicate Chemical compound [Na+].[Na+].[Na+].[Na+].[O-][Si]([O-])([O-])[O-] POWFTOSLLWLEBN-UHFFFAOYSA-N 0.000 claims description 5
- 239000011259 mixed solution Substances 0.000 claims description 4
- 229920001519 homopolymer Polymers 0.000 claims description 3
- 239000007788 liquid Substances 0.000 claims description 3
- 239000012299 nitrogen atmosphere Substances 0.000 claims description 2
- 239000002994 raw material Substances 0.000 claims description 2
- 238000002156 mixing Methods 0.000 claims 2
- IRLPACMLTUPBCL-KQYNXXCUSA-N 5'-adenylyl sulfate Chemical compound C1=NC=2C(N)=NC=NC=2N1[C@@H]1O[C@H](COP(O)(=O)OS(O)(=O)=O)[C@@H](O)[C@H]1O IRLPACMLTUPBCL-KQYNXXCUSA-N 0.000 claims 1
- 239000002001 electrolyte material Substances 0.000 abstract description 3
- 239000003999 initiator Substances 0.000 abstract description 3
- 238000011031 large-scale manufacturing process Methods 0.000 abstract description 3
- 150000003377 silicon compounds Chemical class 0.000 abstract description 2
- 239000004020 conductor Substances 0.000 abstract 1
- 238000001035 drying Methods 0.000 abstract 1
- 238000010438 heat treatment Methods 0.000 abstract 1
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 51
- 239000000446 fuel Substances 0.000 description 14
- 230000008961 swelling Effects 0.000 description 11
- 230000035699 permeability Effects 0.000 description 9
- 150000003254 radicals Chemical class 0.000 description 6
- 238000004519 manufacturing process Methods 0.000 description 4
- 229920000172 poly(styrenesulfonic acid) Polymers 0.000 description 3
- 229940005642 polystyrene sulfonic acid Drugs 0.000 description 3
- 230000005855 radiation Effects 0.000 description 3
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- 229920000557 Nafion® Polymers 0.000 description 2
- PPBRXRYQALVLMV-UHFFFAOYSA-N Styrene Chemical compound C=CC1=CC=CC=C1 PPBRXRYQALVLMV-UHFFFAOYSA-N 0.000 description 2
- 239000007864 aqueous solution Substances 0.000 description 2
- 238000009792 diffusion process Methods 0.000 description 2
- 239000003014 ion exchange membrane Substances 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- -1 poly(2-acrylamido-2-methylpropanesulfonic acid) Polymers 0.000 description 2
- BQCIDUSAKPWEOX-UHFFFAOYSA-N 1,1-Difluoroethene Chemical compound FC(F)=C BQCIDUSAKPWEOX-UHFFFAOYSA-N 0.000 description 1
- LSNNMFCWUKXFEE-UHFFFAOYSA-M Bisulfite Chemical compound OS([O-])=O LSNNMFCWUKXFEE-UHFFFAOYSA-M 0.000 description 1
- 241000577418 Polybia Species 0.000 description 1
- 239000004793 Polystyrene Substances 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 239000012298 atmosphere Substances 0.000 description 1
- 230000004888 barrier function Effects 0.000 description 1
- 230000000052 comparative effect Effects 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000003792 electrolyte Substances 0.000 description 1
- XUCNUKMRBVNAPB-UHFFFAOYSA-N fluoroethene Chemical compound FC=C XUCNUKMRBVNAPB-UHFFFAOYSA-N 0.000 description 1
- UQSQSQZYBQSBJZ-UHFFFAOYSA-N fluorosulfonic acid Chemical compound OS(F)(=O)=O UQSQSQZYBQSBJZ-UHFFFAOYSA-N 0.000 description 1
- 239000012456 homogeneous solution Substances 0.000 description 1
- 150000002500 ions Chemical class 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 229920002223 polystyrene Polymers 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 238000012827 research and development Methods 0.000 description 1
- 239000002904 solvent Substances 0.000 description 1
- 238000006277 sulfonation reaction Methods 0.000 description 1
- 125000000542 sulfonic acid group Chemical group 0.000 description 1
Classifications
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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
- Y02E60/30—Hydrogen technology
- Y02E60/50—Fuel cells
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Abstract
本发明涉及一种聚偏氟乙烯枝接共混聚2-丙烯酰胺基-2-甲基丙磺酸质子交换膜的制备方法,属于电池电解质材料领域。本发明首先将硅化合物溶于含水的N-甲基吡咯烷酮溶液,再将聚偏氟乙烯PVDF和2-丙烯酰胺基-2-甲基丙磺酸(AMPS)加入该溶液中,添加引发剂,加热搅拌,将溶液浇铸到洁净的玻璃板上并烘干、脱膜,得改性聚偏氟乙烯与聚2-丙烯酰胺基-2-甲基丙磺酸接枝共聚物膜;本发明制备的质子交换膜,不但具有很好的质子导电件,而目便于进行大规模生产。The invention relates to a preparation method of a polyvinylidene fluoride graft blended poly 2-acrylamide-2-methylpropanesulfonic acid proton exchange membrane, belonging to the field of battery electrolyte materials. In the present invention, the silicon compound is first dissolved in an aqueous N-methylpyrrolidone solution, then polyvinylidene fluoride PVDF and 2-acrylamido-2-methylpropanesulfonic acid (AMPS) are added to the solution, and an initiator is added. heating and stirring, casting the solution onto a clean glass plate, drying, and stripping to obtain a modified polyvinylidene fluoride and poly 2-acrylamide-2-methylpropanesulfonic acid graft copolymer film; prepared by the present invention The proton exchange membrane not only has a good proton conductor, but also facilitates large-scale production.
Description
技术领域technical field
本发明涉及一种聚偏氟乙烯枝接共混聚2-丙烯酰胺基-2-甲基丙磺酸质子交换膜的制备方法,属于电池电解质材料领域。The invention relates to a preparation method of a polyvinylidene fluoride graft blended poly 2-acrylamide-2-methylpropanesulfonic acid proton exchange membrane, belonging to the field of battery electrolyte materials.
背景技术Background technique
在质子交换膜燃料电池及直接甲醇燃料电池中,质子交换膜电解质是电池中的关键材料,质子交换膜的性能将直接影响电池的性能,因此,质子交换膜一直是燃料电池研发的重点课题。目前,广泛使用的质子交换膜主要是由美国杜邦公司生产的全氟磺酸离子交换膜(Nafion膜)。这种质子交换膜具有良好的质子导电性,但是由于是全氟离子交换膜,因此生产成本较贵,特别是这种质子交换膜对甲醇等液体燃料的阻隔性差,溶胀率大,不利于制作有机燃料的燃料电池。为了解决这一问题,已开发出一些新的质子交换膜,如聚偏氟乙烯磺酸质子交换膜膜,这种膜不但具有很好的质子导电性,同时还具有较低的甲醇渗透性,因此是一种理想的直接甲醇燃料电池用质子交换膜。In proton exchange membrane fuel cells and direct methanol fuel cells, the proton exchange membrane electrolyte is the key material in the battery, and the performance of the proton exchange membrane will directly affect the performance of the battery. Therefore, the proton exchange membrane has always been a key topic in the research and development of fuel cells. At present, the widely used proton exchange membrane is mainly the perfluorosulfonic acid ion exchange membrane (Nafion membrane) produced by DuPont Company of the United States. This kind of proton exchange membrane has good proton conductivity, but because it is a perfluorinated ion exchange membrane, the production cost is relatively expensive, especially this kind of proton exchange membrane has poor barrier property to liquid fuels such as methanol and has a large swelling rate, which is not conducive to production Fuel cells for organic fuels. In order to solve this problem, some new proton exchange membranes have been developed, such as polyvinylidene fluoride sulfonic acid proton exchange membrane, which not only has good proton conductivity, but also has low methanol permeability, Therefore, it is an ideal proton exchange membrane for direct methanol fuel cells.
制备聚偏氟乙烯磺酸膜的关键问题是怎样使聚偏氟乙烯脱去HF产生活性点,目前所采用的方法是,先利用甲基吡咯烷酮作溶剂,用溶液浇注的方法将聚偏氟乙烯制成膜,再利用高能电子辐射照射,使其产生自由基,在自由基产生后立即将膜放入到配有引发剂的苯乙烯的溶液中进行枝接,一定时间后将已枝接的膜进行磺化处理,从而得到了聚偏氟乙烯枝接聚苯乙烯磺酸的质子交换膜。根据射线照射时间及枝接时间的不同,膜的质子导电性以及膜的甲醇渗透性均不同。在一个合适的条件下,这种枝接膜具有很高的质子导电性能。因此这种膜被认为是一种理想的质子交换膜燃料电池的电解质材料。The key issue in the preparation of polyvinylidene fluoride sulfonic acid membrane is how to remove HF from polyvinylidene fluoride to generate active points. The current method is to use methyl pyrrolidone as solvent first, and pour polyvinylidene fluoride into the film by solution casting. Make a film, and then irradiate it with high-energy electron radiation to generate free radicals. Immediately after the free radicals are generated, the film is placed in a solution of styrene with an initiator for grafting. After a certain period of time, the grafted The membrane is sulfonated to obtain a proton exchange membrane grafted with polyvinylidene fluoride and polystyrene sulfonic acid. The proton conductivity of the membrane and the methanol permeability of the membrane are different according to the radiation time and the grafting time. Under a suitable condition, the grafted film has high proton conductivity. Therefore, this membrane is considered to be an ideal electrolyte material for proton exchange membrane fuel cells.
上述质子交换膜燃料电池中,质子交换膜一直是影响燃料电池的关键材料,质子交换膜不但起着传导离子的作用,同时还起着隔离燃料的作用。然而,在直接甲醇燃料电池中使用甲醇作为燃料,因此电池中的质子交换膜要求不但具有很高的质子导电性,同时应具备很低的甲醇渗透性,这就使目前广泛使用的全氟磺酸质子交换膜不再适用。为了能得到适用于直接甲醇燃料电池的质子交换膜,人们提出使用聚偏氟乙烯枝接聚苯乙烯磺酸膜,但是这种膜由于必须使用射线来激发自由基,另一方面接枝到聚偏氟乙烯膜上的聚苯乙烯还需磺化,这种方法工艺复杂不利于大规模生产。In the above proton exchange membrane fuel cell, the proton exchange membrane has always been the key material affecting the fuel cell. The proton exchange membrane not only plays the role of conducting ions, but also plays the role of isolating fuel. However, methanol is used as fuel in direct methanol fuel cells, so the proton exchange membrane in the battery is required not only to have high proton conductivity, but also to have very low methanol permeability, which makes the widely used perfluorosulfur Acid proton exchange membranes are no longer suitable. In order to obtain a proton exchange membrane suitable for direct methanol fuel cells, it is proposed to use polyvinylidene fluoride grafted polystyrene sulfonic acid membrane, but this membrane must use radiation to excite free radicals, on the other hand grafted to polystyrene sulfonic acid membrane. The polystyrene on the vinylidene fluoride film needs sulfonation, which is complex and unfavorable for large-scale production.
发明内容Contents of the invention
本发明的目的在于提供一种利用硅化合物使聚偏氟乙烯产生自由基,直接接枝共混的2-丙烯酰胺基-2-甲基丙磺酸,这样不但可使膜的生产工艺过程简化,同时也能对枝接量和电导率进行控制的聚偏氟乙烯枝接共混聚2-丙烯酰胺基-2-甲基丙磺酸质子交换膜的制备方法。The object of the present invention is to provide a kind of 2-acrylamido-2-methyl propanesulfonic acid that utilizes silicon compound to make polyvinylidene fluoride produce free radicals, and directly grafts and blends, so that not only can simplify the production process of the film A method for preparing a polyvinylidene fluoride graft blended poly 2-acrylamido-2-methylpropanesulfonic acid proton exchange membrane capable of controlling the grafting amount and electrical conductivity at the same time.
技术解决方案:本发明原料包括:原硅酸钠、2-丙烯酰胺基-2-甲基丙磺酸、过硫酸铵和聚偏氟乙烯;Technical solution: The raw materials of the present invention include: sodium orthosilicate, 2-acrylamido-2-methylpropanesulfonic acid, ammonium persulfate and polyvinylidene fluoride;
制备方法如下:(1)按重量百分比将5wt%~12wt%的原硅酸钠溶于含水3wt%~5wt%的N-甲基吡咯烷酮溶液中,搅拌1~3小时得溶液A,其中:每克聚偏氟乙烯需液体N-甲基吡咯烷酮5~6mL;(2)再将53wt%~72wt%聚偏氟乙烯PVDF倒入溶液A中搅拌1-2小时得混合溶液B;(3)称1wt%~2wt%过硫酸铵,量取20wt%~30wt%的2-丙烯酰胺基-2-甲基丙磺酸,加入到混合溶液B中在氮气气氛80℃~90℃水浴中继续进行电动搅拌1~2h,静置3h,得溶液C;(4)将溶液C浇铸到洁净的玻璃板上,铸膜的厚度控制到0.08mm~0.1mm,在80℃~90℃温度下挥发5~7小时后,干燥、脱膜,得改性聚偏氟乙烯与聚2-丙烯酰胺基-2-甲基丙磺酸接枝共聚物膜;(5)所得膜用去离子水抽提24小时以上,完全去除2-丙烯酰胺基-2-甲基丙磺酸均聚物。The preparation method is as follows: (1) Dissolve 5wt% to 12wt% sodium orthosilicate in water-containing 3wt% to 5wt% N-methylpyrrolidone solution by weight percentage, and stir for 1 to 3 hours to obtain solution A, wherein: One gram of polyvinylidene fluoride requires 5-6 mL of liquid N-methylpyrrolidone; (2) pour 53wt%-72wt% polyvinylidene fluoride PVDF into solution A and stir for 1-2 hours to obtain mixed solution B; (3) weigh 1wt% ~ 2wt% ammonium persulfate, measure 20wt% ~ 30wt% 2-acrylamido-2-methylpropanesulfonic acid, add it to the mixed solution B, and continue to electrokinetic in a water bath at 80°C ~ 90°C in a nitrogen atmosphere. Stir for 1-2 hours and let stand for 3 hours to obtain solution C; (4) Cast solution C on a clean glass plate, control the thickness of the casting film to 0.08mm-0.1mm, and volatilize at 80°C-90°C for 5- After 7 hours, dry and remove the film to obtain a modified polyvinylidene fluoride and poly 2-acrylamide-2-methylpropanesulfonic acid graft copolymer film; (5) the obtained film was extracted with deionized water for 24 hours Above, the 2-acrylamido-2-methylpropanesulfonic acid homopolymer was completely removed.
在使用前将膜进行在去离子水中浸泡6~12小时。The membrane was soaked in deionized water for 6-12 hours before use.
本发明在聚偏氟乙烯枝接聚2-丙烯酰胺基-2-甲基丙磺酸,使聚偏氟乙烯上形成自由基,然后使用自由基引发剂。其效果:本发明制得的质子交换膜具有较低的甲醇渗透性(在10-7cm2/分钟数量级),同时具有很好的质子导电性(电导率达到10-2S/cm数量级),溶胀率较低,与美国杜邦公司的Nafion117膜相比,对甲醇的渗透性降低了1个数量级(在10-7cm2/分钟数量级),溶胀率降低了10%,电导率提高了1至2倍。同时,生产成本低,便于进行大规模生产。The invention grafts poly(2-acrylamido-2-methylpropanesulfonic acid) on the polyvinylidene fluoride to form free radicals on the polyvinylidene fluoride, and then uses a free radical initiator. Its effect: the proton exchange membrane prepared by the present invention has lower methanol permeability (on the order of 10 -7 cm 2 /min), and has good proton conductivity (conductivity reaches the order of 10 -2 S/cm) , the swelling rate is low, compared with DuPont's Nafion117 membrane, the permeability to methanol is reduced by an order of magnitude (in the order of 10 -7 cm 2 /min), the swelling rate is reduced by 10%, and the conductivity is increased by 1 to 2 times. At the same time, the production cost is low, and it is convenient for large-scale production.
具体实施方式Detailed ways
实施例:Example:
将0.4g粉末状的原硅酸钠溶于含水3%~5%的N-甲基吡咯烷酮16mL,搅拌1小时得溶液A,溶液A呈均一状溶液;再将3.1g聚偏氟乙烯PVDF粉末倒入搅拌好的溶液A中搅拌2h得溶液B;称取0.08g过硫酸铵,称量取1.5g的2-丙烯酰胺基-2-甲基丙磺酸AMPS,加入到溶液B中在氮气气氛80℃水浴中继续进行电动搅拌1h,静置3h得溶液C,将得溶液C浇铸到洁净的玻璃板上,在90℃温度下挥发5小时后,干燥、脱膜,得改性聚偏氟乙烯与聚2-丙烯酰胺基-2-甲基丙磺酸接枝共聚物膜;所得膜用去离子水抽提24小时以上,完全去除2-丙烯酰胺基-2-甲基丙磺酸均聚物。在使用前需将膜进行在去离子水中浸泡6~12小时。通过两电极交流阻抗法测其电导率,用溶胀度(SD)来表征膜的溶胀行为,先将干膜剪裁成大小为约3cm×4cm的长方形膜片(面积为Sd),浸入1mol·L-1的甲醇水溶液中,充分溶胀48h后取出,测定湿膜的尺寸,得到面积SW,通过下式计算膜的溶胀度SD:
比较例 作为比较,我们利用Nafion117膜,对其甲醇的渗透性、溶胀率和电导率进行了比较,将Nafion117膜在去离子水中浸泡数小时,通过两电极交流阻抗法测其电导率;用溶胀度(SD)来表征膜的溶胀行为,先将干膜剪裁成大小为约3cm×4cm的长方形膜片(面积为Sd),浸入1mol·L-1的甲醇水溶液中,充分溶胀48h后取出,测定湿膜的尺寸,得到面积SW,通过下式计算膜的溶胀度SD:
表1改性聚偏氟乙烯接枝共混2-丙烯酰胺基-2-甲基丙磺酸(AMPS)质子交换膜在25℃下的性能与Nafion膜的比较Table 1 Comparison of performance of modified polyvinylidene fluoride graft blended 2-acrylamido-2-methylpropanesulfonic acid (AMPS) proton exchange membrane with Nafion membrane at 25°C
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