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CN105406091B - A kind of preparation method of Kynoar heteropoly acid chitosan compound proton exchange membrane - Google Patents

A kind of preparation method of Kynoar heteropoly acid chitosan compound proton exchange membrane Download PDF

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CN105406091B
CN105406091B CN201511000301.5A CN201511000301A CN105406091B CN 105406091 B CN105406091 B CN 105406091B CN 201511000301 A CN201511000301 A CN 201511000301A CN 105406091 B CN105406091 B CN 105406091B
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chitosan
polyvinylidene fluoride
membrane
kynoar
proton exchange
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CN105406091A (en
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文胜
龚春丽
刘海
汪广进
舒红辉
程凡
汪杰
郑根稳
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Hubei Engineering University
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    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M50/00Constructional details or processes of manufacture of the non-active parts of electrochemical cells other than fuel cells, e.g. hybrid cells
    • H01M50/40Separators; Membranes; Diaphragms; Spacing elements inside cells
    • H01M50/409Separators, membranes or diaphragms characterised by the material
    • H01M50/44Fibrous material
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/10Energy storage using batteries

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Abstract

本发明涉及燃料电池技术领域,具体公开了一种聚偏氟乙烯‑杂多酸‑壳聚糖复合质子交换膜的制备方法。该方法首先通过静电纺丝得到聚偏氟乙烯纤维膜,再通过粘附性超强的聚多巴胺将杂多酸包覆在纤维表面,然后将荷正电的天然高分子壳聚糖填充进纤维膜的孔隙,利用壳聚糖与杂多酸之间强烈的静电相互作用力可以有效防止杂多酸在电池使用过程中的流失问题,同时也能大大增加纤维膜的机械性能,所制得的复合膜在室温和高温下均具有高的质子传导率和机械性能。本发明的聚偏氟乙烯‑杂多酸‑壳聚糖复合质子交换膜有望在质子交换膜燃料电池领域具有广阔的应用前景。The invention relates to the technical field of fuel cells, and specifically discloses a method for preparing a polyvinylidene fluoride-heteropolyacid-chitosan composite proton exchange membrane. In this method, the polyvinylidene fluoride fiber membrane is first obtained by electrospinning, and then the heteropolyacid is coated on the surface of the fiber by polydopamine with strong adhesion, and then the positively charged natural polymer chitosan is filled into the fiber. The pores of the membrane can effectively prevent the loss of heteropolyacid during battery use by using the strong electrostatic interaction between chitosan and heteropolyacid, and can also greatly increase the mechanical properties of the fiber membrane. The composite membrane exhibits high proton conductivity and mechanical properties at both room temperature and high temperature. The polyvinylidene fluoride-heteropolyacid-chitosan composite proton exchange membrane of the invention is expected to have broad application prospects in the field of proton exchange membrane fuel cells.

Description

一种聚偏氟乙烯-杂多酸-壳聚糖复合质子交换膜的制备方法A kind of preparation method of polyvinylidene fluoride-heteropoly acid-chitosan composite proton exchange membrane

技术领域technical field

本发明涉及燃料电池技术领域,具体涉及一种聚偏氟乙烯-杂多酸-壳聚糖复合质子交换膜的制备方法。The invention relates to the technical field of fuel cells, in particular to a preparation method of a polyvinylidene fluoride-heteropolyacid-chitosan composite proton exchange membrane.

背景技术Background technique

质子交换膜燃料电池由于具有可室温启动、能量转换效率高、结构紧凑等优点,在电动汽车和便携式电源方面有着广阔的应用前景。作为质子交换膜燃料电池的关键性组件之一,质子交换膜能分隔燃料和氧化剂,允许质子通过,但对电子绝缘,而且它还是电解质和催化剂的基底,因此优良的质子交换膜必须具有高的质子传导率和优异的机械性能。目前所普遍使用的是DuPont公司开发的Nafion系列全氟磺酸型质子交换膜,但其在高温和低湿度下会因强烈失水而导致质子传导率急剧下降、阻醇性能差以及价格昂贵却限制了Nafion膜的广泛商用。因而研制和开发Nafion膜的替代品已刻不容缓。Proton exchange membrane fuel cells have broad application prospects in electric vehicles and portable power supplies due to their advantages such as room temperature start-up, high energy conversion efficiency, and compact structure. As one of the key components of a proton exchange membrane fuel cell, the proton exchange membrane can separate fuel and oxidant, allowing protons to pass through, but insulating electrons, and it is also the substrate of electrolytes and catalysts. Therefore, an excellent proton exchange membrane must have high Proton conductivity and excellent mechanical properties. What is commonly used at present is the Nafion series perfluorosulfonic acid proton exchange membrane developed by DuPont Company, but it will cause a sharp drop in proton conductivity due to strong dehydration under high temperature and low humidity, poor alcohol resistance and high price. The widespread commercial use of Nafion membranes is limited. Therefore, it is urgent to research and develop the substitute of Nafion membrane.

静电纺丝法是聚合物溶液或熔体借助静电作用进行喷射拉伸而获得连续的微纳米级纤维的方法。美国Pintauro教授研究小组[Macromolecules,2008,41,4569.]利用静电纺丝技术先制备了三维互穿的磺化聚芳醚砜纳米纤维膜,然后将一种机械性能优异的惰性聚合物填充到纤维膜的空隙中以提高阻醇性能和机械性能,最终所得膜的质子传导率可与商用的Nafion 117膜相当,但相分离的纳米形态结构未达到预期的理想状态,而且对聚电解质溶液性质与电纺性能之间的关系未加以探讨。国内那辉教授研究小组[Journal ofMembrane Science,2006,281:1.]也采用静电纺丝技术制备了磺化聚醚醚酮(SPEEK)膜,研究表明电纺膜中的磺酸基团在制备过程中更易聚集形成离子簇,但其后续研究和电池性能却还未见报道。中山大学孟跃中等[中国专利ZL201110393309.8]将磺化聚合物与另一种非磺化聚合物分别溶解后进行电纺,得到化学异质的静电纺丝纤维膜,该复合膜具有较高的化学稳定性和质子传导率。总的来看,目前的研究大多集中在用磺化聚合物进行电纺来制备质子交换膜,但由于磺化聚合物分子上的离子基团间存在强烈的斥力干扰,使得聚合物在溶液中呈现出棒状构象,静电纺丝的条件不易调控,难以大规模工业化生产。The electrospinning method is a method in which a polymer solution or melt is sprayed and stretched by electrostatic action to obtain continuous micro-nano-scale fibers. The research group of Professor Pintauro in the United States [Macromolecules, 2008, 41, 4569.] used electrospinning technology to prepare a three-dimensional interpenetrating sulfonated polyarylethersulfone nanofiber membrane, and then filled it with an inert polymer with excellent mechanical properties. In order to improve the alcohol resistance and mechanical properties in the voids of the fiber membrane, the proton conductivity of the final membrane can be comparable to that of the commercial Nafion 117 membrane, but the phase-separated nano-morphological structure has not reached the expected ideal state, and it has a negative effect on the properties of the polyelectrolyte solution. The relationship with electrospinning performance was not explored. Domestic Professor Na Hui's research group [Journal of Membrane Science, 2006, 281:1.] also used electrospinning technology to prepare sulfonated polyetheretherketone (SPEEK) membranes. In the process, it is easier to gather to form ion clusters, but its follow-up research and battery performance have not been reported. Meng Yuezhong from Sun Yat-Sen University [Chinese patent ZL201110393309.8] dissolved the sulfonated polymer and another non-sulfonated polymer separately and then electrospun to obtain a chemically heterogeneous electrospun fiber membrane. The composite membrane has a high chemical stability and proton conductivity. In general, most of the current research focuses on the preparation of proton exchange membranes by electrospinning sulfonated polymers, but due to the strong repulsion interference between the ionic groups on the sulfonated polymer molecules, the polymers in solution It presents a rod-like conformation, the conditions of electrospinning are not easy to control, and it is difficult to produce on a large scale.

聚偏氟乙烯(PVDF)是一种半结晶的含氟聚合物,其综合性能优异,具有优异的机械性能、电化学和热稳定性、高介电常数、易静电纺丝成膜等优点,且成膜后强度和柔韧性优良,但PVDF本身并不具有质子传导性,因此将PVDF与无机质子导体如杂多酸复合是提高其质子传导率的有效途径,但杂多酸易溶于水,在质子交换膜燃料电池的运行过程中,很容易随电极生成的水而流失,因此,如何解决杂多酸在电纺膜中的流失是这类膜能否实际应用的关键问题。Polyvinylidene fluoride (PVDF) is a semi-crystalline fluoropolymer with excellent comprehensive properties, such as excellent mechanical properties, electrochemical and thermal stability, high dielectric constant, and easy electrospinning to form films. And after film formation, the strength and flexibility are excellent, but PVDF itself does not have proton conductivity, so compounding PVDF with inorganic proton conductors such as heteropolyacids is an effective way to improve its proton conductivity, but heteropolyacids are easily soluble in water , during the operation of proton exchange membrane fuel cells, it is easy to lose with the water generated by the electrodes. Therefore, how to solve the loss of heteropolyacids in electrospun membranes is the key issue for the practical application of such membranes.

发明内容Contents of the invention

针对现有技术中存在的不足之处,本发明的目的在于提供一种聚偏氟乙烯-杂多酸-壳聚糖复合质子交换膜的制备方法。Aiming at the deficiencies in the prior art, the object of the present invention is to provide a method for preparing a polyvinylidene fluoride-heteropolyacid-chitosan composite proton exchange membrane.

为实现上述发明目的,本发明采取了如下技术措施:In order to realize the above-mentioned purpose of the invention, the present invention has taken following technical measures:

一种聚偏氟乙烯-杂多酸-壳聚糖复合质子交换膜的制备方法,该方法依次包括以下步骤:A preparation method of polyvinylidene fluoride-heteropolyacid-chitosan composite proton exchange membrane, the method comprises the following steps in sequence:

(1)将聚偏氟乙烯溶解于混合有机溶剂中,配成聚偏氟乙烯浓度为5wt%~30wt%的静电纺丝溶液;(1) Dissolving polyvinylidene fluoride in a mixed organic solvent to prepare an electrospinning solution with a polyvinylidene fluoride concentration of 5wt% to 30wt%;

所述聚偏氟乙烯优选为牌号HSV900的聚偏氟乙烯;The polyvinylidene fluoride is preferably polyvinylidene fluoride of brand HSV900;

所述混合有机溶剂由酰胺类溶剂和酮类溶剂组成,其中,酮类溶剂在混合有机溶剂中的体积百分比含量为2~40%;The mixed organic solvent is composed of an amide solvent and a ketone solvent, wherein the volume percentage of the ketone solvent in the mixed organic solvent is 2-40%;

所述酰胺类溶剂为N,N-二甲基甲酰胺或N,N-二甲基乙酰胺,酮类溶剂为丙酮或丁酮;The amide solvent is N,N-dimethylformamide or N,N-dimethylacetamide, and the ketone solvent is acetone or butanone;

(2)将步骤(1)所得静电纺丝溶液加入到静电纺丝装置的注射器中,在环境温度为10~30℃,纺丝电压为20~40kV,纺丝针头流量为0.1~1mL/h的条件下进行静电纺丝,得到聚偏氟乙烯静电纺丝纤维膜;(2) Add the electrospinning solution obtained in step (1) into the syringe of the electrospinning device, the ambient temperature is 10-30°C, the spinning voltage is 20-40kV, and the flow rate of the spinning needle is 0.1-1mL/h Electrospinning is carried out under certain conditions to obtain a polyvinylidene fluoride electrospun fiber membrane;

(3)配置三(羟甲基)氨基甲烷浓度为1~10mmol/L的Tris-HCl缓冲液,所述Tris-HCl缓冲液pH值为8.0~9.0,将步骤(2)所得聚偏氟乙烯静电纺丝纤维膜浸泡于该Tris-HCl缓冲液中;(3) configuration tris (hydroxymethyl) aminomethane concentration is the Tris-HCl buffer solution of 1~10mmol/L, and described Tris-HCl buffer solution pH value is 8.0~9.0, and step (2) gained polyvinylidene fluoride The electrospun fiber membrane is soaked in the Tris-HCl buffer;

(4)往步骤(3)所得浸泡有聚偏氟乙烯静电纺丝纤维膜的Tris-HCl缓冲液中加入多巴胺盐酸盐,多巴胺盐酸盐与Tris-HCl缓冲液的比例为(0.5~8)mg:1mL,室温磁力搅拌使多巴胺氧化聚合10~48h后,得到聚多巴胺处理的聚偏氟乙烯静电纺丝纤维膜;(4) Add dopamine hydrochloride to the Tris-HCl buffer solution that step (3) gained is soaked with polyvinylidene fluoride electrospinning fiber membrane, the ratio of dopamine hydrochloride and Tris-HCl buffer solution is (0.5~8 )mg: 1mL, magnetically stir at room temperature to oxidatively polymerize dopamine for 10-48 hours, and obtain a polydopamine-treated polyvinylidene fluoride electrospun fiber membrane;

(5)将步骤(4)所得聚巴胺处理的聚偏氟乙烯静电纺丝纤维膜加入到浓度为2wt%~25wt%的杂多酸水溶液中,室温浸泡8~24h,取出纤维膜,并经去离子水洗涤干燥即得聚偏氟乙烯-杂多酸膜;所述杂多酸为磷钨酸、磷钼酸或硅钨酸;(5) Add the polyvinylidene fluoride electrospun fiber membrane treated with polypamine obtained in step (4) into a heteropolyacid aqueous solution with a concentration of 2wt% to 25wt%, soak at room temperature for 8 to 24h, take out the fiber membrane, and Polyvinylidene fluoride-heteropolyacid film is obtained by washing and drying with deionized water; the heteropolyacid is phosphotungstic acid, phosphomolybdic acid or silicotungstic acid;

(6)配置乙酸浓度为0.5wt%~3wt%的乙酸水溶液,然后将壳聚糖溶解在该乙酸水溶液中配成壳聚糖浓度为0.2wt%~5wt%的壳聚糖溶液,将步骤(5)所得聚偏氟乙烯-杂多酸膜加入到该壳聚糖溶液中,室温浸泡15~45min,取出晾干,再重复浸泡、晾干2~6次,最后干燥即得聚偏氟乙烯-杂多酸-壳聚糖复合质子交换膜。(6) configuration acetic acid concentration is the acetic acid aqueous solution of 0.5wt%~3wt%, then chitosan is dissolved in this acetic acid aqueous solution and is made into the chitosan solution that chitosan concentration is 0.2wt%~5wt%, step ( 5) The obtained polyvinylidene fluoride-heteropoly acid film is added to the chitosan solution, soaked at room temperature for 15-45 minutes, taken out to dry, then repeated soaking and drying for 2-6 times, and finally dried to obtain polyvinylidene fluoride -Heteropolyacid-chitosan composite proton exchange membrane.

本发明与现有技术相比,具有如下优点和有益效果:Compared with the prior art, the present invention has the following advantages and beneficial effects:

1、与直接将杂多酸掺杂进聚偏氟乙烯相比,本发明采用一种粘附性超强的聚多巴胺作为中间层,可以将杂多酸牢牢地包附在聚偏氟乙烯纤维的表面(见附图3);1. Compared with directly doping heteropoly acid into polyvinylidene fluoride, the present invention adopts a super-adhesive polydopamine as the intermediate layer, which can firmly wrap heteropoly acid on polyvinylidene fluoride The surface of the fiber (see accompanying drawing 3);

2、与仅将惰性聚合物填充进电纺纤维膜孔隙以增加膜的机械性能相比,本发明将荷正电的天然高分子壳聚糖填充进纤维膜的孔隙,利用壳聚糖与杂多酸之间强烈的静电相互作用力可以有效防止杂多酸在电池使用过程中的流失问题,并且壳聚糖填充后也能大大增加电纺膜的机械性能;2. Compared with only filling the pores of the electrospun fiber membrane with inert polymers to increase the mechanical properties of the membrane, the present invention fills the pores of the fiber membrane with positively charged natural polymer chitosan, and utilizes chitosan and hetero The strong electrostatic interaction between polyacids can effectively prevent the loss of heteropolyacids during battery use, and chitosan filling can also greatly increase the mechanical properties of electrospun membranes;

3、本发明制备的复合膜由于有无机质子导体杂多酸的引入,质子传导率高;3. The composite membrane prepared by the present invention has high proton conductivity due to the introduction of inorganic proton conductor heteropolyacid;

4、本发明制备工艺简单,制备的复合质子交换膜成本远低于Nafion商业膜,易产业化,可推动燃料电池的发展。4. The preparation process of the present invention is simple, and the cost of the prepared composite proton exchange membrane is much lower than that of Nafion commercial membrane, which is easy to be industrialized and can promote the development of fuel cells.

综上所述,本发明制备的聚偏氟乙烯-杂多酸-壳聚糖复合质子交换膜有望在质子交换膜燃料电池领域具有广阔的应用前景。In summary, the polyvinylidene fluoride-heteropolyacid-chitosan composite proton exchange membrane prepared by the present invention is expected to have broad application prospects in the field of proton exchange membrane fuel cells.

附图说明Description of drawings

图1和2分别为实施例1中所制备的聚偏氟乙烯静电纺丝纤维膜的扫描电镜图和能谱图;Figures 1 and 2 are scanning electron micrographs and energy spectrum diagrams of the polyvinylidene fluoride electrospun fiber membrane prepared in Example 1, respectively;

图3和4分别为实施例1中所制备的磷钨酸包覆后的聚偏氟乙烯-磷钨酸纤维膜扫描电镜图和能谱图。Figures 3 and 4 are scanning electron microscope images and energy spectrum images of the polyvinylidene fluoride-phosphotungstic acid fiber membrane coated with phosphotungstic acid prepared in Example 1, respectively.

从图1可以看出静电纺丝制备的聚偏氟乙烯纤维膜的直径较均匀,直径基本在500nm左右;图2中能谱图检测纤维膜中只有C、F元素;从图3可以看出经壳聚糖包覆后,纤维的表面均匀包覆有厚厚的壳层;图4能谱图中明显的P、W、O等元素的出现可以证明包覆层为磷钨酸。It can be seen from Figure 1 that the diameter of the polyvinylidene fluoride fiber membrane prepared by electrospinning is relatively uniform, and the diameter is basically about 500nm; in Figure 2, there are only C and F elements in the fiber membrane detected by the energy spectrum; it can be seen from Figure 3 After being coated with chitosan, the surface of the fiber is evenly covered with a thick shell layer; the appearance of obvious P, W, O and other elements in the energy spectrum in Figure 4 can prove that the coating layer is phosphotungstic acid.

具体实施方式detailed description

下面申请人将结合具体的实施例对本发明的技术方案作进一步的详细说明,目的在于使本领域技术人员对本申请有更加清楚的理解和认识。Below, the applicant will further describe the technical solution of the present invention in detail in combination with specific embodiments, in order to enable those skilled in the art to have a clearer understanding and understanding of the present application.

以下各具体实施例不应在任何程度上被理解或解释为对本申请权利要求书请求保护范围的限制。The following specific examples should not be understood or interpreted as limiting the protection scope of the claims of the present application to any extent.

以下实施例1-5中:Among the following examples 1-5:

所用原料聚偏氟乙烯(牌号HSV900),购于法国阿珂码公司;壳聚糖(脱乙酰度92.5%,分子量为10万)购于浙江奥兴生物科技有限公司。The raw material polyvinylidene fluoride (brand name HSV900) was purchased from Acma, France; chitosan (deacetylation degree 92.5%, molecular weight 100,000) was purchased from Zhejiang Aoxing Biotechnology Co., Ltd.

其他试剂与原料均为常规市售商品。All other reagents and raw materials are commercially available.

实施例1Example 1

一种聚偏氟乙烯-杂多酸-壳聚糖复合质子交换膜的制备方法,步骤如下:A preparation method of polyvinylidene fluoride-heteropolyacid-chitosan composite proton exchange membrane, the steps are as follows:

将5g聚偏氟乙烯溶解在体积比为9.5:0.5的N,N-二甲基乙酰胺和丙酮的混合溶剂中,配成10wt%的聚偏氟乙烯静电纺丝溶液;将该静电纺丝溶液加入到静电纺丝装置的注射器中,在环境温度为25℃,纺丝电压为25kV,纺丝针头流量为0.3mL/h的条件下进行静电纺丝,得到聚偏氟乙烯静电纺丝纤维膜;配置三(羟甲基)氨基甲烷浓度为4mmol/L的Tris-HCl缓冲液,所述Tris-HCl缓冲液pH值为8.5,然后将聚偏氟乙烯静电纺丝纤维膜浸泡在该缓冲溶液中,再往该缓冲液中加入4mg/mL(该比例为多巴胺盐酸盐与Tris-HCl缓冲液的固液比,以下实施例同,不赘述)的多巴胺盐酸盐,室温磁力搅拌24h后,得到聚多巴胺处理的聚偏氟乙烯静电纺丝纤维膜;再将聚多巴胺处理的聚偏氟乙烯静电纺丝纤维膜加入到浓度为15wt%的磷钨酸水溶液中,室温浸泡12h,取出纤维膜,并经去离子水洗涤干燥即得聚偏氟乙烯-磷钨酸膜;配置乙酸浓度为1wt%的乙酸水溶液,然后将壳聚糖溶解在该乙酸水溶液中配成壳聚糖浓度为1wt%的壳聚糖溶液,再将聚偏氟乙烯-磷钨酸膜加入到该壳聚糖溶液中,室温浸泡30min,取出晾干,再重复浸泡、晾干5次,最后干燥即得聚偏氟乙烯-磷钨酸-壳聚糖复合质子交换膜。膜的性能测试结果如表1所示。Dissolve 5g of polyvinylidene fluoride in a mixed solvent of N,N-dimethylacetamide and acetone with a volume ratio of 9.5:0.5 to prepare a 10wt% polyvinylidene fluoride electrospinning solution; The solution was added to the syringe of the electrospinning device, and the electrospinning was carried out under the conditions of the ambient temperature of 25°C, the spinning voltage of 25kV, and the flow rate of the spinning needle of 0.3mL/h to obtain polyvinylidene fluoride electrospun fibers Membrane; configuration tris (hydroxymethyl) aminomethane concentration is the Tris-HCl buffer solution of 4mmol/L, and the pH value of the Tris-HCl buffer solution is 8.5, then the polyvinylidene fluoride electrospun fiber membrane is soaked in this buffer In the solution, add 4mg/mL dopamine hydrochloride (this ratio is the solid-to-liquid ratio of dopamine hydrochloride and Tris-HCl buffer solution, the following examples are the same, do not repeat them) to the buffer solution, and magnetically stir at room temperature for 24h Finally, the polydopamine-treated polyvinylidene fluoride electrospun fiber membrane is obtained; then the polydopamine-treated polyvinylidene fluoride electrospun fiber membrane is added to a phosphotungstic acid aqueous solution with a concentration of 15 wt%, soaked at room temperature for 12 hours, and taken out fiber membrane, and washed and dried with deionized water to obtain polyvinylidene fluoride-phosphotungstic acid membrane; configure the acetic acid aqueous solution with acetic acid concentration of 1wt%, and then dissolve chitosan in the acetic acid aqueous solution to form a chitosan concentration of 1wt% chitosan solution, then add polyvinylidene fluoride-phosphotungstic acid film into the chitosan solution, soak at room temperature for 30min, take it out and dry in the air, repeat soaking and drying for 5 times, and finally dry to obtain the polyvinylidene fluoride-phosphotungstic acid film. Vinylidene fluoride-phosphotungstic acid-chitosan composite proton exchange membrane. The performance test results of the film are shown in Table 1.

表1Table 1

从表1结果可以看出,本实施例所制备的聚偏氟乙烯-磷钨酸-壳聚糖复合质子交换膜的质子传导率在室温和高温(80℃)下均高于Nafion 112膜,尤其是在80℃时质子传导率大约是同条件下Nafion 112膜的3倍;同时该复合质子交换膜的机械性能较未填充壳聚糖的聚偏氟乙烯-磷钨酸膜大大提高。这种复合膜有望用于质子交换膜燃料电池中。It can be seen from the results in Table 1 that the proton conductivity of the polyvinylidene fluoride-phosphotungstic acid-chitosan composite proton exchange membrane prepared in this example is higher than that of the Nafion 112 membrane at room temperature and high temperature (80°C). Especially at 80°C, the proton conductivity is about three times that of Nafion 112 membrane under the same conditions; at the same time, the mechanical properties of the composite proton exchange membrane are greatly improved compared with the polyvinylidene fluoride-phosphotungstic acid membrane not filled with chitosan. This composite membrane is expected to be used in proton exchange membrane fuel cells.

实施例2Example 2

一种聚偏氟乙烯-杂多酸-壳聚糖复合质子交换膜的制备方法,步骤如下:A preparation method of polyvinylidene fluoride-heteropolyacid-chitosan composite proton exchange membrane, the steps are as follows:

将5g聚偏氟乙烯溶解在体积比为9.8:0.2的N,N-二甲基甲酰胺和丁酮的混合溶剂中,配成5wt%的聚偏氟乙烯静电纺丝溶液;将该静电纺丝溶液加入到静电纺丝装置的注射器中,在环境温度为10℃,纺丝电压为20kV,纺丝针头流量为1mL/h的条件下进行静电纺丝,得到聚偏氟乙烯静电纺丝纤维膜;配置三(羟甲基)氨基甲烷浓度为1mmol/L的Tris-HCl缓冲液,所述Tris-HCl缓冲液pH值为8.0,然后将聚偏氟乙烯静电纺丝纤维膜浸泡在该缓冲溶液中,再往该缓冲液中加入0.5mg/mL的多巴胺盐酸盐,室温磁力搅拌10h后,得到聚多巴胺处理的聚偏氟乙烯静电纺丝纤维膜;再将聚多巴胺处理的聚偏氟乙烯静电纺丝纤维膜加入到浓度为2wt%的磷钼酸水溶液中,室温浸泡24h,取出纤维膜,并经去离子水洗涤干燥即得聚偏氟乙烯-磷钼酸膜;配置乙酸浓度为0.5wt%的乙酸水溶液,然后将壳聚糖溶解在该乙酸水溶液中配成壳聚糖浓度为0.2wt%的壳聚糖溶液,再将聚偏氟乙烯-磷钼酸膜加入到该壳聚糖溶液中,室温浸泡15min,取出晾干,再重复浸泡、晾干6次,最后干燥即得聚偏氟乙烯-磷钼酸-壳聚糖复合质子交换膜。Dissolve 5g of polyvinylidene fluoride in a mixed solvent of N,N-dimethylformamide and butanone at a volume ratio of 9.8:0.2 to prepare a 5wt% polyvinylidene fluoride electrospinning solution; The silk solution was added to the syringe of the electrospinning device, and the electrospinning was carried out under the conditions of the ambient temperature of 10°C, the spinning voltage of 20kV, and the flow rate of the spinning needle of 1mL/h to obtain polyvinylidene fluoride electrospun fibers Membrane; configuration tris (hydroxymethyl) aminomethane concentration is the Tris-HCl buffer solution of 1mmol/L, and the pH value of the Tris-HCl buffer solution is 8.0, then the polyvinylidene fluoride electrospun fiber membrane is soaked in this buffer solution, and then add 0.5 mg/mL dopamine hydrochloride to the buffer solution, and after magnetic stirring at room temperature for 10 hours, obtain polydopamine-treated polyvinylidene fluoride electrospun fiber membrane; then polydopamine-treated polyvinylidene fluoride Add the ethylene electrospun fiber membrane to the phosphomolybdic acid aqueous solution with a concentration of 2wt%, soak it at room temperature for 24 hours, take out the fiber membrane, wash and dry it with deionized water to obtain the polyvinylidene fluoride-phosphomolybdic acid membrane; configure the concentration of acetic acid as 0.5wt% acetic acid aqueous solution, and then dissolving chitosan in this acetic acid aqueous solution is made into the chitosan solution that chitosan concentration is 0.2wt%, then adds polyvinylidene fluoride-phosphomolybdic acid film to this chitosan Soak in the sugar solution for 15 minutes at room temperature, take it out and dry it in the air, repeat the soaking and drying for 6 times, and finally dry it to obtain the polyvinylidene fluoride-phosphomolybdic acid-chitosan composite proton exchange membrane.

实施例3Example 3

一种聚偏氟乙烯-杂多酸-壳聚糖复合质子交换膜的制备方法,步骤如下:A preparation method of polyvinylidene fluoride-heteropolyacid-chitosan composite proton exchange membrane, the steps are as follows:

将5g聚偏氟乙烯溶解在体积比为6:4的N,N-二甲基甲酰胺和丁酮的混合溶剂中,配成30wt%的聚偏氟乙烯静电纺丝溶液;将该静电纺丝溶液加入到静电纺丝装置的注射器中,在环境温度为30℃,纺丝电压为40kV,纺丝针头流量为0.1mL/h的条件下进行静电纺丝,得到聚偏氟乙烯静电纺丝纤维膜;配置三(羟甲基)氨基甲烷浓度为10mmol/L的Tris-HCl缓冲液,所述Tris-HCl缓冲液pH值为9.0,然后将聚偏氟乙烯静电纺丝纤维膜浸泡在该缓冲溶液中,再往该缓冲液中加入8mg/mL的多巴胺盐酸盐,室温磁力搅拌48h后,得到聚多巴胺处理的聚偏氟乙烯静电纺丝纤维膜;再将聚多巴胺处理的聚偏氟乙烯静电纺丝纤维膜加入到浓度为25wt%的硅钨酸水溶液中,室温浸泡12h,取出纤维膜,并经去离子水洗涤干燥即得聚偏氟乙烯-硅钨酸膜;配置乙酸浓度为3wt%的乙酸水溶液,然后将壳聚糖溶解在该乙酸水溶液中配成壳聚糖浓度为5wt%的壳聚糖溶液,再将聚偏氟乙烯-硅钨酸膜加入到该壳聚糖溶液中,室温浸泡45min,取出晾干,再重复浸泡、晾干2次,最后干燥即得聚偏氟乙烯-硅钨酸-壳聚糖复合质子交换膜。Dissolve 5g of polyvinylidene fluoride in a mixed solvent of N,N-dimethylformamide and butanone at a volume ratio of 6:4 to prepare a 30wt% polyvinylidene fluoride electrospinning solution; The silk solution was added to the syringe of the electrospinning device, and the electrospinning was carried out under the conditions of the ambient temperature of 30°C, the spinning voltage of 40kV, and the flow rate of the spinning needle of 0.1mL/h to obtain polyvinylidene fluoride electrospinning Fiber membrane; configuration tris (hydroxymethyl) aminomethane concentration is the Tris-HCl buffer solution of 10mmol/L, and the pH value of the Tris-HCl buffer solution is 9.0, then the polyvinylidene fluoride electrospun fiber membrane is immersed in the 8 mg/mL dopamine hydrochloride was added to the buffer solution, and after magnetic stirring at room temperature for 48 hours, the polydopamine-treated polyvinylidene fluoride electrospun fiber membrane was obtained; the polydopamine-treated polyvinylidene fluoride Add the ethylene electrospun fiber membrane to the aqueous solution of silicotungstic acid with a concentration of 25wt%, soak it at room temperature for 12 hours, take out the fiber membrane, wash and dry it with deionized water to obtain the polyvinylidene fluoride-silicotungstic acid membrane; configure the concentration of acetic acid as 3wt% acetic acid aqueous solution, then dissolving chitosan in this acetic acid aqueous solution is made into the chitosan solution that chitosan concentration is 5wt%, then adds polyvinylidene fluoride-silicotungstic acid film to this chitosan solution , soaked at room temperature for 45 minutes, took it out to dry, repeated soaking and drying twice, and finally dried to obtain polyvinylidene fluoride-silicotungstic acid-chitosan composite proton exchange membrane.

实施例4Example 4

一种聚偏氟乙烯-杂多酸-壳聚糖复合质子交换膜的制备方法,步骤如下:A preparation method of polyvinylidene fluoride-heteropolyacid-chitosan composite proton exchange membrane, the steps are as follows:

将5g聚偏氟乙烯溶解在体积比为8:2的N,N-二甲基乙酰胺和丁酮的混合溶剂中,配成15wt%的聚偏氟乙烯静电纺丝溶液;将该静电纺丝溶液加入到静电纺丝装置的注射器中,在环境温度为20℃,纺丝电压为30kV,纺丝针头流量为0.5mL/h的条件下进行静电纺丝,得到聚偏氟乙烯静电纺丝纤维膜;配置三(羟甲基)氨基甲烷浓度为6mmol/L的Tris-HCl缓冲液,所述Tris-HCl缓冲液pH值为8.2,然后将聚偏氟乙烯静电纺丝纤维膜浸泡在该缓冲溶液中,再往该缓冲液中加入5mg/mL的多巴胺盐酸盐,室温磁力搅拌16h后,得到聚多巴胺处理的聚偏氟乙烯静电纺丝纤维膜;再将聚多巴胺处理的聚偏氟乙烯静电纺丝纤维膜加入到浓度为10wt%的磷钨酸水溶液中,室温浸泡16h,取出纤维膜,并经去离子水洗涤干燥即得聚偏氟乙烯-磷钨酸膜;配置乙酸浓度为2wt%的乙酸水溶液,然后将壳聚糖溶解在该乙酸水溶液中配成壳聚糖浓度为2wt%的壳聚糖溶液,再将聚偏氟乙烯-磷钨酸膜加入到该壳聚糖溶液中,室温浸泡25min,取出晾干,再重复浸泡、晾干3次,最后干燥即得聚偏氟乙烯-磷钨酸-壳聚糖复合质子交换膜。Dissolve 5g of polyvinylidene fluoride in a mixed solvent of N,N-dimethylacetamide and butanone at a volume ratio of 8:2 to prepare a 15wt% polyvinylidene fluoride electrospinning solution; The silk solution was added to the syringe of the electrospinning device, and the electrospinning was carried out under the conditions of the ambient temperature of 20°C, the spinning voltage of 30kV, and the flow rate of the spinning needle of 0.5mL/h to obtain polyvinylidene fluoride electrospinning Fiber membrane; configuration tris (hydroxymethyl) aminomethane concentration is the Tris-HCl buffer solution of 6mmol/L, and the pH value of the Tris-HCl buffer solution is 8.2, then the polyvinylidene fluoride electrospun fiber membrane is soaked in this 5 mg/mL dopamine hydrochloride was added to the buffer solution, and after magnetic stirring at room temperature for 16 hours, a polydopamine-treated polyvinylidene fluoride electrospun fiber membrane was obtained; then the polydopamine-treated polyvinylidene fluoride Add the ethylene electrospun fiber membrane to the phosphotungstic acid aqueous solution with a concentration of 10wt%, soak it at room temperature for 16 hours, take out the fiber membrane, wash and dry it with deionized water to obtain the polyvinylidene fluoride-phosphotungstic acid membrane; configure the concentration of acetic acid as 2wt% acetic acid aqueous solution, then dissolving chitosan in the acetic acid aqueous solution to form a chitosan solution with a chitosan concentration of 2wt%, and then adding the polyvinylidene fluoride-phosphotungstic acid film to the chitosan solution , soaked at room temperature for 25 minutes, took it out to dry, repeated soaking and drying 3 times, and finally dried to obtain polyvinylidene fluoride-phosphotungstic acid-chitosan composite proton exchange membrane.

实施例5Example 5

一种聚偏氟乙烯-杂多酸-壳聚糖复合质子交换膜的制备方法,步骤如下:A preparation method of polyvinylidene fluoride-heteropolyacid-chitosan composite proton exchange membrane, the steps are as follows:

将5g聚偏氟乙烯溶解在体积比为7:3的N,N-二甲基甲酰胺和丙酮的混合溶剂中,配成25wt%的聚偏氟乙烯静电纺丝溶液;将该静电纺丝溶液加入到静电纺丝装置的注射器中,在环境温度为25℃,纺丝电压为35kV,纺丝针头流量为0.8mL/h的条件下进行静电纺丝,得到聚偏氟乙烯静电纺丝纤维膜;配置三(羟甲基)氨基甲烷浓度为2mmol/L的Tris-HCl缓冲液,所述Tris-HCl缓冲液pH值为8.2,然后将聚偏氟乙烯静电纺丝纤维膜浸泡在该缓冲溶液中,再往该缓冲液中加入2mg/mL的多巴胺盐酸盐,室温磁力搅拌30h后,得到聚多巴胺处理的聚偏氟乙烯静电纺丝纤维膜;再将聚多巴胺处理的聚偏氟乙烯静电纺丝纤维膜加入到浓度为20wt%的磷钼酸水溶液中,室温浸泡8h,取出纤维膜,并经去离子水洗涤干燥即得聚偏氟乙烯-磷钼酸膜;配置乙酸浓度为1.5wt%的乙酸水溶液,然后将壳聚糖溶解在该乙酸水溶液中配成壳聚糖浓度为3wt%的壳聚糖溶液,再将聚偏氟乙烯-磷钼酸膜加入到该壳聚糖溶液中,室温浸泡35min,取出晾干,再重复浸泡、晾干4次,最后干燥即得聚偏氟乙烯-磷钼酸-壳聚糖复合质子交换膜。Dissolve 5g of polyvinylidene fluoride in a mixed solvent of N,N-dimethylformamide and acetone with a volume ratio of 7:3 to prepare a 25wt% polyvinylidene fluoride electrospinning solution; The solution was added to the syringe of the electrospinning device, and the electrospinning was carried out under the conditions of the ambient temperature of 25°C, the spinning voltage of 35kV, and the flow rate of the spinning needle of 0.8mL/h to obtain polyvinylidene fluoride electrospun fibers Membrane; configuration tris (hydroxymethyl) aminomethane concentration is the Tris-HCl buffer solution of 2mmol/L, and the pH value of the Tris-HCl buffer solution is 8.2, then the polyvinylidene fluoride electrospun fiber membrane is soaked in this buffer solution, then add 2mg/mL dopamine hydrochloride to the buffer solution, and after magnetic stirring at room temperature for 30h, obtain polydopamine-treated polyvinylidene fluoride electrospun fiber membrane; then polydopamine-treated polyvinylidene fluoride The electrospun fiber membrane was added to a 20wt% phosphomolybdic acid aqueous solution, soaked at room temperature for 8 hours, the fiber membrane was taken out, washed and dried with deionized water to obtain a polyvinylidene fluoride-phosphomolybdic acid membrane; the concentration of acetic acid was 1.5 Wt% acetic acid aqueous solution, then dissolving chitosan in this acetic acid aqueous solution is made into the chitosan solution that chitosan concentration is 3wt%, then polyvinylidene fluoride-phosphomolybdic acid film is added to this chitosan solution , soaked at room temperature for 35 minutes, took it out to dry, repeated soaking and drying 4 times, and finally dried to obtain polyvinylidene fluoride-phosphomolybdic acid-chitosan composite proton exchange membrane.

表2列出了实施例2-5制得的聚偏氟乙烯-杂多酸-壳聚糖复合质子交换膜的各项性能指标数据。Table 2 lists the performance index data of the polyvinylidene fluoride-heteropolyacid-chitosan composite proton exchange membrane prepared in Examples 2-5.

表2Table 2

以上各实施例所制备的膜性能测试条件统一描述如下:The film performance test conditions prepared by each of the above embodiments are described in a unified manner as follows:

(1)质子传导率:膜的电阻在频率响应分析仪上进行测试,频率扫描范围为1-107Hz,交流信号振幅为100mV。将裁剪好的膜(4cm×5cm)采用四电极交流阻抗法测试,在测试之前,膜样品置于室温去离子水中达饱和。膜的质子传导率σ(S/cm)通过下式进行计算:(1) Proton conductivity: The resistance of the membrane was tested on a frequency response analyzer, the frequency scanning range was 1-10 7 Hz, and the amplitude of the AC signal was 100mV. The cut film (4cm×5cm) was tested by four-electrode AC impedance method. Before the test, the film sample was placed in deionized water at room temperature to reach saturation. The proton conductivity σ (S/cm) of the membrane was calculated by the following formula:

式中,L和A分别为两电极的间距和两电极间待测膜的有效横截面积,R是膜的电阻,通过交流阻抗测试所得的Nyquist图求取。In the formula, L and A are the distance between the two electrodes and the effective cross-sectional area of the film to be tested between the two electrodes, respectively, and R is the resistance of the film, which is obtained from the Nyquist diagram obtained from the AC impedance test.

(2)拉伸强度和断裂伸长率:将膜裁成长50mm,宽20mm的长方形样条,在电子拉力机上采用2mm/min的拉伸速度进行测试。(2) Tensile strength and elongation at break: Cut the film into a rectangular strip with a length of 50 mm and a width of 20 mm, and test it on an electronic tensile machine at a tensile speed of 2 mm/min.

(3)杂多酸的流失率:首先称取干膜的质量为W1,然后将膜在室温去离子水中浸泡24h后取出,干燥至恒重后称取其质量为W2,杂多酸的流失率通过下式进行计算:(3) Loss rate of heteropoly acid: first weigh the mass of the dry film as W 1 , then soak the film in deionized water at room temperature for 24 hours, take it out, dry it to constant weight, and weigh its mass as W 2 , the mass of the heteropoly acid The churn rate for is calculated by the following formula:

上述实施例为本发明的较佳实施方式,但本发明的实施方式并不受上述实施例的限制。其它任何未背离本发明精神实质及原理所做的改变、修饰、替代、组合、简化,均应视为等效置换方式,包含在本发明保护范围之内。The above examples are preferred implementations of the present invention, but the implementation of the present invention is not limited by the above examples. Any other changes, modifications, substitutions, combinations, and simplifications that do not deviate from the spirit and principles of the present invention shall be regarded as equivalent replacements, and shall be included in the protection scope of the present invention.

Claims (1)

1. a kind of preparation method of Kynoar-heteropoly acid-chitosan compound proton exchange membrane, this method includes following successively Step:
(1)Kynoar is dissolved in mixed organic solvents, is made into the electrostatic that Kynoar concentration is 5wt% ~ 30wt% Spinning solution;
The mixed organic solvents are made up of amide solvent and ketones solvent, wherein, ketones solvent is in mixed organic solvents Volume percent content be 2 ~ 40%;
The amide solvent is DMF or DMA, and ketones solvent is acetone or butanone;
(2)By step(1)Gained electrostatic spinning solution is added in the syringe of electrostatic spinning apparatus, environment temperature be 10 ~ 30 DEG C, spinning voltage be 20 ~ 40 kV, spinning syringe needle flow carry out electrostatic spinning under conditions of being 0.1 ~ 1 mL/h, obtain poly- inclined PVF electrospun fibers film;
(3)Configuration three(Methylol)Aminomethane concentration is 1 ~ 10 mmol/L Tris-HCl buffer solutions, and the Tris-HCl delays Fliud flushing pH value is 8.0 ~ 9.0, by step(2)Gained Kynoar electrospun fibers film is soaked in the Tris-HCl buffer solutions In;
(4)Toward step(3)Gained in the Tris-HCl buffer solutions of Kynoar electrospun fibers film immersed with adding DOPA The ratio of amine hydrochlorate, dopamine hydrochloride and Tris-HCl buffer solutions is 0.5 ~ 8 mg:1mL, room temperature magnetic agitation make DOPA After 10 ~ 48h of amine oxidation polymerization, the Kynoar electrospun fibers film of poly-dopamine processing is obtained;
(5)By step(4)A Kynoar electrospun fibers film for poly- bar of amine processing of gained be added to concentration for 2wt% ~ In the 25wt% heteropoly acid aqueous solution, 8 ~ 24h of soaking at room temperature, tunica fibrosa is taken out, and poly- inclined fluorine is drying to obtain through deionized water washing Ethene-heteropoly acid film;
The heteropoly acid is one kind in phosphotungstic acid, phosphomolybdic acid or silico-tungstic acid;
(6)The acetic acid aqueous solution that acetic acid concentration is 0.5wt% ~ 3wt% is configured, is then dissolved chitosan in the acetic acid aqueous solution The chitosan solution that chitosan concentration is 0.2wt% ~ 5wt% is made into, by step(5)Gained Kynoar-heteropoly acid film adds Into the chitosan solution, 15 ~ 45min of soaking at room temperature, taking-up is dried, and is repeated immersion, is dried 2 ~ 6 times, finally dry to gather Vinylidene-heteropoly acid-chitosan compound proton exchange membrane.
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CN107093760A (en) * 2017-05-05 2017-08-25 湖北工程学院 The preparation method of Kynoar loading chitosan PEM
CN107248584A (en) * 2017-06-22 2017-10-13 长春工业大学 Chitosan phosphotungstic acid ionic liquid compound proton exchange membrane of novel porous structure and preparation method thereof
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Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1697225A (en) * 2005-05-20 2005-11-16 武汉理工大学 Composite proton exchange membrane for low humidification and long life fuel cell and its preparation
CN101071873A (en) * 2007-06-06 2007-11-14 武汉理工大学 Polymer supershort fiber reinforced fuel cell proton exchange membrane and its preparing method
CN101319051A (en) * 2008-07-15 2008-12-10 山东东岳神舟新材料有限公司 Fibre reinforcement inorganics doped multi-layer fluorine ion exchange containing film
CA2558801C (en) * 2001-12-05 2009-06-02 Honda Giken Kogyo Kabushiki Kaisha Fuel cell metallic separator and method for manufacturing same
EP2730680A1 (en) * 2012-11-08 2014-05-14 Siemens Aktiengesellschaft Bipolar plate for an electrolyser, electrolyser and method for producing a bipolar plate
CN103956506A (en) * 2014-05-22 2014-07-30 胡国良 Preparation method of composite proton exchange membrane for fuel cell

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US7807311B2 (en) * 2006-10-16 2010-10-05 Gm Global Technology Operations, Inc. Apparatus for hydrogen-air mixing in a fuel cell assembly and method

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CA2558801C (en) * 2001-12-05 2009-06-02 Honda Giken Kogyo Kabushiki Kaisha Fuel cell metallic separator and method for manufacturing same
CN1697225A (en) * 2005-05-20 2005-11-16 武汉理工大学 Composite proton exchange membrane for low humidification and long life fuel cell and its preparation
CN101071873A (en) * 2007-06-06 2007-11-14 武汉理工大学 Polymer supershort fiber reinforced fuel cell proton exchange membrane and its preparing method
CN101319051A (en) * 2008-07-15 2008-12-10 山东东岳神舟新材料有限公司 Fibre reinforcement inorganics doped multi-layer fluorine ion exchange containing film
EP2730680A1 (en) * 2012-11-08 2014-05-14 Siemens Aktiengesellschaft Bipolar plate for an electrolyser, electrolyser and method for producing a bipolar plate
CN103956506A (en) * 2014-05-22 2014-07-30 胡国良 Preparation method of composite proton exchange membrane for fuel cell

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