CN116093345A - A nanofiber catalytic layer membrane and fuel cell membrane electrode based on electrospinning and its preparation method - Google Patents
A nanofiber catalytic layer membrane and fuel cell membrane electrode based on electrospinning and its preparation method Download PDFInfo
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- CN116093345A CN116093345A CN202310246660.7A CN202310246660A CN116093345A CN 116093345 A CN116093345 A CN 116093345A CN 202310246660 A CN202310246660 A CN 202310246660A CN 116093345 A CN116093345 A CN 116093345A
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- 239000012528 membrane Substances 0.000 title claims abstract description 102
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- HEDRZPFGACZZDS-UHFFFAOYSA-N Chloroform Chemical compound ClC(Cl)Cl HEDRZPFGACZZDS-UHFFFAOYSA-N 0.000 claims description 4
- IAZDPXIOMUYVGZ-UHFFFAOYSA-N Dimethylsulphoxide Chemical compound CS(C)=O IAZDPXIOMUYVGZ-UHFFFAOYSA-N 0.000 claims description 4
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- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
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Abstract
Description
技术领域technical field
本发明属于膜电极技术领域,尤其涉及一种基于静电纺丝的纳米纤维催化层膜和燃料电池膜电极及其制备方法。The invention belongs to the technical field of membrane electrodes, and in particular relates to a nanofiber catalytic layer membrane based on electrospinning, a fuel cell membrane electrode and a preparation method thereof.
背景技术Background technique
当今全世界由于气候的加速变化、能源资源的不断约束导致的能源结构深度调整的大环境下,氢能已经是公认的战略方向之一,备受关注。由于燃料电池不需要经过热机的卡诺循环而具有更高的效率,同时使用过程中不存在排放物而绿色环保,因此燃料电池是氢能重要应用方向之一。燃料电池正处在商业化应用的初期上升阶段,面临寿命不足、成本高等问题。而其核心部件-膜电极的制备工艺较为复杂,性能、生产效率、良品率等对燃料电池成本和寿命都至关重要。In today's environment where the world's energy structure is deeply adjusted due to accelerated climate change and constant constraints on energy resources, hydrogen energy has become one of the recognized strategic directions and has attracted much attention. Since the fuel cell does not need to go through the Carnot cycle of the heat engine, it has higher efficiency, and at the same time, there is no emission during use and is environmentally friendly, so the fuel cell is one of the important application directions of hydrogen energy. Fuel cells are in the initial rising stage of commercial application, facing problems such as short lifespan and high cost. However, the preparation process of its core component, the membrane electrode, is relatively complicated, and its performance, production efficiency, and yield rate are all crucial to the cost and life of the fuel cell.
目前膜电极连续生产工艺是基于喷涂、刮涂和丝网印刷等工艺直接将催化层制备到质子交换膜上形成膜电极,或将催化层制备到其他基底材料表面,然后通过热转印等工艺将催化层转印到质子交换膜上制备膜电极。At present, the continuous production process of membrane electrodes is based on processes such as spray coating, scrape coating and screen printing to directly prepare the catalytic layer on the proton exchange membrane to form a membrane electrode, or prepare the catalytic layer on the surface of other substrate materials, and then use thermal transfer printing and other processes The catalytic layer was transferred to the proton exchange membrane to prepare the membrane electrode.
专利《一种生产膜电极的工艺方法》中,通过热转印工艺方法、热复合工艺方法、碳纸贴合工艺方法及热压工艺方法,该方法虽然可实现连续自动化生产,但是转印过程对于质子交换膜损伤较大,不利于膜电极耐久性。专利《一种燃料电池用膜-膜电极的集成化制备方法》提出的是从树脂溶液开始制备质子交换膜和膜电极,该方法具备工艺简单和易于实现规模化生产,但是在制备质子交换膜之后,不经过产品良率验证,直接进行膜电极制备,可能存在产品良率低的问题。In the patent "A Process Method for Producing Membrane Electrodes", through thermal transfer printing process, thermal composite process, carbon paper bonding process and hot pressing process, although this method can realize continuous automatic production, the transfer process The damage to the proton exchange membrane is relatively large, which is not conducive to the durability of the membrane electrode. The patent "A Membrane-Membrane Electrode Integrated Preparation Method for Fuel Cell" proposes to prepare proton exchange membrane and membrane electrode from resin solution. This method has simple process and is easy to realize large-scale production. After that, if the membrane electrode is prepared directly without product yield verification, there may be a problem of low product yield.
发明内容Contents of the invention
有鉴于此,本发明的目的在于提供一种基于静电纺丝的纳米纤维催化层膜和燃料电池膜电极及其制备方法,该催化层膜能单独成卷;其具备通孔结构、沿纤维短传输路径等优势可实现高传质,制备的膜电极具备高性能。In view of this, the object of the present invention is to provide a nanofiber catalytic layer membrane based on electrospinning and a fuel cell membrane electrode and a preparation method thereof. The catalytic layer membrane can be rolled separately; Advantages such as the transmission path can achieve high mass transfer, and the prepared membrane electrode has high performance.
本发明提供了一种基于静电纺丝的纳米纤维催化层膜,由催化剂纺丝浆料静电纺丝制得;The invention provides a nanofiber catalytic layer membrane based on electrospinning, which is prepared by electrospinning catalyst spinning slurry;
所述催化剂纺丝浆料中包括树脂、催化剂、高分子载体和溶剂;The catalyst spinning slurry includes resin, catalyst, polymer carrier and solvent;
所述高分子载体选自聚丙烯酸、聚氧化乙烯、聚四氟乙烯、聚偏氯乙烯、聚乙烯醇、聚醋酸乙烯、聚丙烯腈和聚甲基丙烯酸酯中的一种或多种。The polymer carrier is selected from one or more of polyacrylic acid, polyethylene oxide, polytetrafluoroethylene, polyvinylidene chloride, polyvinyl alcohol, polyvinyl acetate, polyacrylonitrile and polymethacrylate.
现有技术中催化层直接做在质子交换膜上,或做在类似PTFE等材料上。由于质子交换膜或PTFE等材料连带着催化层,催化层进一步的高温处理的温度受限。本发明由于催化层可以独立成膜,因此不受后处理温度等条件限制。本发明提供的基于静电纺丝的纳米纤维催化层膜能够单独剥离成膜(见图1);证明催化层膜与基底材料剥离可行性。In the prior art, the catalytic layer is directly formed on the proton exchange membrane, or on materials such as PTFE. Since materials such as proton exchange membrane or PTFE are attached to the catalytic layer, the temperature for further high-temperature treatment of the catalytic layer is limited. In the present invention, since the catalytic layer can be formed into a film independently, it is not limited by post-treatment temperature and other conditions. The nanofiber catalytic layer film based on electrospinning provided by the present invention can be peeled off separately to form a film (see FIG. 1 ); it proves the feasibility of peeling off the catalytic layer film from the base material.
在本发明中,所述树脂选自长支链型全氟磺酸树脂、短支链型全氟磺酸树脂、磺化聚苯乙烯、磺化聚芳醚砜、磺化聚醚醚酮、聚偏氟乙烯、聚四氟乙烯和四氟乙烯-共聚-六氟乙烯中的一种或多种;In the present invention, the resin is selected from long-chain branched perfluorosulfonic acid resin, short-chain branched perfluorosulfonic acid resin, sulfonated polystyrene, sulfonated polyarylether sulfone, sulfonated polyether ether ketone, One or more of polyvinylidene fluoride, polytetrafluoroethylene and tetrafluoroethylene-co-hexafluoroethylene;
所述溶剂选自水、异丙醇、正丙醇、乙醇、甲醇、N,N-二甲基甲酰胺、二甲基亚砜和氯仿中的一种或多种;The solvent is selected from one or more of water, isopropanol, n-propanol, ethanol, methanol, N,N-dimethylformamide, dimethylsulfoxide and chloroform;
所述催化剂选自铂碳催化剂、铂基合金催化剂和非贵金属催化剂中的一种或多种。The catalyst is selected from one or more of platinum-carbon catalysts, platinum-based alloy catalysts and non-noble metal catalysts.
在本发明中,所述树脂、催化剂、高分子载体和溶剂的质量比为(0.1~5):(0.1~5):(0.01~2):(1~60)。In the present invention, the mass ratio of the resin, catalyst, polymer carrier and solvent is (0.1-5): (0.1-5): (0.01-2): (1-60).
在本发明中,所述催化剂纺丝浆料由树脂、催化剂、高分子载体和溶剂混合制得;In the present invention, the catalyst spinning slurry is prepared by mixing resin, catalyst, polymer carrier and solvent;
所述混合的方式选自超声、珠磨、搅拌和均质中的一种或多种。The mixing method is selected from one or more of ultrasonic, bead milling, stirring and homogenization.
在本发明中,所述催化剂纺丝浆料静电纺丝时的电压为0.1~100kv,喷头与接收基底的距离为1~20cm,温度为15~80℃,湿度为10%RH~80RH%;In the present invention, the electrospinning voltage of the catalyst spinning slurry is 0.1-100kv, the distance between the nozzle and the receiving substrate is 1-20cm, the temperature is 15-80°C, and the humidity is 10%RH-80RH%;
针头选自针式喷头、无针式喷头或多微孔喷头。The needles are selected from needle showers, needleless showers or microporous showers.
在本发明中,所述接收基底选自离型纸、硅油纸或铝箔。In the present invention, the receiving substrate is selected from release paper, silicone oil paper or aluminum foil.
在本发明中,所述阴极纳米纤维催化层膜的载量为0.05~1mgPt/cm2;In the present invention, the loading capacity of the cathode nanofiber catalytic layer membrane is 0.05-1 mg Pt /cm 2 ;
所述阳极纳米纤维催化层膜的载量为0.05~1mgPt/cm2。The loading capacity of the anode nanofiber catalytic layer membrane is 0.05-1 mg Pt /cm 2 .
本发明纳米纤维催化层膜是通过静电纺丝在基底材料上制得;如图2所示,将基底材料放置料轴A上,通过辊压轴a进行牵引,基底材料按照设定速度前进,该速度主要根据催化层载量设定;纺丝设备在料轴B出进行纺丝,在辊压轴c处进行催化层膜和基底材料剥离,基底材料通过轴d收卷至料轴C;催化层膜经过轴e,再经过后处理工序收卷至料轴D,制备得到催化层膜。The nanofiber catalytic layer film of the present invention is made on the base material by electrospinning; as shown in Figure 2, the base material is placed on the material shaft A, pulled by the roller pressing shaft a, and the base material advances according to the set speed, the The speed is mainly set according to the loading capacity of the catalytic layer; the spinning equipment spins out of the material shaft B, and the catalytic layer film and the substrate material are peeled off at the roller pressing shaft c, and the substrate material is wound to the material shaft C through the shaft d; the catalytic layer The film passes through the axis e, and then winds up to the material axis D through the post-treatment process to prepare the catalytic layer film.
所述催化层膜包括催化剂、树脂和高分子载体(PAA等),通过纤维编制成催化层,因此具有一定强度可单独成卷,利于催化层的单独后处理。在本发明中,催化剂纺丝浆料静电纺丝后还包括后处理;The catalytic layer membrane includes catalyst, resin and polymer carrier (PAA, etc.), and is woven into a catalytic layer through fibers, so it has a certain strength and can be rolled separately, which is beneficial to the separate post-treatment of the catalytic layer. In the present invention, post-treatment is also included after the electrospinning of the catalyst spinning slurry;
所述后处理包括热辊压、平板加热、红外加热或鼓风烘箱加热。The post-treatment includes hot rolling, flat plate heating, infrared heating or blast oven heating.
本发明提供了一种燃料电池膜电极,包括阴极纳米纤维催化层膜、质子交换膜和阳极纳米纤维催化层膜;The invention provides a fuel cell membrane electrode, comprising a cathode nanofiber catalyst layer membrane, a proton exchange membrane and an anode nanofiber catalyst layer membrane;
所述阴极纳米纤维催化层膜和阳极纳米纤维催化层膜均为上述技术方案所述纳米纤维催化层膜。Both the cathode nanofiber catalyst layer membrane and the anode nanofiber catalyst layer membrane are nanofiber catalyst layer membranes described in the above technical solution.
本发明提供了一种上述技术方案所述燃料电池膜电极的制备方法,包括以下步骤:The present invention provides a method for preparing a fuel cell membrane electrode described in the above technical solution, comprising the following steps:
将阳极纳米纤维催化层膜、质子交换膜和阴极纳米纤维催化层膜复合,得到膜电极;Composite the anode nanofiber catalyst layer membrane, the proton exchange membrane and the cathode nanofiber catalyst layer membrane to obtain a membrane electrode;
所述复合的压力为0.1~10MPa,复合的温度为10~140℃。The compounding pressure is 0.1-10MPa, and the compounding temperature is 10-140°C.
如图3所示,在一个具体实施例中,所述燃料电池膜电极的制备方法包括:将质子交换膜放置料轴E,将质子交换膜背膜剥离后收集至料轴F,质子交换膜通过辊压轴f牵引;阳极催化层膜和阴极催化层膜分别放置料轴G和料轴H,分别通过辊压轴h和辊压轴i牵引;质子交换膜、阳极纳米纤维催化层膜和阴极纳米纤维催化层膜通过辊压轴j和料轴k进行复合制备得到CCM产品,与背膜复合收集至料轴I;料轴j和料轴k处的复合工艺可控制压力、温度等参数。As shown in Figure 3, in a specific embodiment, the preparation method of the fuel cell membrane electrode includes: placing the proton exchange membrane on the material axis E, stripping the back film of the proton exchange membrane and collecting it on the material axis F, and the proton exchange membrane Traction by the roller pressing shaft f; the anode catalytic layer film and the cathode catalytic layer film are respectively placed on the material axis G and the material axis H, and are respectively pulled by the roller pressing axis h and the rolling axis i; the proton exchange membrane, the anode nanofiber catalytic layer membrane and the cathode nanofiber The catalytic layer film is prepared by compounding the roll pressing axis j and the material axis k to obtain the CCM product, which is combined with the back film and collected to the material axis I; the composite process at the material axis j and the material axis k can control parameters such as pressure and temperature.
参见图4:具体实施例中,所述燃料电池膜电极的制备方法具体包括S1:催化剂纺丝浆料的制备;S2:纳米纤维催化层膜制备工艺;S3:CCM制备-纳米纤维催化层膜与质子交换膜复合工艺。上述膜电极的生产过程灵活,质量可控,可实现降低CCM制备成本、提升良率的效果;与质子交换膜的复合过程较为温和,对其损伤较小,且在一定程度上缓解静电纺丝工艺的低效率问题。Referring to Fig. 4: in the specific embodiment, the preparation method of the fuel cell membrane electrode specifically includes S1: preparation of catalyst spinning slurry; S2: preparation process of nanofiber catalytic layer membrane; S3: CCM preparation-nanofiber catalytic layer membrane Composite process with proton exchange membrane. The production process of the above-mentioned membrane electrode is flexible and the quality is controllable, which can reduce the cost of CCM preparation and improve the yield rate; the composite process with the proton exchange membrane is relatively mild, with less damage to it, and to a certain extent alleviates the effects of electrospinning. Process inefficiencies.
本发明通过静电纺丝制备的纳米纤维催化层膜,具备通孔结构、沿纤维短传输路径等优势可实现高传质,膜电极具备高性能,如极化性能;其能单独成卷作为产品,利于催化层的中间处理,以及与质子交换膜的灵活匹配;实现催化层膜与质子交换膜的单独生产,加快催化剂涂覆膜(CCM)生产效率和灵活性。此外,催化层膜与质子交换膜温和复合工艺,可解决热转印工艺中对质子交换膜造成的损伤问题。The nanofiber catalytic layer membrane prepared by electrospinning in the present invention has the advantages of through-hole structure and short transmission path along the fiber, which can realize high mass transfer, and the membrane electrode has high performance, such as polarization performance; it can be rolled into a single product as a product , which is conducive to the intermediate treatment of the catalytic layer and the flexible matching with the proton exchange membrane; realizes the separate production of the catalytic layer membrane and the proton exchange membrane, and accelerates the production efficiency and flexibility of the catalyst coated membrane (CCM). In addition, the mild composite process of the catalytic layer membrane and the proton exchange membrane can solve the problem of damage to the proton exchange membrane caused by the thermal transfer process.
附图说明Description of drawings
图1为催化层膜单独剥离成膜的示意图;Fig. 1 is the schematic diagram that catalytic layer film is peeled off separately;
图2为具体实施例中催化层膜的制备流程示意图;Fig. 2 is the preparation flow diagram of catalytic layer film in specific embodiment;
图3为具体实施例中催化层膜与质子交换膜复合成膜电极的工艺过程;Fig. 3 is the technological process of composite film-forming electrode of catalyst layer membrane and proton exchange membrane in the specific embodiment;
图4为本发明具体实施例中基于静电纺丝的燃料电池膜电极的工艺过程;Fig. 4 is the technological process of the fuel cell membrane electrode based on electrospinning in the specific embodiment of the present invention;
图5为本发明实施例和对比例制备的膜电极的电化学活性面积(ECSA)比较;Fig. 5 compares the electrochemically active area (ECSA) of the membrane electrode prepared by the embodiment of the present invention and comparative example;
图6为本发明实施例和对比例制备的膜电极的电池测试性能结果。Fig. 6 is the battery test performance results of the membrane electrodes prepared in the examples and comparative examples of the present invention.
具体实施方式Detailed ways
为了进一步说明本发明,下面结合实施例对本发明提供的一种基于静电纺丝的纳米纤维催化层膜和燃料电池膜电极及其制备方法进行详细地描述,但不能将它们理解为对本发明保护范围的限定。In order to further illustrate the present invention, a kind of electrospinning-based nanofiber catalytic layer film and fuel cell membrane electrode and preparation method thereof provided by the present invention are described in detail below in conjunction with the examples, but they cannot be interpreted as limiting the protection scope of the present invention. limit.
对比例1Comparative example 1
传统催化层制备Preparation of traditional catalytic layer
通过超声喷涂方法制备阴极载量0.15mgPt/cm2和阳极载量0.05mgPt/cm2的膜电极,所制备膜电极装入标准单池,80℃,100% RH测试H2/Air下的极化性能。A membrane electrode with a cathode loading of 0.15 mg Pt /cm 2 and an anode loading of 0.05 mg Pt /cm 2 was prepared by ultrasonic spraying. The prepared membrane electrode was loaded into a standard single cell and tested under H 2 /Air at 80°C and 100% RH polarization performance.
实施例1Example 1
阴极催化层膜制备:称取阴极催化剂Pt/C(57wt%Pt)2.7g,加入9g水和9g异丙醇作为溶剂,在加入4.57g 20wt%全氟磺酸树脂,超声1h。再加入0.5g 45万分子量的PAA,搅拌48h;在质子交换膜的一侧,7×7cm区域上,通过静电纺丝(电压30kV,流速1mL/h,针头和接收器距离10cm)制备0.15mgPt/cm2阴极催化层膜;Cathodic catalyst layer film preparation: Weigh 2.7g of cathode catalyst Pt/C (57wt%Pt), add 9g of water and 9g of isopropanol as solvent, add 4.57g of 20wt% perfluorosulfonic acid resin, and sonicate for 1h. Then add 0.5g of PAA with a molecular weight of 450,000, and stir for 48h; prepare 0.15mg of PAA by electrospinning (voltage 30kV, flow rate 1mL/h, distance between needle and receiver 10cm) on one side of the proton exchange membrane, on a 7×7cm area. Pt / cm2 cathode catalytic layer film;
阳极催化层膜制备:称取阳极催化剂Pt/C(50wt%Pt)2g,加入7g水和7g异丙醇作为溶剂,在加入4.5g 20wt%全氟磺酸树脂,超声1h。再加入0.5g45万分子量的PAA,搅拌48h;在质子交换膜的一侧,7×7cm区域上,通过静电纺丝(电压25kV,流速0.5mL/h,针头和接收器距离10cm)制备0.05mgPt/cm2阳极催化层膜;Preparation of the anode catalyst layer film: Weigh 2g of the anode catalyst Pt/C (50wt%Pt), add 7g of water and 7g of isopropanol as solvents, add 4.5g of 20wt% perfluorosulfonic acid resin, and sonicate for 1h. Then add 0.5g of PAA with a molecular weight of 450,000, and stir for 48h; prepare 0.05mg by electrospinning (voltage 25kV, flow rate 0.5mL/h, distance between needle and receiver 10cm) on one side of the proton exchange membrane, on a 7×7cm area. Pt /cm 2 anode catalyst layer film;
所制备膜电极装入标准单池,80℃,100% RH测试H2/Air下的极化性能。The prepared membrane electrode was loaded into a standard single cell, and the polarization performance under H 2 /Air was tested at 80°C and 100% RH.
实施例2Example 2
热处理的催化层膜制备:Heat-treated catalytic layer film preparation:
阴极催化层膜制备:称取阴极催化剂Pt/C(57wt%Pt)2.7g,加入9g水和9g异丙醇作为溶剂,在加入4.57g20wt%全氟磺酸树脂,超声1h。再加入0.5g 45万分子量的PAA,搅拌48h;在7×7cm的离型纸上,通过静电纺丝(电压30kV,流速1mL/h,针头和接收器距离10cm)制备0.15mgPt/cm2阴极催化层膜,将催化层膜剥离,放置烘箱150℃热处理20min;Cathodic catalyst layer film preparation: Weigh 2.7g of cathode catalyst Pt/C (57wt%Pt), add 9g of water and 9g of isopropanol as solvent, add 4.57g of 20wt% perfluorosulfonic acid resin, and sonicate for 1h. Then add 0.5g PAA with a molecular weight of 450,000, and stir for 48h; prepare 0.15mg Pt / cm2 by electrospinning (voltage 30kV, flow rate 1mL/h, distance between needle and receiver 10cm) on a 7×7cm release paper For the cathode catalytic layer film, peel off the catalytic layer film and place it in an oven for heat treatment at 150°C for 20 minutes;
阳极催化层膜制备:称取阳极催化剂Pt/C(50wt%Pt)2g,加入7g水和7g异丙醇作为溶剂,在加入4.5g 20wt%全氟磺酸树脂,超声1h。再加入0.5g45万分子量的PAA,搅拌48h;在7×7cm的离型纸,通过静电纺丝(电压25kV,流速0.5mL/h,针头和接收器距离10cm)制备0.05mgPt/cm2阳极催化层膜,将催化层膜剥离,放置烘箱150℃热处理20min;Preparation of the anode catalyst layer film: Weigh 2g of the anode catalyst Pt/C (50wt%Pt), add 7g of water and 7g of isopropanol as solvents, add 4.5g of 20wt% perfluorosulfonic acid resin, and sonicate for 1h. Then add 0.5g of PAA with a molecular weight of 450,000 and stir for 48h; prepare a 0.05mg Pt / cm2 anode by electrospinning (voltage 25kV, flow rate 0.5mL/h, needle and receiver distance 10cm) on a 7×7cm release paper Catalytic layer film, peel off the catalytic layer film, and place it in an oven for heat treatment at 150°C for 20 minutes;
将阳极催化层膜、质子交换膜、阳极催化层膜按照图3所示工艺热压复合,得到膜电极;The anode catalyst layer membrane, the proton exchange membrane, and the anode catalyst layer membrane are hot-pressed and composited according to the process shown in Figure 3 to obtain a membrane electrode;
将所制备的膜电极装入标准电池,80℃,100%RH测试H2/Air下的极化性能。The prepared membrane electrode was loaded into a standard battery, and the polarization performance under H 2 /Air was tested at 80° C. and 100% RH.
图5为本发明实施例和对比例制备的膜电极的电化学活性面积(ECSA)比较,实施例2>实施例1>对比例1,说明纳米纤维膜催化层内催化剂的利用率高于对比例1中的传统催化层,且热压工艺处理后催化剂利用率也明显提升,说明热压工艺促进纤维之间的结构重排,并且高温利于树脂在催化剂表面的均匀分布,可提升性能;Fig. 5 compares the electrochemically active area (ECSA) of the membrane electrode prepared by the embodiment of the present invention and comparative example, embodiment 2>embodiment 1>comparative example 1, illustrates that the utilization rate of the catalyst in the nanofiber membrane catalyst layer is higher than that of the pair The traditional catalytic layer in ratio 1, and the utilization rate of the catalyst after the hot-pressing process is also significantly improved, indicating that the hot-pressing process promotes the structural rearrangement between fibers, and high temperature is conducive to the uniform distribution of resin on the surface of the catalyst, which can improve performance;
图6为本发明实施例和对比例制备的膜电极的电池性能极化曲线比较,实施例2制备的膜电极在2000mA/cm2下达到0.637V,实施例1制备的膜电极在2000mA/cm2下达到0.597V,而对比例1制备的膜电极在2000mA/cm2达到0.568V;可以看出,实施例2中的膜电极比传统膜电极在高电密区具备更优的传质能力,因此相同电流密度下体现更高的电压性能。Figure 6 is a comparison of the battery performance polarization curves of the membrane electrodes prepared in the examples of the present invention and comparative examples. The membrane electrodes prepared in Example 2 reached 0.637V at 2000mA/cm 2 2 and reached 0.597V, while the membrane electrode prepared in Comparative Example 1 reached 0.568V at 2000mA/cm 2 ; it can be seen that the membrane electrode in Example 2 has better mass transfer capacity than the traditional membrane electrode in the high density area , so it shows higher voltage performance at the same current density.
由以上实施例可知,本发明提供了一种基于静电纺丝的纳米纤维催化层膜,由催化剂纺丝浆料静电纺丝制得;所述催化剂纺丝浆料中包括树脂、催化剂、高分子载体和溶剂;所述高分子载体选自聚丙烯酸、聚氧化乙烯、聚四氟乙烯、聚偏氯乙烯、聚乙烯醇、聚醋酸乙烯、聚丙烯腈和聚甲基丙烯酸酯中的一种或多种。该催化层膜采用高分子载体作为原料之一,再结合静电纺丝编制而成,具有一定强度能单独成膜;利于其中间处理,以及与质子交换膜灵活匹配;与质子交换膜复合后的膜电极具有较高的极化性能。As can be seen from the above examples, the present invention provides a nanofiber catalytic layer film based on electrospinning, which is prepared by electrospinning of catalyst spinning slurry; the catalyst spinning slurry includes resin, catalyst, polymer carrier and solvent; the polymer carrier is selected from one or more of polyacrylic acid, polyethylene oxide, polytetrafluoroethylene, polyvinylidene chloride, polyvinyl alcohol, polyvinyl acetate, polyacrylonitrile and polymethacrylate Various. The catalytic layer membrane is made of polymer carrier as one of the raw materials, combined with electrospinning, which has a certain strength and can be formed into a film alone; it is conducive to its intermediate treatment and flexible matching with the proton exchange membrane; Membrane electrodes have high polarizability.
以上所述仅是本发明的优选实施方式,应当指出,对于本技术领域的普通技术人员来说,在不脱离本发明原理的前提下,还可以做出若干改进和润饰,这些改进和润饰也应视为本发明的保护范围。The above is only a preferred embodiment of the present invention, it should be pointed out that, for those of ordinary skill in the art, without departing from the principle of the present invention, some improvements and modifications can also be made, and these improvements and modifications can also be made. It should be regarded as the protection scope of the present invention.
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