CN115411274A - A slurry for reducing the defects of fuel cell membrane electrode catalytic layer and its preparation method - Google Patents
A slurry for reducing the defects of fuel cell membrane electrode catalytic layer and its preparation method Download PDFInfo
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- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 claims description 6
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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
- H01M4/00—Electrodes
- H01M4/86—Inert electrodes with catalytic activity, e.g. for fuel cells
- H01M4/8663—Selection of inactive substances as ingredients for catalytic active masses, e.g. binders, fillers
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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
- H01M4/00—Electrodes
- H01M4/86—Inert electrodes with catalytic activity, e.g. for fuel cells
- H01M4/88—Processes of manufacture
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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
- H01M4/00—Electrodes
- H01M4/86—Inert electrodes with catalytic activity, e.g. for fuel cells
- H01M4/88—Processes of manufacture
- H01M4/8803—Supports for the deposition of the catalytic active composition
- H01M4/881—Electrolytic membranes
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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
- H01M4/00—Electrodes
- H01M4/86—Inert electrodes with catalytic activity, e.g. for fuel cells
- H01M4/88—Processes of manufacture
- H01M4/8825—Methods for deposition of the catalytic active composition
- H01M4/8828—Coating with slurry or ink
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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
- H01M8/00—Fuel cells; Manufacture thereof
- H01M8/10—Fuel cells with solid electrolytes
- H01M8/1004—Fuel cells with solid electrolytes characterised by membrane-electrode assemblies [MEA]
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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
本发明属于燃料电池技术领域,具体涉及一种减少燃料电池膜电极催化层缺陷的浆料及其制备方法。所述浆料包括如下组分:催化剂颗粒1‑40wt.%、非活性材料0.5‑45wt.%、离聚物分散液1‑30wt.%和溶剂1‑95wt.%;所述活性材料为TiC、TiO2、LiCoO2、CaCO3、P、C、AlN、Te、Si、Ru、Rh中的一种或多种。本发明将非活性材料引入催化层浆料里,在催化层成型时可将非活性材料填补至一部分催化层缺陷中,避免了中高沸点溶剂挥发不充分,催化层成型后内部有残留这一问题,并有效降低了催化层亮点、针孔等缺陷数量及大小。
The invention belongs to the technical field of fuel cells, and in particular relates to a slurry for reducing defects in a catalytic layer of a fuel cell membrane electrode and a preparation method thereof. The slurry includes the following components: catalyst particles 1-40wt.%, inactive materials 0.5-45wt.%, ionomer dispersion 1-30wt.% and solvent 1-95wt.%; the active material is TiC One or more of , TiO 2 , LiCoO 2 , CaCO 3 , P, C, AlN, Te, Si, Ru, Rh. The present invention introduces the inactive material into the slurry of the catalytic layer, and can fill the inactive material into a part of the defects of the catalytic layer when the catalytic layer is formed, avoiding the problem of insufficient volatilization of medium and high boiling point solvents, and residual residues inside the catalytic layer after forming , and effectively reduce the number and size of defects such as bright spots and pinholes in the catalytic layer.
Description
技术领域technical field
本发明属于燃料电池技术领域,具体涉及一种减少燃料电池膜电极催化层缺陷的浆料及其制备方法。The invention belongs to the technical field of fuel cells, and in particular relates to a slurry for reducing defects in a catalytic layer of a fuel cell membrane electrode and a preparation method thereof.
背景技术Background technique
在燃料电池运行过程中,其内部氢气、空气、电子、质子与水的高效传输对于催化层的发电性能起到举足轻重地作用。一般来说,催化层先由Pt/C催化剂、高分子离聚物、溶剂混合后的浆料进行分散,形成催化层浆料,再将催化层浆料通过喷涂、刮涂或者静电纺丝手段并进行干燥制备成电极。然而,通常由上述方法制备的催化层通常存在亮点、针孔、裂纹等一系列缺陷。During the operation of the fuel cell, the efficient transport of hydrogen, air, electrons, protons and water inside plays a decisive role in the power generation performance of the catalytic layer. Generally speaking, the catalytic layer is first dispersed by the slurry mixed with Pt/C catalyst, polymer ionomer, and solvent to form the catalytic layer slurry, and then the catalytic layer slurry is sprayed, scraped or electrospun and dried to prepare electrodes. However, the catalytic layer usually prepared by the above method usually has a series of defects such as bright spots, pinholes, cracks and so on.
宏观上来看,催化层的裂纹、针孔等缺陷会对质子交换膜的耐久性产生不利影响,缺陷处的应力相对集中,膜在运行过程中该处的机械耐久性较差,会有阴阳极气体串漏的风险。此外,在燃料电池运行过程中,催化层缺陷处会产生水淹,降低气体传输,从而使膜电极性能下降。From a macro point of view, defects such as cracks and pinholes in the catalytic layer will adversely affect the durability of the proton exchange membrane. The stress at the defect is relatively concentrated, and the mechanical durability of the membrane is poor during operation, and there will be negative and positive electrodes. Risk of gas leakage. In addition, during the operation of the fuel cell, water flooding will occur in the defects of the catalytic layer, which will reduce the gas transmission and reduce the performance of the membrane electrode.
专利CN110729494A采用乙酸、乙二酸、丙酸、丙烯酸、丁酸或异丁酸中的一种或多种的混合,选择的是中沸点溶剂,可保证在干燥过程中浆料的流动性,降低了催化层在干燥过程中的颗粒团聚,减少了催化层亮点、裂纹等缺陷。然而,上述方法中的溶剂沸点均高于100℃,实际干燥过程所需时间较长,降低生产效率。此外,溶剂挥发不充分,在催化层内部有残留,将对膜电极性能与耐久性产生影响。Patent CN110729494A adopts the mixture of one or more of acetic acid, oxalic acid, propionic acid, acrylic acid, butyric acid or isobutyric acid, and chooses a medium boiling point solvent, which can ensure the fluidity of the slurry during the drying process and reduce the It prevents the particle agglomeration of the catalytic layer during the drying process, and reduces defects such as bright spots and cracks in the catalytic layer. However, the boiling points of the solvents in the above methods are all higher than 100° C., and the actual drying process takes a long time, reducing production efficiency. In addition, if the solvent is not volatilized enough, there will be residues inside the catalytic layer, which will affect the performance and durability of the membrane electrode.
发明内容Contents of the invention
本发明针对上述问题,本发明提供一种减少燃料电池膜电极催化层缺陷的浆料及其制备方法,将催化层浆料中添加非活性材料,既能规避生产效率的风险,又通过填补方式减少了催化层缺陷。The present invention aims at the above problems. The present invention provides a slurry for reducing the defects of the fuel cell membrane electrode catalytic layer and a preparation method thereof. Adding inactive materials to the catalytic layer slurry can not only avoid the risk of production efficiency, but also through the filling method Catalyst layer defects are reduced.
为了实现上述目的,本发明的技术方案如下:In order to achieve the above object, the technical scheme of the present invention is as follows:
本发明一方面提供一种减少燃料电池膜电极催化层缺陷的浆料,包括如下组分:催化剂颗粒1-40wt.%、非活性材料0.5-45wt.%、离聚物分散液1-30wt.%和溶剂1-95wt.%;One aspect of the present invention provides a slurry for reducing defects in the catalytic layer of a fuel cell membrane electrode, comprising the following components: 1-40wt.% of catalyst particles, 0.5-45wt.% of inactive materials, and 1-30wt.% of ionomer dispersion. % and solvent 1-95wt.%;
所述非活性材料为TiC、TiO2、LiCoO2、CaCO3、P、C、AlN、Te、Si、Ru、Rh中的一种或多种。The inactive material is one or more of TiC, TiO 2 , LiCoO 2 , CaCO 3 , P, C, AlN, Te, Si, Ru, Rh.
上述技术方案中,进一步地,所述催化剂颗粒为PtCo/C、PtNi/C、PtFe/C、PtCu/C、PtMo/C、AuPtCo/C、RhPtSn/C、Pt/C中的一种或多种。In the above technical solution, further, the catalyst particles are one or more of PtCo/C, PtNi/C, PtFe/C, PtCu/C, PtMo/C, AuPtCo/C, RhPtSn/C, Pt/C kind.
上述技术方案中,进一步地,所述离聚物分散液为全氟磺酸树脂分散液。。In the above technical solution, further, the ionomer dispersion is a perfluorosulfonic acid resin dispersion. .
上述技术方案中,进一步地,所述溶剂为水、甲醇、乙醇、丙醇、异丙醇、正丁醇、异丁醇、仲丁醇、叔丁醇、乙二醇、丙三醇中的一种或多种。In the above technical scheme, further, the solvent is water, methanol, ethanol, propanol, isopropanol, n-butanol, isobutanol, sec-butanol, tert-butanol, ethylene glycol, glycerol one or more.
本发明另一方面提供一种上述减少燃料电池膜电极催化层缺陷的浆料的制备方法,包括以下步骤:Another aspect of the present invention provides a method for preparing the slurry for reducing the defects of the fuel cell membrane electrode catalytic layer, comprising the following steps:
(1)催化剂与非活性材料的混合分散液制备:(1) Preparation of mixed dispersion liquid of catalyst and inactive material:
将催化剂颗粒与非活性材料以及纯水混合,搅拌,分散均匀后形成催化剂与非活性材料的混合分散液;Mix catalyst particles with inactive materials and pure water, stir, and disperse evenly to form a mixed dispersion of catalyst and inactive materials;
(2)离聚物分散液制备:(2) Preparation of ionomer dispersion:
将离聚物与溶剂混合进行超声震荡、搅拌,得到离聚物分散液;Mix the ionomer with the solvent for ultrasonic vibration and stirring to obtain the ionomer dispersion;
(3)催化层浆料制备:(3) Catalytic layer slurry preparation:
将步骤(2)得到的离聚物分散液与步骤(1)得到的催化剂与非活性材料的混合分散液搅拌,分散均匀后得到催化层浆料。Stir the ionomer dispersion obtained in step (2) with the mixed dispersion of catalyst and inactive material obtained in step (1), and disperse evenly to obtain a catalytic layer slurry.
本发明再一方面提供一种燃料电池膜电极CCM,包括质子交换膜和质子交换膜两侧的阳极催化层和阴极催化层,所述阳极催化层和/或阴极催化层由上述催化层浆料喷涂或涂布于质子交换膜制成。Another aspect of the present invention provides a fuel cell membrane electrode CCM, comprising a proton exchange membrane and an anode catalyst layer and a cathode catalyst layer on both sides of the proton exchange membrane, and the anode catalyst layer and/or the cathode catalyst layer are made of the above catalyst layer slurry It is made by spraying or coating on the proton exchange membrane.
本发明还提供一种燃料电池膜电极,包括上述的CCM,在所述CCM的两侧上设置气体扩散层,得到膜电极。The present invention also provides a fuel cell membrane electrode, comprising the above-mentioned CCM, and gas diffusion layers are arranged on both sides of the CCM to obtain a membrane electrode.
本发明的有益效果为:The beneficial effects of the present invention are:
本发明将非活性材料引入催化层浆料里,在催化层成型时可将非活性材料填补至一部分催化层缺陷中,避免了中高沸点溶剂挥发不充分,催化层成型后内部有残留这一问题,并有效降低了催化层亮点、针孔等缺陷数量及大小。另外,添加该非活性材料对MEA性能无影响,有效提升了催化层成型质量。The invention introduces the inactive material into the slurry of the catalytic layer, and the inactive material can be filled into a part of the defects of the catalytic layer when the catalytic layer is formed, so as to avoid the problem of insufficient volatilization of medium and high boiling point solvents and residues in the catalytic layer after forming , and effectively reduce the number and size of defects such as bright spots and pinholes in the catalytic layer. In addition, the addition of the inactive material has no effect on the performance of the MEA, and effectively improves the molding quality of the catalytic layer.
附图说明Description of drawings
图1为本发明实施例1所制备的催化层显微镜表征图;Fig. 1 is the microscopic characterization figure of the catalytic layer prepared by the embodiment of the
图2为本发明对比例1所制备的催化层显微镜表征图;Fig. 2 is the microscopic characterization figure of the catalytic layer prepared by comparative example 1 of the present invention;
图3为本发明实施例1与对比例1所制备的MEA性能表征图。FIG. 3 is a performance characterization diagram of the MEA prepared in Example 1 and Comparative Example 1 of the present invention.
具体实施方式Detailed ways
为使本发明专利实施例的目的、技术方案和优点更加清楚,下面将结合本发明实施例中的附图及表格,对本发明专利实施例中的技术方案进行清楚、完整地描述。所描述的实施例是本发明专利一部分实施例,而不是全部的实施例。基于本发明专利中的实施例,本领域其他技术人员在没有做出创造性劳动前提下所获得的所有其他实施例,都属于本发明专利保护的范围。In order to make the purpose, technical solutions and advantages of the patented embodiments of the present invention clearer, the technical solutions in the patented embodiments of the present invention will be clearly and completely described below in conjunction with the drawings and tables in the embodiments of the present invention. The described embodiments are some, not all, embodiments of the patent of the present invention. Based on the embodiments in the patent of the present invention, all other embodiments obtained by those skilled in the art without making creative efforts belong to the protection scope of the patent of the present invention.
实施例1Example 1
一种减少燃料电池膜电极催化层缺陷的浆料,包括如下组分:包括9wt.%的催化剂颗粒、0.6wt.%的非活性材料,24wt.%的离聚物分散液、66.4wt.%的溶剂;其中,催化剂颗粒为Pt/C颗粒,非活性材料为C材料,离聚物分散液为全氟磺酸树脂分散液,溶剂为水、乙醇和异丙醇的混合溶剂。A slurry for reducing the defects of the fuel cell membrane electrode catalytic layer, comprising the following components: 9wt.% catalyst particles, 0.6wt.% inactive materials, 24wt.% ionomer dispersion, 66.4wt.% solvent; wherein, the catalyst particles are Pt/C particles, the inactive material is C material, the ionomer dispersion is a perfluorosulfonic acid resin dispersion, and the solvent is a mixed solvent of water, ethanol and isopropanol.
实施例1催化层浆料制备方法具体步骤如下:The concrete steps of
(1)催化剂与非活性材料的混合分散液制备:将催化剂颗粒与非活性材料以及纯水混合,转速为1000rpm/min,搅拌15min,分散均匀后形成催化剂与非活性材料的混合分散液;(1) Preparation of mixed dispersion of catalyst and inactive material: mix catalyst particles with inactive material and pure water at a speed of 1000 rpm/min, stir for 15 min, and form a mixed dispersion of catalyst and inactive material after dispersing evenly;
(2)离聚物分散液制备:将离聚物与溶剂混合进行超声震荡、转速为1000rpm/min,然后搅拌15min,得到离聚物分散液;(2) Preparation of the ionomer dispersion: mix the ionomer with a solvent for ultrasonic vibration at a speed of 1000 rpm/min, and then stir for 15 minutes to obtain the ionomer dispersion;
(3)催化层浆料制备:将步骤(2)中的高分子离聚物溶液与步骤(1)中的催化剂与非活性材料的混合分散液用搅拌器搅拌约15min,转速为1500rpm/min,然后将混合浆料采取球磨方式进行分散,并最终制得催化层浆料。(3) Catalyst layer slurry preparation: the polymer ionomer solution in step (2) and the mixed dispersion liquid of the catalyst and inactive material in step (1) were stirred with a stirrer for about 15min, and the rotating speed was 1500rpm/min , and then disperse the mixed slurry by means of ball milling, and finally prepare the catalytic layer slurry.
对比例1Comparative example 1
对比例1催化层浆料制备方法除不添加非活性材料外,其余与实施例1一致。The preparation method of the catalytic layer slurry of Comparative Example 1 is consistent with that of Example 1 except that no inactive materials are added.
分别将实施例1与对比例1制得的浆料通过喷涂或涂布方式使之成型,并用光学显微镜表征催化层缺陷,呈像范围为13*10mm。实施例1及对比例1所制备的催化层显微镜表征图分别如图1和图2所示。从图中可以看出,催化层添加非活性材料缺陷个数大幅减少,13mm*10mm视野范围内缺陷个数从10729个减少至1190个。另外,亮点平均半径也有所降低,由21.2μm降至12μm。由此可见,催化层浆料添加非活性材料可降低成型缺陷大小与数量。The slurries prepared in Example 1 and Comparative Example 1 were molded by spraying or coating, and the defects of the catalytic layer were characterized by an optical microscope, and the imaging range was 13*10mm. The microscopic representations of the catalytic layers prepared in Example 1 and Comparative Example 1 are shown in Figure 1 and Figure 2, respectively. It can be seen from the figure that the number of defects added to the catalytic layer has been greatly reduced, and the number of defects in the field of view of 13mm*10mm has been reduced from 10729 to 1190. In addition, the average radius of bright spots has also decreased from 21.2 μm to 12 μm. It can be seen that adding inactive materials to the catalytic layer slurry can reduce the size and number of molding defects.
实施例1与对比例1制得的浆料缺陷统计如表1所示。Table 1 shows the defect statistics of the slurry prepared in Example 1 and Comparative Example 1.
表1Table 1
分别对实施例1和对比例1的浆料所成型的催化层,进行组装成膜电极,进行电化学性能测试,结果如图3所示。。The catalytic layers formed by the slurries of Example 1 and Comparative Example 1 were respectively assembled into film-forming electrodes and tested for electrochemical performance. The results are shown in FIG. 3 . .
测试条件如下:电池温度为80℃;阳极侧氢气的化学计量比为2,阴极侧空气的化学计量比为2;阴极侧相对湿度为0%,阳极侧相对湿度为50%;阳极侧氢气压力为170kpa,阴极侧空气压力为150kpa。The test conditions are as follows: the battery temperature is 80°C; the stoichiometric ratio of hydrogen on the anode side is 2, and the stoichiometric ratio of air on the cathode side is 2; the relative humidity on the cathode side is 0%, and the relative humidity on the anode side is 50%; the hydrogen pressure on the anode side is It is 170kpa, and the air pressure on the cathode side is 150kpa.
从图3可以看出,催化层添加非活性材料极化曲线与不添加非活性材料具有高度重合,在2000mA/cm2条件下,二者电压分别均为0.65V。It can be seen from Figure 3 that the polarization curves of the catalytic layer with inactive materials and without inactive materials are highly overlapped. Under the condition of 2000mA/cm 2 , the voltages of both are 0.65V respectively.
以上实施例仅仅是本发明的优选施例,并非对于实施方式的限定。本发明的保护范围应当以权利要求所限定的范围为准。在上述说明的基础上还可以做出其它不同形式的变化或变动。由此所引伸出的显而易见的变化或变动仍处于本发明创造的保护范围之中。The above embodiments are only preferred embodiments of the present invention, and are not intended to limit the implementation. The protection scope of the present invention should be determined by the scope defined in the claims. On the basis of the above description, other changes or changes in different forms can also be made. Obvious changes or variations derived therefrom are still within the scope of protection of the present invention.
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