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DEVELOPMENT OF PRODUCTION TECHNOLOGY FOR MEMBRANE-ELECTRODE ASSEMBLIES WITH RADICAL CAPTURING LAYER

机译:具有激进捕获层的膜电极组件生产技术的开发

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This paper describes the development of mass-production technology for membrane-electrode assemblies (MEA) with a radical capturing layer and verifies its performance. Some of the authors of this paper previously developed an MEA with a radical capturing layer along the boundaries between the electrode catalyst layer and the polymer membrane to realize an endurance time of 20,000 h in accelerated daily start and daily stop (DSS) deterioration tests. Commercialization of these MEAs requires a production technology that suits mass production lines and provides reasonable cost performance. After developing a water-based slurry and selecting a gas diffusion layer (GDL), a catalyst layer forming technology uses a rotary screen method for electrode formation. Studies confirmed continuous formation of the catalyst layer, obtaining an anode/cathode thickness of 55 μm (+10/- 20)/50 μm (+10/- 20) by optimizing the opening ratio and thickness of the screen plate. A layer-forming technology developed for the radical capturing layer uses a two-fluid spraying method. Continuous formation of an 8-μm-thick (±3 μm) radical capturing layer proved feasible by determining the appropriate slurry viscosity, spray head selection, and optimization of spraying conditions.
机译:本文介绍了具有激进捕获层的膜 - 电极组件(MEA)的大规模生产技术的发展,并验证其性能。本文的一些作者之前,沿着电极催化剂层和聚合物膜之间的界限开发了一种具有激进捕获层的MEA,以实现20,000小时的加速日常开始和每日停止(DSS)劣化测试的耐久性时间。这些MEA的商业化需要生产技术,适合大规模生产线并提供合理的成本性能。在开发水基浆料并选择气体扩散层(GDL)之后,催化剂层形成技术使用旋转筛法进行电极形成。研究证实催化剂层的连续形成,通过优化筛板的开口比和厚度来获得55μm(+ 10 / -20)/50μm(+ 10 / -20)的阳极/阴极厚度。为自由基捕获层开发的层形成技术使用双流体喷射方法。通过测定适当的浆料粘度,喷头选择和喷涂条件的优化来证明可行的8μm厚(±3μm)自由基捕获层的连续形成。

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