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采用电解质集成聚合物涂层集流体方法扩大基于聚四氟乙烯的气体扩散电极规模。

Scale-Up of PTFE-Based Gas Diffusion Electrodes Using an Electrolyte-Integrated Polymer-Coated Current Collector Approach.

作者信息

Filippi Michael, Möller Tim, Pastusiak Remigiusz, Magori Erhard, Paul Benjamin, Strasser Peter

机构信息

The Electrochemical Energy, Catalysis, and Materials Science Laboratory, Department of Chemistry, Chemical Engineering Division, Technical University Berlin, 10623 Berlin, Germany.

Siemens Energy (SE) New Energy Business (NEB) Technology & Products (TP) Development (DEV), Siemens Energy Global GmbH & Co. KG, 81739 Munich, Germany.

出版信息

ACS Energy Lett. 2024 Mar 3;9(4):1361-1368. doi: 10.1021/acsenergylett.4c00114. eCollection 2024 Apr 12.

Abstract

Nonconductive porous polymer substrates, such as PTFE, have been pivotal in the fabrication of stable and high-performing gas diffusion electrodes (GDEs) for the reduction of CO/CO in small scale electrolyzers; however, the scale-up of polymer-based GDEs without performance penalties to technologically more relevant electrode sizes has remained elusive. This work reports on a new current collector concept that enables the scale-up of PTFE-based GDEs from 5 to 100 cm and beyond. The present approach builds on a multifunctional current collector concept that enables multipoint front-contacting of thin catalyst coatings, which mitigates performance losses even for high resistivity cathodes. Our improved current collector design concomitantly incorporates a flow-field functionality in a monopolar plate configuration, keeping electrolyte gaps small for increased performance. Experiments with 100 cm cathodes were conducted in a one-gap alkaline AEM and acid CEM system. Our design represents an important step forward in the development of larger-size CO electrolyzers.

摘要

非导电多孔聚合物基材,如聚四氟乙烯(PTFE),在制造用于小型电解槽中一氧化碳/二氧化碳还原的稳定且高性能气体扩散电极(GDE)方面发挥了关键作用;然而,在不降低性能的情况下将基于聚合物的气体扩散电极扩大到技术上更相关的电极尺寸仍然难以实现。这项工作报道了一种新的集流体概念,该概念能够将基于聚四氟乙烯的气体扩散电极从5平方厘米扩大到100平方厘米及更大尺寸。目前的方法基于一种多功能集流体概念,该概念能够实现薄催化剂涂层的多点正面接触,即使对于高电阻阴极也能减轻性能损失。我们改进的集流体设计同时在单极板配置中融入了流场功能,保持较小的电解液间隙以提高性能。在单间隙碱性阴离子交换膜和酸性阳离子交换膜系统中对100平方厘米的阴极进行了实验。我们的设计代表了大型一氧化碳电解槽开发中的重要一步。

https://cdn.ncbi.nlm.nih.gov/pmc/blobs/cf93/11019647/2cff1b079dfe/nz4c00114_0001.jpg

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