电解质
阳极
图层(电子)
化学工程
膜
多孔性
材料科学
聚合物
催化作用
化学
纳米技术
电极
复合材料
有机化学
工程类
物理化学
生物化学
作者
Pablo A. García‐Salaberri,Hung-Ming Chang,Jack Todd Lang,Nausir Mahmoud Firas,Hasan Shahzad,Yu Morimoto,Iryna V. Zenyuk
标识
DOI:10.1016/j.cej.2025.160722
摘要
Reducing the dependency of proton exchange membrane water electrolyzers (PEMWE) on precious metals, such as iridium (Ir), is necessary to develop a widespread green hydrogen system. This challenge requires a careful design of the interface between the anode porous transport layer (PTL) and the catalyst layer (CL). A comprehensive numerical analysis of relevant parameters that govern the behavior of the anode PTL/CL interface is presented. Calculations are also combined with an experimental characterization of the thickness and electrical conductivity of an unsupported CL as a function of Ir loading. The results show that the in-plane electrical resistance at the anode PTL/CL interface plays a critical role in cell performance. Reaching an acceptable electrical resistance at low Ir loading ( L Ir ≃ 0 . 1 mg Ir , cm − 2 ) can be accomplished through the incorporation of a micrometer-sized microporous layer (MPL) onto the PTL or the preparation of bimodal CLs with a secondary conductive phase. Further reduction of the Ir loading to the ultra-low regime ( L Ir ≲ 0 . 1 mg Ir , cm − 2 ) may require the use of nanometer-sized MPLs with unsupported CLs or micrometer-sized MPLs with bimodal CLs. Furthermore, the decline of the volume reactive area at ultra-low Ir loading needs a maximization of the exchange current density and the specific electrochemical surface area, and a decrease of the catalyst oxygen coverage factor in the anode CL. • A 2D parametric analysis of key factors of the anode PTL/CL interface is presented • In-plane CL electrical resistance at PTL interface plays a critical role on performance. • Low Ir loading ( 0 . 1 mg Ir , cm − 2 ) can be achieved with micrometer-sized MPL or bimodal CL. • Ultra-low Ir loading ( ≲ 0 . 1 mg Ir , cm − 2 ) can be reached with fine MPLs and bimodal CL. • Optimization of volumetric exchange current density and gas saturation is needed.
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