Pedersen Angus, Kumar Kavita, Ku Yu-Ping, Martin Vincent, Dubau Laetitia, Santos Keyla Teixeira, Barrio Jesús, Saveleva Viktoriia A, Glatzel Pieter, Paidi Vinod K, Li Xiaoyan, Hutzler Andreas, Titirici Maria-Magdalena, Bonnefont Antoine, Cherevko Serhiy, Stephens Ifan E L, Maillard Frédéric
Imperial College London, Department of Materials, Royal School of Mines London SW7 2AZ UK
Imperial College London, Department of Chemical Engineering London SW7 2AZ UK.
Energy Environ Sci. 2024 Jul 30;17(17):6323-6337. doi: 10.1039/d4ee01995d. eCollection 2024 Aug 27.
Atomic Fe in N-doped C (Fe-N-C) catalysts provide the most promising non-precious metal O reduction activity at the cathodes of proton exchange membrane fuel cells. However, one of the biggest remaining challenges to address towards their implementation in fuel cells is their limited durability. Fe demetallation has been suggested as the primary initial degradation mechanism. However, the fate of Fe under different operating conditions varies. Here, we monitor Fe dissolution of a highly porous and >50% FeN electrochemical utilization Fe-N-C catalyst in 0.1 M HClO, under O and Ar at different temperatures, in both flow cell and gas diffusion electrode (GDE) half-cell coupled to inductively coupled plasma mass spectrometry (ICP-MS). By combining these results with - and analyses, we demonstrate that in the absence of oxygen, Fe cations diffuse away within the liquid phase. Conversely, at -15 mA cm and more negative O reduction currents, the Fe cations reprecipitate as Fe-oxides. We support our conclusions with a microkinetic model, revealing that the local pH in the catalyst layer predominantly accounts for the observed trend. Even at a moderate O reduction current density of -15 mA cm at 25 °C, a significant H consumption and therefore pH increase (pH = 8-9) within the bulk Fe-N-C layer facilitate precipitation of Fe cations. This work provides a unified view on the Fe dissolution degradation mechanism for a model Fe-N-C in both high-throughput flow cell and practical operating GDE conditions, underscoring the crucial role of local pH in regulating the stability of the active sites.
氮掺杂碳(Fe-N-C)催化剂中的原子铁在质子交换膜燃料电池阴极提供了最具前景的非贵金属氧还原活性。然而,在燃料电池中实现其应用仍面临的最大挑战之一是其耐久性有限。铁脱金属被认为是主要的初始降解机制。然而,不同操作条件下铁的命运各不相同。在此,我们在流动池和与电感耦合等离子体质谱(ICP-MS)联用的气体扩散电极(GDE)半电池中,监测了一种高度多孔且FeN含量>50%的电化学利用型Fe-N-C催化剂在0.1 M高氯酸中、不同温度下、氧气和氩气氛围中的铁溶解情况。通过将这些结果与-和分析相结合,我们证明在无氧条件下,铁阳离子在液相中扩散离开。相反,在-15 mA cm且氧还原电流更负时,铁阳离子会重新沉淀为铁氧化物。我们用微观动力学模型支持我们的结论,揭示催化剂层中的局部pH主要解释了观察到的趋势。即使在25°C下-15 mA cm的中等氧还原电流密度下,大量Fe-N-C层内显著的氢消耗以及因此导致的pH升高(pH = 8 - 9)也促进了铁阳离子的沉淀。这项工作在高通量流动池和实际操作的GDE条件下,对模型Fe-N-C的铁溶解降解机制提供了统一的观点,强调了局部pH在调节活性位点稳定性方面的关键作用。