Bashir Shahid M, Gyenge Előd L
Department of Chemical and Biological Engineering, The University of British Columbia, 2360 East Mall, Vancouver V6T 1Z3, Canada.
Clean Energy Research Centre, the University of British Columbia, 2360 East Mall, Vancouver V6T 1Z3, Canada.
ACS Omega. 2024 Dec 20;10(1):1493-1509. doi: 10.1021/acsomega.4c09202. eCollection 2025 Jan 14.
The electrochemical carbon dioxide reduction reaction (CORR) using renewable electricity sources could provide a sustainable solution for generating valuable chemicals, such as formate salt or formic acid. However, an efficient, stable, and scalable electrode generating formate at industrially viable current densities (>100 mA cm) is yet to be developed. Sn or In-based catalysts in gas diffusion electrodes (GDE) can efficiently produce formate. However, their long-term durability is limited owing to catalyst deactivation, carbonate deposition, and electrode flooding. Herein, a systematic study of 20 cm GDEs with SnO and InO catalyst layers is presented in conjunction with various electrode operation strategies (i.e., flow-by vs flow through, dry vs humidified CO, continuous vs reverse polarity pulse electrolysis). It is demonstrated that the incorporation of CeO nanoparticles as a promoter in either SnO or InO catalyst layers coupled with intermittent reverse polarity pulse operation dramatically improves the GDE stability during 12 h of tests at 500 mA cm with over 90% formate Faradaic efficiency. Due to its strong oxidizing capacity, CeO helps Sn and In regain their valence state of + IV and + III, respectively, which are in situ reduced during CORR, as shown by the surface characterization of the electrodes. The effect of the initial particle size of SnO and reverse polarity pulse on the catalytic activity, durability, and carbonate salt precipitation in the GDE have also been addressed. Regarding two-phase flow dynamics, the quasi-convective gas flow through the GDE was more beneficial than the gas flow-by mode for enabling stable operation at high current densities (up to 500 mA cm). The synergistic approach of catalyst layer engineering coupled with diverse GDE operation modes explored here is promising for the scale-up of efficient and durable reactors for the CORR to formate and CO redox flow batteries.
利用可再生电源的电化学二氧化碳还原反应(CORR)可为生成有价值的化学品(如甲酸盐或甲酸)提供可持续的解决方案。然而,尚未开发出一种能在工业可行电流密度(>100 mA/cm²)下高效、稳定且可扩展地生成甲酸盐的电极。气体扩散电极(GDE)中的Sn基或In基催化剂可高效生产甲酸盐。然而,由于催化剂失活、碳酸盐沉积和电极水淹,它们的长期耐久性有限。在此,本文对具有SnO和InO催化剂层的20 cm² GDE进行了系统研究,并结合了各种电极操作策略(即旁流与流通、干燥与加湿CO、连续与反向极性脉冲电解)。结果表明,在SnO或InO催化剂层中加入CeO₂纳米颗粒作为促进剂,并采用间歇反向极性脉冲操作,可在500 mA/cm²下进行12小时测试期间显著提高GDE的稳定性,甲酸盐法拉第效率超过90%。由于其强氧化能力,CeO₂有助于Sn和In分别恢复其+IV和+III价态,这两种价态在CORR过程中会原位还原,电极的表面表征证明了这一点。还探讨了SnO的初始粒径和反向极性脉冲对GDE中催化活性、耐久性和碳酸盐沉淀的影响。关于两相流动力学,对于在高电流密度(高达500 mA/cm²)下实现稳定运行,通过GDE的准对流气流比旁流模式更有利。本文探索的催化剂层工程与多种GDE操作模式相结合的协同方法,对于扩大用于CORR生成甲酸盐和CO氧化还原液流电池的高效耐用反应器规模很有前景。