Unveiling the effects of dimensionality of tin oxide-derived catalysts on CO2 reduction by using gas-diffusion electrodes. Issue 2 (23rd December 2020)

• Record Type: Journal Article
• Authors: Li, Mengran; Idros, Mohamed Nazmi; Wu, Yuming; Garg, Sahil; Gao, Shuai; Lin, Rijia; Rabiee, Hesamoddin; Li, Zhiheng; Ge, Lei; Rufford, Thomas Edward; Zhu, Zhonghua; Li, Liye; Wang, Geoff
• Is Part Of: Reaction chemistry & engineering. Volume 6:Issue 2(2021)
• Page Start: 345
• Page End: 352
• Publication Date: 2020-12-23
• Subjects: Reaction mechanisms (Chemistry) -- Periodicals; Chemical engineering -- Periodicals; Chemical engineering; Reaction mechanisms (Chemistry); Periodicals; 547.705
• DOI: 10.1039/d0re00396d
• Languages: English
• ISSNs: 2058-9883

Abstract

Abstract : Catalyst dimensionality is essential for the reactivity and selectivity of gas-diffusion electrodes for CO2 electrochemical reduction to produce formate. Abstract : We report the effects of catalyst dimensionality on electrochemical CO2 conversion to formate by comparing the performance of tin oxide-derived 3D nanoparticles and tin oxide-derived 2D nanosheets deposited on gas-diffusion electrodes. Our results indicated that an extensive interface between the catalyst and the electrode substrate could lower the surface tin oxidation states and the hydrophobicity of the catalyst layer during CO2 electrolysis at a current density over 100 mA cm −2 . This catalyst–substrate interfacial effect provides the nanosheets with a large interface area to become more selective for CO2 electrochemical reduction but with a higher overpotential requirement as compared to the 3D nanoparticle catalysts with limited interfacial area. Consequently, the electrode with nanosheets as the catalyst achieved a partial current density of formate at 116 mA cm −2 at a cathode potential of −1.03 V versus reversible hydrogen electrode, which is equivalent to a formate production rate of 36 μmol min −1 cm −2 . Our work here demonstrates the importance of the catalyst–substrate interface in determining the oxidation states and wettability at the catalyst surface and the ultimate performance of the gas-diffusion electrode. These findings also have potential to guide the design of a catalyst–substrate to advance other important electrochemical processes such as fuel cells and water splitting.