4.6 Article

Unveiling the effects of dimensionality of tin oxide-derived catalysts on CO2 reduction by using gas-diffusion electrodes

期刊

REACTION CHEMISTRY & ENGINEERING
卷 6, 期 2, 页码 345-352

出版社

ROYAL SOC CHEMISTRY
DOI: 10.1039/d0re00396d

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资金

  1. HBIS Group
  2. Australian Research Council (ARC) Linkage project [LP 160101729]
  3. University of Queensland
  4. ARC centre for LNG Futures [IC150100019]
  5. UQ Training Program (RTP)

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The study compared the performance of 3D nanoparticles and 2D nanosheets as catalysts for electrochemical CO2 conversion to formate, finding that a catalyst with extensive interface could enhance CO2 reduction selectivity but require higher overpotential. Therefore, the catalyst-substrate interface structure plays a crucial role in determining the performance of gas-diffusion electrodes in such processes.
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 mu mol 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.

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