4.7 Article

Understanding CO2 electrochemical reduction kinetics of mixed-conducting cathodes by the electrical conductivity relaxation method

Journal

INTERNATIONAL JOURNAL OF HYDROGEN ENERGY
Volume 46, Issue 15, Pages 9646-9652

Publisher

PERGAMON-ELSEVIER SCIENCE LTD
DOI: 10.1016/j.ijhydene.2020.07.141

Keywords

CO2 reduction; Solid oxide electrolysis cell; Electrical conductivity relaxation; Electrocatalyst; Kinetics

Funding

  1. Guangdong Basic and Applied Basic Research Foundation [2019A1515110025, 2017A030313289]
  2. Research Grant for Scientific Platform and Project of Guangdong Provincial Education office [2019KTSCX151]
  3. Shenzhen Government's Plan of Science and Technology [JCYJ20180305125247308]
  4. National Natural Science Foundation of China [51402093, 21706162]
  5. China postdoctoral commission

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In this study, a new theoretical method based on the electrical conductivity relaxation technique was proposed to investigate the kinetics of CO2 reduction reaction on a typical electrode. Three kinetic parameters commonly used in electrochemical test experiments were derived, providing a new approach for studying the kinetic process of CO2 electrolysis and evaluating electrocatalyst activity of developed electrode materials.
Electrochemical reduction reaction is an important approach to utilize CO2 and convert it into valuable products. Exceptional reaction kinetics at a high temperature of solid oxide electrolysis cells (SOECs) attracts particular attention. In this work, we propose to investigate CO2-RR kinetics using a new theoretical method based on the electrical conductivity relaxation (ECR) technique on a typical mixed-conducting Sr2Fe1.5Mo0.5O6-delta (SFM) electrode. Three kinetic parameters that are commonly adopted in the typical electrochemical test experiments consisting of overpotential, current density and area-specific resistance (ASR) are derived. The overpotential resulted from the difference in the oxygen partial pressure is caused by the change of CO2 partial pressure, while current density from the surface reaction rate constant. Accordingly, area-specific resistance, as well as overpotential-current density relationship, can be derived. We believe that this work brings a new method to study the kinetic process of CO2 electrolysis and to evaluate the electrocatalyst activity of developed new electrode materials as well as to benefit the designing of novel electrode electrocatalysts for highly efficient solid oxide electrolysis cells. (C) 2020 Hydrogen Energy Publications LLC. Published by Elsevier Ltd. All rights reserved.

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