Electrochemical Conversion of CO2 into Hydrocarbons at Industrial Current Densities on Shaped Copper-oxide Gas Diffusion Electrodes
Tim Möller a, Trung Ngo Thanh a, Zarko Jovanov a, Peter Strasser a
a The Electrochemical Energy, Catalysis, and Materials Science Laboratory, Department of Chemistry, Chemical Engineering Division, Technical University Berlin, Berlin, Germany
Materials for Sustainable Development Conference (MATSUS)
Proceedings of nanoGe Fall Meeting19 (NFM19)
#SolCat19. (Photo)electrocatalysis for sustainable carbon utilization: mechanisms, methods, and reactor development
Berlin, Germany, 2019 November 3rd - 8th
Organizer: Matthew Mayer
Oral, Tim Möller, presentation 242
DOI: https://doi.org/10.29363/nanoge.nfm.2019.242
Publication date: 18th July 2019

 

The electrochemical reduction of CO2 (CO2RR) is one promising technique to address global issues of energy storage and advance towards a circular economy. Over the recent years, scientific efforts have generated much fundamental insight into the parameters dictating this complex reaction but studies probing high production rates for design of applicable devices are still scarce.

 

Here, we are presenting a study based on cubic Cu2O particles for the electrochemical CO2RR in a flow electrolyzer at high current density of 50 to 700 mA cm-2. To trace changes of the material during CO2RR, we use electron microscopy and X-Ray spectroscopy for respective determination of morphological and phase alterations. In this, we can observe drastic changes of the catalyst caused by reduction of the oxide phase. To overcome mass transport limitations and achieve high production rates, gas diffusion electrodes (GDEs) were prepared by spray coating the cubic particles mixed with Nafion ionomer on porous carbon layers. We found the electrode preparation to strongly influence the CO2RR selectivity and have systematically studied the effect of changing particle loading and Nafion content. We used electrochemical techniques and electron microscopy to assess differences in active surface area of the electrodes and comment on the role of accessibility of the catalytic sites during the reaction. Furthermore, investigations of catholyte concentration suggest strong influences of the buffer capacity and local pH even at high currents, which have been previously believed to be only minor. Our study shows the possibility to transition from fundamental experiments to production rates of technological importance by the use of gas diffusion electrodes for the electrochemical CO2RR. Additionally, we demonstrate how system parameters influence the overall performance and give a guideline how to approach a functional electrolyzer for the CO2RR.

  

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