Using a 3D Porous Flow-Through Electrode Geometry for High-Rate Electrochemical Reduction of CO2 to CO in Ionic Liquid
- Lawrence Livermore National Lab. (LLNL), Livermore, CA (United States)
Three-dimensional porous flow-through electrodes promise the realization of higher current densities in the electrochemical carbon dioxide reduction reaction (CO2RR) by overcoming mass-transport limitations associated with the diffusion of dissolved CO2 in the bulk electrolyte. Using an ionic-liquid-based electrolyte, [EMIM]BF4, offers the additional benefit of higher CO2 solubility compared to water-based electrolytes. Here, we quantitatively evaluated the effects of flow-driven reactant transport on electrode activity and selectivity for the electrochemical CO2RR in [EMIM]BF4. High-surface-area porous flow-through electrodes were fabricated by wet-chemical deposition of Ag nanoflowers on commercial macroporous Al foams. At the highest electrolyte flow-through rate of 100 mL min–1, we observed a 70-fold increase in partial CO current density, and a 7-fold increase in the Faradaic efficiency toward CO, from 10% without flow to 75% with flow. At the same time, the selectivity changed from oxalate as the main product without flow to CO in the electrolyte flow-through configuration. These results demonstrate that the flow-through approach provides a promising path forward to control selectivity and to overcome mass-transport limitations of the electrochemical CO2RR.
- Research Organization:
- Lawrence Livermore National Lab. (LLNL), Livermore, CA (United States)
- Sponsoring Organization:
- USDOE National Nuclear Security Administration (NNSA)
- Grant/Contract Number:
- AC52-07NA27344
- OSTI ID:
- 1630811
- Report Number(s):
- LLNL-JRNL-782157; 976694
- Journal Information:
- ACS Catalysis, Vol. 9, Issue 12; ISSN 2155-5435
- Publisher:
- American Chemical Society (ACS)Copyright Statement
- Country of Publication:
- United States
- Language:
- English
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