463736 Effects of Temperature and Gas-Liquid Mass Transfer on the Operation of Small Electrochemical Cells for the Quantitative Evaluation of CO2 Reduction Electrocatalysts

Monday, November 14, 2016: 8:40 AM
Franciscan C (Hilton San Francisco Union Square)
Peter Lobaccaro1,2,3, Meenesh Singh1,2,3, Ezra L. Clark1,2,3, Youngkook Kwon1,2, Alexis T. Bell1,2,3 and Joel W. Ager III1,4,5, (1)Joint Center for Artificial Photosynthesis, Lawrence Berkeley National Laboratory, CA, (2)Chemical Sciences Division, Lawrence Berkeley National Laboratory, CA, (3)Department of Chemical and Biomolecular Engineering, University of California, Berkeley, Berkeley, CA, (4)Materials Sciences Division, Lawrence Berkeley National Laboratory, CA, (5)Department of Materials Science and Engineering, University of California, Berkeley, Berkeley, CA

In the last few years, there has been increased interest in electrochemical CO2 reduction (CO2R). Many experimental studies employ a membrane separated, electrochemical cell with a mini H-cell geometry to characterize CO2R catalysts in aqueous solution. Gas products are measured periodically by sampling the effluent CO2, which is continuously sparging the cell, while liquid products are measured by batch sampling of the electrolyte. The sensitivity of this approach for the detection of liquid products can be increased by increasing the catalyst surface area to electrolyte volume ratio (S/V) of the cell. However, we show that operating cells with high S/V at high current densities can have subtle consequences, especially for the cell temperature and electrolyte CO2 concentration.

Both effects were evaluated quantitatively in high S/V cells using Cu electrodes and a bicarbonate buffer electrolyte. Electrolyte temperature is a function of the current and total voltage passed through the cell as well as the cell geometry. Even at very high current density, 20 mA cm-2, the measured temperature rise was less than 4 °C and a decrease of <10% in the dissolved CO2 concentration is predicted. In contrast, limits on the CO2 gas-liquid mass transfer into the cells produce much larger effects. By using the pH in the cell to measure the dissolved CO2 concentration, significant undersaturation of CO2 is observed, even at more modest current densities of 10 mA cm-2.

Importantly, undersaturation of CO2 produces large changes in the faradaic efficiency product distribution observed on Cu electrodes, with H2 production becoming increasingly favored as the CO2 undersaturation worsens. We show that the size of the CO2 bubbles being introduced into the cell is critical for maintaining the equilibrium CO2 concentration in the electrolyte, and we have designed a high S/V cell that is able to maintain the equilibrium CO2 concentration at current densities up to 15 mA cm-2.

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