Controlling the C<sub>1</sub>/C<sub>2+</sub> product selectivity of electrochemical CO<sub>2</sub> reduction upon tuning bimetallic CuIn electrocatalyst composition and operating conditions — Lin Gu (2023) | RDL Network
Controlling the C<sub>1</sub>/C<sub>2+</sub> product selectivity of electrochemical CO<sub>2</sub> reduction upon tuning bimetallic CuIn electrocatalyst composition and operating conditions
Electrochemical carbon dioxide (CO<sub>2</sub>) reduction (eCO<sub>2</sub>R) over Cu-based bimetallic catalysts is a promising technique for converting CO<sub>2</sub> into value-added multi-carbon products, such as fuels, chemicals, and materials. For improving the process efficiency, electrocatalyst development for the eCO<sub>2</sub>R must be integrated with tuning of operating conditions. For example, CuIn-based materials typically lead to preferential C<sub>1</sub> product selectivity, which delivers the desired C<sub>2+</sub> products upon varying the In/Cu ratio and operating conditions (<i>i.e.</i>, in 0.1 M KHCO<sub>3</sub> electrolytes using an H-type cell with a cation exchange membrane <i>vs.</i> in 1 M KOH electrolytes using a flow cell with an anion exchange membrane). At lower Cu-loading (<i>i.e.</i>, InCu<sub>5</sub>O<sub><i>x</i></sub> material), the maximum faradaic efficiency of HCOOH (FE<sub>HCOOH</sub>) of 70% was achieved at -1 V <i>versus</i> the reversible hydrogen electrode (<i>vs.</i> RHE) in an H-type cell. However, upon increasing the Cu loading, the preferential product selectivity could be altered: the InCu<sub>73</sub>O<sub><i>x</i></sub> material led to a high CO selectivity (maximum FE of 51%) in the H-type cell at -0.8 V <i>vs.</i> RHE and delivered a current density of 100 mA cm<sup>-2</sup> with a FE<sub>C2+</sub> of up to 37% at -0.8 V <i>vs.</i> RHE in the flow cell configuration. Various characterization tools were also employed to probe the catalytic materials to rationalize the electrocatalytic performance.
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