Abstract
Electrocatalytic CO(2) reduction is a promising approach to mitigate rising atmospheric CO(2) levels while converting CO(2) into valuable products such as CH(4). Conversion into other useful substances further expands its potential applications. However, the efficiency of the CO(2) reduction reaction (CO(2)RR) is strongly influenced by device geometry and CO(2) mass transfer in the electrolyte. In this work, we present and evaluate microchannel electrocatalytic devices consisting of a porous Cu cathode and a Pt anode, fabricated via metal-assisted chemical etching (MACE). The porous surfaces generated through MACE enhanced reaction activity. To study the impact of the distance between electrodes, several devices with different channel heights were fabricated and tested. The device with the highest CH(4) selectivity had a narrow inter-electrode gap of 50 μm and achieved a Faradaic efficiency of 56 ± 11% at an applied potential of -5 V versus an Ag/AgCl reference electrode. This efficiency was considerably higher than that of the device with larger inter-electrode gaps (300 and 480 μm). This reduced efficiency in the larger channel was attributed to limited CO(2) availability at the cathode surface. Bubble visualization experiments further demonstrated that the electrolyte flow rate had a strong impact on supplied CO(2) bubble morphology and mass transfer. At a flow rate of 0.75 mL/min, smaller CO(2) bubbles were formed, increasing the gas-liquid interfacial area and thereby enhancing CO(2) dissolution into the electrolyte. These results underline the critical role of electrode gap design and bubble dynamics in optimizing microchannel electrocatalytic devices for efficient CO(2)RR.