tivity. To achieve economically compelling CO 2 RR, technoeconomic analysis (TEA) highlights the pressing need for industrially relevant productivity (>200 mA cm −2 ) and energy efficiency (>50%) for CO 2 to ethylene (C 2 H 4 ) conversion. [4,5] This emphasizes the importance of high selectivity, high energy efficiency, and high product yield. [4][5][6][7][8][9] There exists an urgent need to find electrocatalysts and reactors enabling to produce a specific chemical efficiently at a low cost.Understanding the CO 2 RR electrolyzer is crucial for this purpose. In an H-cell, CO 2 is bubbled into the electrolyte and the low CO 2 solubility limits the production rates of C 2 H 4 to several tens of mA cm −2 in CO 2 RR. [10] In the flow cell, where catholyte, anolyte, and CO 2 flow independently in separate chambers, CO 2 gas is supplied from the backside of a porous gas diffusion electrode (GDE), overcoming the mass transport limitation and achieving C 2 H 4 productivities of >100 mA cm −2 . [11] Membrane electrode assembly (MEA) electrolyzers are newly emerging systems, where cathode:membrane:anode are stacked together to minimize ohmic loss. [12,13] Electrocatalysts are deployed typically on hydrophobic and porous substrates to form GDEs. The design of GDEs is important to achieve efficient transport of CO 2 to the local reaction environment. [14,15] Three mass transport regions, which include the electrolyte phase reaction (bulk reaction), reaction
High-rate conversion of carbon dioxide (CO2 ) to ethylene (C 2 H 4 ) in the CO 2 reduction reaction (CO 2 RR) requires fine control over the phase boundary of the gas diffusion electrode (GDE) to overcome the limit of CO 2 solubility in aqueous electrolytes. Here, a metal-organic framework (MOF)-functionalized GDE design is presented, based on a catalysts:MOFs:hydrophobic substrate materials layered architecture, that leads to high-rate and selective C 2 H 4 production in flow cells and membrane electrode assembly (MEA) electrolyzers. It is found that using electroanalysis and operando X-ray absorption spectroscopy (XAS), MOF-induced organic layers in GDEs augment the local CO 2 concentration near the active sites of the Cu catalysts. MOFs with different CO 2 adsorption abilities are used, and the stacking ordering of MOFs in the GDE is varied. While sputtering Cu on poly(tetrafluoroethylene) (PTFE) (Cu/PTFE) exhibits 43% C 2 H 4 Faradaic efficiency (FE) at a current density of 200 mA cm −2 in a flow cell, 49% C 2 H 4 FE at 1 A cm −2 is achieved on MOFaugmented GDEs in CO 2 RR. MOF-augmented GDEs are further evaluated in an MEA electrolyzer, achieving a C 2 H 4 partial current density of 220 mA cm −2 for CO 2 RR and 121 mA cm −2 for the carbon monoxide reduction reaction (CORR), representing 2.7-fold and 15-fold improvement in C 2 H 4 production rate, compared to those obtained on bare Cu/PTFE.