solubility of CO 2 in aqueous electrolyte solution (≈30 × 10 −3 m), which leads to diffusion-limited current densities. Device engineering has addressed this issue through the development of flow cell configurations that overcome mass transport limitations of conventional H-cells, thus improving attainable current densities. [4][5][6][7] Another complication resides in the kinetic requirement for multiple electron and proton transfers, which results in high energy barriers for certain products, requiring efficient catalysts for high current densities. The similarity in thermodynamic potentials for different CO 2 R products (Table 1) means that product selectivity is a problem. Additionally, proton reduction is kinetically fast in aqueous conditions leading to competitive hydrogen generation. CO 2 R electrocatalysts have been developed to address this broad range of products that can be generated and the concomitant lack of selectivity.Although molecular electrocatalysts have demonstrated high selectivity for CO 2 R to C 1 products, [8] they currently suffer from short-term stability. [9] The most effective catalysts are those based on metallic or semiconducting materialsheterogeneous catalysts. Metallic catalysts in particular have shown high selectivity for: CO using Ag, Zn, and Au; formate using Sn, In, and Pb; and a range of multi-carbon products using Cu catalysts in EC systems. [10][11][12][13][14][15] Knowledge of how nanoscale properties and morphological effects influence specificity, has enabled systems to achieve high selectivity with competitive production rates. [13] For example, identifying key morphological attributes and alterations under operating conditions, [16][17][18][19][20][21][22] observing trends in size and facet-dependent selectivity, [23][24][25][26][27] and evaluating the impact of structuration on the local chemical environment, [28][29][30] all contribute to increased understanding of structure-activity relationships in CO 2 R. The type of catalyst employed therefore plays a large role in overall performance.EC CO 2 R devices can theoretically be coupled with any renewable electricity source, however, the direct integration of sunlight-driven processes is a desirable route to product formation. [31,32] An integrated approach avoids the need for grid access in remote locations, enabling direct on-site utilization, and reduces energy losses from current conversion. The additional costs in combining grid electricity with conventional electrolyzers has driven research toward the incorporation of increasingly affordable PV components. An additional benefit is the dual functionality of these devices that allows them to retain their The simultaneous mitigation of CO 2 emissions and direct generation of value-added chemicals has motivated research in solar-driven electrochemical CO 2 reduction. Here, devices incorporating heterogeneous catalysts that operate under bias-free aqueous conditions are categorized and compared, encompassing photoelectrochemical (PEC), photovoltaic-electrochemical ...