Concurrent solar generation of hydrogen and CO through photoelectrochemical (PEC) water and CO 2 electrolysis, and the subsequent use of the product gas mixture in conventional Fischer-Tropsch processes, has the potential to provide a flexible pathway for direct solar generation of a variety of liquid fuels. In order for this approach to be practical, PEC devices must be designed to continuously and selectively provide a well-defined ratio of hydrogen to CO, independent of operating conditions. We develop a computational PEC device model providing insight into the dynamics and design requirements of such a device. We investigate a variety of combinations of catalysts (Ag, Cu, Ni, Pt, Co) and photoabsorbers (Si and Ga-based) under steady and transient solar irradiation conditions. Typical H 2 /CO ratios of 0.1 were observed for Ag-based electrodes, and ratios of 5 when using Cu-based electrodes. Variation in catalyst and photoabsorber properties provided guidance for the development of catalysts allowing for a H 2 /CO product ratio close to 2. Device design variations and the addition of Ni as a second cathode-side catalyst improved the generation of hydrogen, allowing H 2 /CO ratios to reach between 1.7 and 2.15. Transient simulations showed that product ratios vary significantly over the day and year, implying the use of storage or controlling measures or the addition of a water gas shift reactor. Our model provides insights and practical considerations for the design and implementation of a PEC device for the concurrent production of hydrogen and CO. Solar liquid fuel production can potentially be achieved by the reduction of water and CO 2 through two non-biological pathways: [1][2][3][4] i) solar thermochemical (STC) approaches, and ii) photoelectrochemical (PEC) approaches. In both cases, water and CO 2 is split into hydrogen and CO (a mixture called synthesis gas) and, for PEC approaches only, other lower order hydrocarbon products. Synthesis gas can subsequently be used in a Fischer-Tropsch process to produce liquid fuels such as gasoline and diesel. In STC approaches, redox couples are used and alternatingly reduced then oxidized at temperatures above 1000 K while splitting water and CO 2 . Synthesis gas is very selectively produced at a tailorable hydrogen to CO ratio.
5In PEC approaches, water electrolysis has been achieved, 6 and the reduction of CO 2 has been demonstrated, 7-10 but with challenges in respect to product selectivity and efficiency. While the PEC production of CO requires the involvement of two electrons only, methanol or higher order hydrocarbon products require the involvement of six, eight, or even twelve electrons (Eqs. 5 and 6), presenting significant challenges for the development of efficient and selective catalysts. Assuming that STC and PEC approaches can be complementary solar fuel processing pathways, synthesis gas appears to be the obvious fuel choice, as it can be produced by both pathways (comparatively easy in the case of PEC compared to other products) and would subseque...