“…They permit current densities of almost two orders of magnitude higher at the same overpotential compared with planar electrodes (Weng et al., 2018) by introducing gaseous CO 2 into the electrolyte at the active site through a gas diffusion layer inside the GDE. Alternatively, the mass transport of CO 2 can be improved by increasing its solubility by adjusting the pressure (in MeOH, 333 mA·cm 2 , FE (CO) > 85%, 40 atm at Cu wire, Saeki et al., 1995a, Saeki et al., 1995b, up to 68 atm, Li and Prentice, 1997) and the temperature (down to −30°C, in MeOH, Naitoh et al., 1993, Mizuno et al., 1995, Kaneco et al., 1998a, Kaneco et al., 1998b, Kaneco et al., 1998c, Oh et al., 2014). Owing to requirements regarding the current density for an industrial application, the continuous supply of CO 2 applying GDEs is preferred over submerged electrodes.…”