“…As a consequence, the study of the electrochemical reduction of CO 2 to formate has attracted renewed and growing interest over the last years. Some studies have used fixed-bed reactors (Köleli et al, 2003;Köleli and Balun, 2004;Kwon and Lee, 2010) or divided H-type cells (Chen and Kanan, 2012;Kaneco et al, 1998Kaneco et al, , 1999Li et al, 2012). Nevertheless, several works in the literature have been focussed on parallel-plate or filter-press flow-by type cells (Agarwal et al, 2011;Akahori et al, 2004;Alvarez-Guerra et al, 2012;Innocent et al, 2009;Li and Oloman, 2005, 2007Machunda et al, 2010Machunda et al, , 2011Narayanan et al, 2011;Subramanian et al, 2007;, under different working conditions and cathodes of very different nature, such as indium-impregnated lead wire (Akahori et al, 2004), lead-plated stainless steel woven mesh (Subramanian et al, 2007), tinned-copper mesh Oloman, 2005, 2006), tin particles (shots and granules) (Li and Oloman, 2007), lead plates (Alvarez-Guerra et al, 2012;Innocent et al, 2009), or metal catalysts (such as indium (Narayanan et al, 2011), lead (Machunda et al, 2010) or tin (Agarwal et al, 2011;Machunda et al, 2011;) electrodeposited on different substrates.…”