The two-electron reduction of
O2
at pH 3 (1 M
Na2SO4
acidified by glacial acetic acid) and 9.6 (mixture of 0.5 M
Na2CO3
and 0.5 M
NaHCO3false)
was investigated in flow-by electrochemical reactors with three-dimensional cathodes, consisting of graphite felt (GF) or reticulated vitreous carbon (RVC). The cathode was operated with co-current upward gas/liquid flow and
O2
pressures in the range of 200-700 kPa. A factorial design with four variables at two levels was employed to investigate the effects of superficial current density, liquid load,
O2
pressure, and cationic surfactant concentration [i.e., trioctylmethylammonium chloride (Aliquat® 336, A336)] on
H2O2
concentration, current efficiency, and reactor voltage. Among the investigated variables A336 exerted the strongest positive main effect on both
H2O2
concentration and current efficiency. The beneficial effect of A336 was due to suppression of the
H2O2
loss by both electroreduction and surface-catalyzed decomposition. However, A336 increased the pressure gradient through GF by up to 100%. The surfactant effect on the pressure gradient was estimated using the Herbolzheimer-Park model for the influence of surfactant on the motion of gas bubbles in liquid-filled capillaries. An
O2
mass-transfer model in both GF and RVC was developed and correlated with the experimental results. © 2005 The Electrochemical Society. All rights reserved.