The kinetics of oxygen reduction from electrolyte emulsions containing oxyg
en carriers was studied with respect: to fuel cell applications. Electroche
mical experiments including stationary and nonstationary measurements under
defined hydrodynamic conditions at a rotating platinum disk electrode reve
aled that diffusion-controlled limiting currents can be increased significa
ntly at high oxygen concentrations. Additionally, the limiting currents sho
w a strong correlation with the composition and the structure of the emulsi
ons. In particular, the average droplet size of the organic phase and its d
istribution depends on the nature of the emulsifying agents used for stabil
isation. The complex hydrodynamic behaviour of two-phase electrolyte emulsi
ons and the influence of different surfactants seem to outweigh the; effect
of the total oxygen concentration on the transport kinetics of oxygen. (C)
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