Journal of The Electrochemical Society · 2002 · 77 citations · 15 references
Natural SciencesMaterials EngineeringMaterials ScienceCorrosion ScienceElectrochemistrySurface ScienceCorrosion KineticsCorrosion MechanismsElectrochemical CorrosionElectrochemical KineticsElectrode KineticsElectrode-electrolyte InterfacesCorrosion Current DensityCorrosion ElectrochemistryElectrochemical Corrosion MechanismsElectrochemical Corrosion ProcessesElectrochemical MechanismsElectrochemical Reaction KineticsKinetic ControlOxygen Reduction Reaction
There are many important processes in corrosion for which the diffusion-limited current density of oxygen reduction, i L , plays a dominant role in terms of kinetic control. The conventionally accepted value of i L (for the four-electron reduction mechanism) which can be found in many corrosion textbooks is in the range of 50-100 μA cm -2 , but the origins of this range of values are a bit mysterious. Previous research in our group aimed at ascertaining i L (under stagnant conditions) on a planar Cu electrode and a Cu microelectrode array in a naturally aerated 0.1 M Na 2 SO 4 electrolyte found that i L was in the range of 20-30 μA cm -2 . In situ scanning tunneling microscopy was used to characterize the Cu surface at relevant potentials. Rotating disk electrode studies were used to measure i L in a naturally aerated 0.1 M Na 2 SO 4 electrolyte as a function of pH for both Pt and Cu electrodes. By comparing results for Pt and Cu we conclude that oxygen reduction occurs on a Cu surface via the four-electron mechanism. The oxygen diffusion-limited current density was found to be independent of pH (in the range 1.5-14). Finally, we conclude that our previous determination of i L in a stagnant electrolyte reflects an accurate range of values of the oxygen diffusion-limited current density.
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