In crevices where the internal iron is not short-circuited to external metal, the corrosion rate is determined by the limiting cathodic current for oxygen reduction. This limiting current, and accordingly the corrosion rate, is independent of pH and C1-concentration but is suppressed to a constant value when the height of the crevice is less than the thickness of the oxygen diffusion layer. When iron in the crevice is short-circuited to external, open platinum, the initial crevice corrosion rate is independent of crevice height but increases with increasing C1-concentration and area of external electrode. At constant CI-concentration, the crevice corrosion rate of internal iron short-circuited to o~en external iron decreases with increasing chromate ion concentration. At a constant chromate ion concentration which does not give protection, the crevice corrosion rate is greater the greater the chloride ion concentration for short times, but at longer times the rates are essentially independent of bulk chloride concentration.Rosenfeld and Marshakov (1) have shown that crevice corrosion usually proceeds in two main stages: (i) initiation by differential aeration and (ii) propagation by crevice acidification. Initially, the sheltered metal in contact with a restricted oxygen supply becomes anodic relative to the open metal to which it is connected. At longer times, the presence of the crevice plays a different role, that of causing corrosion products to accumulate within the crevice so as to change the local solution composition and pH.Reports that not only crevices (1, 2) but also stresscorrosion cracks (3, 4) and pits (5, 6) acidify locally has led to the view that all three forms of localized corrosion share the unifying feature of being "occluded corrosion cells" (7) having restricted exchange with bulk electrolyte and thus common solution chemistries. Thus, most recent studies have utilized the thermodynamic, rather than kinetic, approach, with emphasis on factors such as resultant crevice solution chemistry, pH, and electrode potential (8-11). Little recent work has been done on the polarization kinetics of metals under crevices. One exception has been the correlation between the shape of cyclic anodic polarization curves for various engineering alloys in 3 89 % NaC1 with their longer range performances in natural seawater (12). Polarization curves have been reported in some well-defined but synthetic, generalized "occluded corrosion cells" sans crevices, in which the "internal" metal was activated by anodic polarization (13) or by deaeration (14). Other investigators have reported current-time (15) and potential-time (10, 16), but not current-potential relationships.The purpose of this study was to take up the systematic approach of Rosenfeld and Marshakov (1) in order to investigate in an organized manner kinetic aspects of a fairly simple crevice system. Iron was chosen, partly because of the attention given this metal in a wide variety of open systems. The effect of vari-* Electrochemical Society Active Mem...