Both pH and pCl sensing plates were fabricated, and the H + and Cl − distributions in the crevice solution for 18Cr-10Ni-5.5Mn stainless steel were visualized at 0.3 V (vs. Ag/AgCl, 3.33 M KCl) in 0.01 M NaCl (pH 3.0, adjusted with H 2 SO 4 ) at 298 K. While the pH inside the crevice gradually decreased with time, no accumulation of Cl − ions occurred. The SO 4 2− ions that were added to adjust the pH probably accumulated to maintain electroneutrality. When the pH reached 1.7, a metastable pit was generated inside the crevice, providing a sharp decrease in pH to 0.4 and an increase in Cl − concentration to above 4 M. After that, the corroded area grew steadily with time, and the pH and the Cl − concentration remained constant at pH 0.4 and above 4 M Cl − . Acidification from pH 1.7 to 0.4 was induced by the hydrolysis of the dissolving metal ions from the pit and resulted in the depassivation of the surrounding steel matrix. The metastable pitting also caused the Cl − accumulation inside the crevice by electromigration. The crevice corrosion was found to be initiated when the pH and Cl − concentration inside the crevice reached the conditions for metastable pit formation.Crevice corrosion of stainless steels is a problem in chemical industries and marine structures, and it has been the subject of many investigations largely because crevice corrosion sometimes happens in steels that generally exhibit excellent corrosion resistance. 1 The prevention of crevice corrosion requires an in-depth understanding of its initiation process. In crevice corrosion, geometric restrictions cause deoxygenation inside the crevice, resulting in the separation of anodic and cathodic sites. On the anodic site (inside the crevice), metal ions accumulate by passive dissolution, which cause acidification of the crevice solution by hydrolysis. 2 The electromigration and accumulation of Cl − ions also occur inside the crevice. In the incubation time to crevice corrosion, the pH and the Cl − concentration of the crevice solution gradually reach the critical values for depassivation, and then the transition from passive to active dissolution occurs. This is the classical initiation mechanism (passive dissolution model) of crevice corrosion. 2 However, this mechanism appears not to be consistent with experimental observations. 2,3 The IR drop and metastable pitting models have been proposed for the initiation of crevice corrosion.In the IR drop model, 4-13 crevice corrosion starts when the potential difference between the outside and the inside of the crevice becomes large enough to cause the transition from passive to active inside the crevice. The IR (ohmic potential) drop arises from the anodic current (I) from the inside to the outside of the crevice and the electric resistance (R) of the crevice solution and corrosion products. In this model, acidification and Cl − accumulation bring about an active loop in the polarization curve in the crevice solutions, and both factors also accelerate the active dissolution rate. 13 Metastable (micro)...