Computational modeling of cathodic limitations on localized corrosion of wetted SS 316L at room temperature

The ability of a SS 316L surface wetted with a thin electrolyte layer to serve as an effective cathode for an active localized corrosion site was studied computationally. The dependence of the total net cathodic current, I net, supplied at the repassivation potential E rp (of the anodic crevice) on relevant physical parameters including water layer thickness (WL), chloride concentration ([Cl−]) and length of cathode (Lc) were investigated using a three-level, full factorial design. The effects of kinetic parameters including the exchange current density (i o,c) and Tafel slope (β c) of oxygen reduction, the anodic passive current density (i p) (on the cathodic surface), and E rp were studied as well using three-level full factorial designs of [Cl−] and Lc with a fixed WL of 25μm. The study found that all the three parameters WL, [Cl−] and Lc as well as the interactions of Lc×WL and Lc×[Cl−] had significant impact on I net. A five-factor regression equation was obtained which fits the computation results reasonably well, but demonstrated that interactions are more complicated than can be explained with a simple linear model. Significant effects on I net were found upon varying either i o,c, β c, or E rp, whereas i p in the studied range was found to have little impact. It was observed that I net asymptotically approached maximum values (I max) when Lc increased to critical minimum values. I max can be used to determine the stability of coupled localized corrosion and the critical Lc provides important information for experimental design and corrosion protection.