Crevice Corrosion and Pitting Corrosion Most common forms
- Slides: 43
Crevice Corrosion and Pitting Corrosion
Most common forms of localized corrosion are pitting – film breakdown often by halides and oxidizing solutions, crevice corrosion - within small gaps and openings and stress corrosion cracking
Crevice corrosion schematics
Electrode potential for crevice is more negative than the open face iron
0. 5 mm is the diffusion layer thickness for oxygen in water, smaller gaps mean oxygen transport is impeded Crevice heights
Evans diagram for the crevice corrosion of iron Crevice corrosion propagation by sustained different composition in crevice
Confined anodic reaction produces concentrated cations and cations, which then attract Cl- to maintain charge neutrality and make a very corrosive local environment
Area effects Area outside crevice drives/accelerates crevice corrosion How?
Distance from crevice
Design considerations to reduce crevice corrosion
• • Protecting against crevice corrosion Corrosion inhibitors chromates, dichromates, molybdates, phosphates, etc. Cathodic protection Design to eliminate crevices Select resistant materials
halides promote pitting and shift peak effect of changing anions in solution
Overwhelming the Cl with SO 42 - reduces its effect
Pit initiation
Actual measured values in a real pit
Increasing H+ and Cl- increases the corrosion current (conditions found in pits)
2) Dissolved Mo species makes molybdates which acts as a corrosion inhibitor 3) Mo species interact with cation vacancies to slow transport 4) Molydate species form a layer which inhibit transport of Cl- ions 5)Mo slows dissolution at pit base
Why? ? ?
Demonstration of Cl- increased in film when pitting occurs
Illustration showing similarities between pitting corrosion, crevice corrosion and stress corrosion cracking There is always a transport obstacle for the cathodic and anodic reactions.
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