One significant factor in the degradation of pipelines used for oil and gas production is internal pitting corrosion. The penetration of the pipe wall by pits is a process that consists of three stages: formation of a passive layer on the steel surface; initiation of pits at localized regions on the steel surface where film breakdown occurs; and pit propagation and eventual penetration of the pipe wall. Electrochemical reactions are involved in all three stages. As a result, each stage of pitting corrosion can be modelled based on electrochemical principles. This paper reviews the merits and demerits of 35 electrochemical-science models.

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