Effect of Field Operational Variables on Internal Pitting Corrosion of Oil and Gas Pipelines

Internal pitting corrosion, caused by carbon dioxide (CO2) and hydrogen sulfide (H^sub 2^S), is one of the predominant failure mechanisms of these pipelines.1-7 An integrated model to predict internal pitting corrosion of oil and gas pipelines has already been described.8 According to this model, th...

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Published inCorrosion (Houston, Tex.) Vol. 65; no. 11; pp. 741 - 747
Main Authors DEMOZ, A, PAPAVINASAM, S, OMOTOSO, O, MICHAELIAN, K, REVIE, R. W
Format Journal Article
LanguageEnglish
Published Houston, TX NACE International 01.11.2009
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Abstract Internal pitting corrosion, caused by carbon dioxide (CO2) and hydrogen sulfide (H^sub 2^S), is one of the predominant failure mechanisms of these pipelines.1-7 An integrated model to predict internal pitting corrosion of oil and gas pipelines has already been described.8 According to this model, the internal pitting corrosion of oil and gas pipelines occurs in four stages: -the low- or no-corrosion stage when the internal surface of the pipeline is covered by hydrocarbons, i.e., oil-wet conditions; -formation of surface layers on the steel surface due to corrosion reactions once the surface is covered with water, i.e., water-wet conditions; -initiation of pits at localized regions on the steel surface when surface-layer breakdown occurs; and -pit propagation and eventual penetration of the pipe wall. In the absence of any surface layer and other extraneous materials (e.g., sand), the susceptibility to pitting corrosion was low, as found with Pipe B. CONCLUSIONS Based on field experiments conducted over a period of four years in six operating fields, it was found that: * Pitting corrosion rates were similar when the compositions of surface layers were similar. * When a compact layer of a single species formed, the surface was protected from pitting corrosion; the FeS layer was more protective than the FeCO3 layer. * When multiple layers of several species formed, the susceptibility of the surface to pitting corrosion increased.
AbstractList Internal pitting corrosion, caused by carbon dioxide (CO2) and hydrogen sulfide (H sigma ub 2 capital sigma ), is one of the predominant failure mechanisms of these pipelines.1-7 An integrated model to predict internal pitting corrosion of oil and gas pipelines has already been described.8 According to this model, the internal pitting corrosion of oil and gas pipelines occurs in four stages: -the low- or no-corrosion stage when the internal surface of the pipeline is covered by hydrocarbons, i.e., oil-wet conditions; -formation of surface layers on the steel surface due to corrosion reactions once the surface is covered with water, i.e., water-wet conditions; -initiation of pits at localized regions on the steel surface when surface-layer breakdown occurs; and -pit propagation and eventual penetration of the pipe wall. In the absence of any surface layer and other extraneous materials (e.g., sand), the susceptibility to pitting corrosion was low, as found with Pipe B. CONCLUSIONS Based on field experiments conducted over a period of four years in six operating fields, it was found that: * Pitting corrosion rates were similar when the compositions of surface layers were similar. * When a compact layer of a single species formed, the surface was protected from pitting corrosion; the FeS layer was more protective than the FeCO3 layer. * When multiple layers of several species formed, the susceptibility of the surface to pitting corrosion increased.
Internal pitting corrosion, caused by carbon dioxide (CO2) and hydrogen sulfide (H^sub 2^S), is one of the predominant failure mechanisms of these pipelines.1-7 An integrated model to predict internal pitting corrosion of oil and gas pipelines has already been described.8 According to this model, the internal pitting corrosion of oil and gas pipelines occurs in four stages: -the low- or no-corrosion stage when the internal surface of the pipeline is covered by hydrocarbons, i.e., oil-wet conditions; -formation of surface layers on the steel surface due to corrosion reactions once the surface is covered with water, i.e., water-wet conditions; -initiation of pits at localized regions on the steel surface when surface-layer breakdown occurs; and -pit propagation and eventual penetration of the pipe wall. In the absence of any surface layer and other extraneous materials (e.g., sand), the susceptibility to pitting corrosion was low, as found with Pipe B. CONCLUSIONS Based on field experiments conducted over a period of four years in six operating fields, it was found that: * Pitting corrosion rates were similar when the compositions of surface layers were similar. * When a compact layer of a single species formed, the surface was protected from pitting corrosion; the FeS layer was more protective than the FeCO3 layer. * When multiple layers of several species formed, the susceptibility of the surface to pitting corrosion increased.
Experiments were conducted in six operating oil and gas production pipelines over four years to determine internal pitting corrosion rates under realistic operating conditions. —Pitting corrosion rates were similar when the compositions of surface layers were similar. —When a compact layer of single species formed, the surface was protected from pitting corrosion; the iron sulfide (FeS) layer was more protective than the siderite (FeCO3) layer. —When multiple layers of several species formed, the susceptibility of the surface to pitting corrosion increased. Frequent changes in the pipeline operating conditions facilitated the formation of multiple layers. —When no surface layer formed, the susceptibility of the surface to pitting corrosion decreased but was not eliminated. Extraneous materials (e.g., sand) on the surface facilitated pitting corrosion. —In the absence of surface layer and extraneous materials, no pitting corrosion was observed.
Author MICHAELIAN, K
PAPAVINASAM, S
DEMOZ, A
REVIE, R. W
OMOTOSO, O
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Issue 11
Keywords Gas pipeline
Prediction
Localized corrosion
Gas industry
Corrosion rate
sour
oil and gas pipelines
pitting corrosion rate
internal pitting corrosion
Pipeline
Oil industry
Pitting corrosion
sweet
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Snippet Internal pitting corrosion, caused by carbon dioxide (CO2) and hydrogen sulfide (H^sub 2^S), is one of the predominant failure mechanisms of these...
Experiments were conducted in six operating oil and gas production pipelines over four years to determine internal pitting corrosion rates under realistic...
Internal pitting corrosion, caused by carbon dioxide (CO2) and hydrogen sulfide (H sigma ub 2 capital sigma ), is one of the predominant failure mechanisms of...
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StartPage 741
SubjectTerms Applied sciences
Carbon dioxide
Corrosion
Corrosion effects
Corrosion environments
Corrosion products
Corrosion rate
Covering
Exact sciences and technology
Experiments
Fourier transforms
Gas pipelines
Gas production
Hydrogen sulfide
Iron carbonate
Iron sulfides
Mathematical models
Metals. Metallurgy
Natural gas
Oil and gas production
Petroleum pipelines
Pipelines
Pipes
Pitting (corrosion)
Protected species
R&D
Repair & maintenance
Research & development
Sand
Scanning electron microscopy
Siderite
Steel
Submarine pipelines
Sulphides
Surface layers
Title Effect of Field Operational Variables on Internal Pitting Corrosion of Oil and Gas Pipelines
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