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 in | Corrosion (Houston, Tex.) Vol. 65; no. 11; pp. 741 - 747 |
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Main Authors | , , , , |
Format | Journal Article |
Language | English |
Published |
Houston, TX
NACE International
01.11.2009
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Subjects | |
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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. |
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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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Copyright | 2015 INIST-CNRS Copyright National Association of Corrosion Engineers Nov 2009 Copyright NACE International Nov 2009 |
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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 Application |
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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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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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