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Picture for Extension of Cathodic Protection Effect to Steel Piles At Tidal and Splash Zone
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Extension of Cathodic Protection Effect to Steel Piles At Tidal and Splash Zone

Product Number: 51314-3627-SG
ISBN: 3627 2014 CP
Author: Mohamed Khalil
Publication Date: 2014
$0.00
Picture for External Corrosion Behavior of Oil Pipelines With Polyethylene Coating Under Pressure Fluctuations
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External Corrosion Behavior of Oil Pipelines With Polyethylene Coating Under Pressure Fluctuations

Product Number: 51319-13199-SG
Author: Yanping Li
Publication Date: 2019
$20.00

External corrosion on buried pipe steels has been demonstrated to be a major threat to pipeline integrity. Although it has been extensively investigated and well understood electrochemically there is no particular model that is widely accepted by industry due to the complex nature of external corrosion. This paper demonstrates that the severity of external corrosion on polyethylene (PE) tape coated oil pipe is exacerbated by proximity downstream of pump stations and suggests mechanistic explanations related to pressure fluctuations. There are very limited studies available on this topic for buried liquid pipelines.External corrosion features reported by the most recent In-Line Inspection (ILI) ultrasonic wall measurement (UTWM) tools for two oil pipelines were correlated with the distance to upstream (U/S) pump stations. ILI data with UTWM is used because the data includes features that are under sleeve. These two oil pipelines with PE coating were investigated for a total length of about 2500 km. The pipelines have been in service for more than 40 years.Analysis of the results shows that external corrosion features with a depth <20% wall thickness (WT) reported by UTWM tools are distributed uniformly along the pipelines. However a clear increase in the frequency of corrosion features with depth >=20%WT is seen within 10 km from the U/S pump station. There is a much more pronounced increase in the density of deeper feature classes in the same region. This trend is further validated by the distribution of field nondestructive examination (NDE) excavations driven by external corrosion. Based on these data it is undeniable that the frequency and severity of external corrosion on these tape coated pipelines is positively correlated to U/S pump station proximity.Possible mechanisms may include mechano-electrochemistry and pressure fluctuations that facilitate electrochemical processes and/or PE tape coating damage: 1) Pressure fluctuations increase dislocation density and thus electrochemical potential ahead of corrosion tip due to stress concentration. 2) Pressure fluctuations may refresh the electrochemical environments inside corrosion and thus accelerating corrosion. 3) The PE coating damage accelerated by pressure fluctuations could contribute to the external corrosion distribution. One of the benefits of the findings in this paper is to help External Corrosion Direct Assessment (ECDA) to locate severe corrosion features especially for the lines that are non-piggable. Also the discoveries can provide guidance for future research and pipeline integrity management with external corrosion.

Picture for Factors Affecting Impact Toughness in Carbon Steels
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Factors Affecting Impact Toughness in Carbon Steels

Product Number: 51319-13361-SG
Author: Sangeetha Cathapuram
Publication Date: 2019
$20.00
Picture for Factors for Selecting Thermal Insulation Materials to Prevent Corrosion Under Insulation
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Factors for Selecting Thermal Insulation Materials to Prevent Corrosion Under Insulation

Product Number: 51319-12952-SG
Author: Kentaro Mizushima
Publication Date: 2019
$20.00
Picture for Factors Influencing Droplet Corrosion in Dense Phase CO2
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Factors Influencing Droplet Corrosion in Dense Phase CO2

Product Number: 51319-13017-SG
Author: Ralph Baessler
Publication Date: 2019
$20.00

Recent studies have shown that even at a very low concentration of impurities (less than 100 ppmv of SO2 NO2 O2 and H2O) the droplet formation and condensation of sulfuric and nitric acids in dense phase CO2 are possible and observable. To reveal the mechanism of droplet corrosion in dense CO2 at high pressure and low temperature further studies on factors that affect wettability and resulting corrosion behaviors of transport pipeline steels are needed.In this work carbon steels (X52 X70) martensitic steel UNSS41500 and superaustenite UNS08031 were examined not only in static but also dynamic CO2 stream with either oxidizing (SO2 NO2 O2) or reducing (H2S and H2) impurities. Exposure tests with and without CO2 saturated water droplets were performed at both low temperature (278 K) and high temperature (313 K) at high pressure where CO2 is supercritical or in dense phase. To reveal the effects of surface morphology carbon steel coupons with different surface roughness were prepared not only to measure the wettability by contact angle but also to expose to CO2 stream containing oxidizing/reducing impurities to observe the condensation and possible droplet corrosion that followed. Two-week exposed coupons showed no condensation at 313 K 10 MPa and 50 ppmv H2O indicating the important role of temperature on the possibility of condensation regardless the type of impurities and flow rate. At 278 K the result from exposure tests signified the role of oxidizing impurities on the condensation and the droplet corrosion that followed. Although different surface roughness resulted in different wetting behaviors and therefore the measured contact angles it did not significantly influence the corrosion process upon long time exposure. This is attributed to the change of wetting behavior due to corrosion products that covered the carbon steel surface during exposure test.

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Factors On Tank Lining For Corrosion Prevention

Product Number: 51321-16583-SG
Author: N. S. S. Rajan
Publication Date: 2021
$20.00