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Picture for Long Life Chloride Affected Concrete Structures – Some Corrosion Mechanistic Considerations
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Long Life Chloride Affected Concrete Structures – Some Corrosion Mechanistic Considerations

Product Number: 51321-16919-SG
Author: W K Green; J B Katen; D B McDonald
Publication Date: 2021
$20.00
Picture for Long Distance, Long Duration Case Study of Successful Inhibitor Application on a Very Light Hydrocarbon Pipeline
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Long Distance, Long Duration Case Study of Successful Inhibitor Application on a Very Light Hydrocarbon Pipeline

Product Number: 51324-21214-SG
Author: Trevor Place; Tyler Markowski; Jennifer Sargent; Hitesh Bagaria
Publication Date: 2024
$40.00
The operating mileage of North American pipelines transporting low density, high API gravity hydrocarbon liquids has increased significantly over the past two decades. This trend began in the early 2000’s because of increasing oil sands production in Canada, where light hydrocarbons are used to reduce the viscosity of bitumen to achieve practical ‘heavy oil’ specifications suitable for pipeline transport. The light tight oil boom of the 2010’s continued this trend, as multistage fracking unlocked high API gravity liquids from previously low permeability shale and sandstone formations. While different in origin and composition, light tight oils (LTOs), diluents used for bitumen transportation, and some refined products are similar in terms of density (density 680-800 kg/m3, or API 35-70), viscosity (<1cSt), and steel surface wetting behavior (hydrophilic). In previous works, the use of the NACE TM0172 ‘spindle test’ was demonstrated as an effective screening tool to assess the performance of corrosion inhibitors1 and led to the recommendation of hydrocarbon soluble inhibitors. Digital coupon analysis was used to provide unbiased quantification of results allowing better discrimination of inhibitor performance.2 The authors also provided an exploration of parasitic inhibitor consumption by fluid borne particulate.3 This work completes a decade-long pipeline case history where effective corrosion inhibition was used to solve a myriad of particulate related issues in a long-distance diluent carrying pipeline. Significant learnings about the performance and longevity of inhibitor (successfully applied at only one location of a 2500 km pipeline), the measurement of dissolved and particulate adsorbed inhibitor, the effect of maintenance pigging on the inhibitor film, and unexpected learnings about the ability of the inhibitor to disperse accumulated particulate is presented.
	Picture for Localized Corrosion Limit of Use of S13%Cr (UNS S41427) Connector in Converted Injection Treated Seawater Well
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Localized Corrosion Limit of Use of S13%Cr (UNS S41427) Connector in Converted Injection Treated Seawater Well

Product Number: 51324-20714-SG
Author: Nicolas Larché; Marianne Kleive; Charles Leballeur; Eva Malmanger
Publication Date: 2024
$40.00
Many systems can be converted and used for different applications not initially planned. This is the case for production wells, sometimes converted into water injection wells and for which the production tubing material selection is clearly not adapted for prolonged contact with natural seawater. Oxygen removal treatment must be applied but precise control is not obvious and excursions above zero or close-to-zero oxygen can occur. The production tubing material S13%Cr are known to be sensitive to dissolved oxygen excursions in seawater, but data from the literature cannot precisely help in defining the allowed limits of use. Exploring the possibility to convert a production well into a treated seawater injection well then requires a careful assessment of the corrosion resistance limits of the involved alloys. A series of corrosion tests in treated seawater were designed to assess the limits of use of fast connector made of alloy UNS S41427. The corrosion tests were performed both at laboratory scale and on full-scale fast connectors in a treated seawater flow loops simulating service conditions. For all the performed tests, maintaining the dissolved oxygen content (DOC) at 15 ppb and below never led to localized corrosion and has been considered as a safe condition in terms of corrosion risk for alloy S41427 at ambient temperature. It was found that prolonged dissolved oxygen content (DOC) above 30±10 ppb may lead to initial crevice corrosion after only 4 h of exposure. Globally, a very good correlation between the laboratory and the full-scale test results was found. The critical crevice potential for alloy S41427 was significantly affected by the cleaning process of the tested coupons, while the stop of the corrosion was always measured for potentials reached at DOC < 10 ppb. The proposed methodology, involving both laboratory and full-scale tests, allowed to precisely quantify the limits of use of UNS S41427 in treated injection well. It could be used for any other material and applications to help at designing adapted and reliable engineering diagrams for material selections.
Picture for Localized Corrosion Behavior of Lean Duplex Stainless Steels in Chloride Containing Synthetic Tap Water
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Localized Corrosion Behavior of Lean Duplex Stainless Steels in Chloride Containing Synthetic Tap Water

Product Number: 51319-13280-SG
Author: Sang Won Cho
Publication Date: 2019
$20.00

Duplex stainless steel (DSS) is a material in the issue as it’s very excellent in corrosion resistance mechanical properties weldability in various environments as compared with common materials. Due to these characteristics DSS is applied to various industries such as petrochemical facilities offshore structures power plants etc. However since duplex stainless steel is expensive it has a limitation that it is difficult to apply it to equipment that needs to be replaced periodically. Compared to DSS lean duplex stainless steel (LDSS) has good formability and corrosion resistance while the reduced content of nickel molybdenum is superior in terms of economics. Therefore LDSS can be economically efficiently maintained and managed by applying it to equipment requiring periodic replacement such as a plate or a tube of a heat exchanger.At present in the district heating system a plate heat exchangers of austenitic SS material are installed and it is always exposed to chloride containing environments. Generally failures of the plate heat exchanger are occurred by the tap water of user side and it is mainly broken due to crevice induced corrosion cracking between the gasket and the heat exchanger pitting etc. As a result researches on localized corrosion of austenitic SS and DSS are actively underway in chloride containing environments. Whereas there are few researches on the localized corrosion behavior of LDSS in these environments. Therefore in this study we would like to evaluate the localized corrosion behavior of LDSS in the chloride containing synthetic tap water at 60 ℃ which is the operating condition of plate heat exchanger for district heating system.