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Picture for Study of Minimal Surface Preparation for Various Patch Repair Coating Products Applied under the Minimum Allowable Temperatures
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Study of Minimal Surface Preparation for Various Patch Repair Coating Products Applied under the Minimum Allowable Temperatures

Product Number: 51324-21005-SG
Author: Shan (Sherry) Rao; Da Kuang; Connor McManus
Publication Date: 2024
$40.00
Patch repair coating products provide cost-effective solutions for restoring small to medium-sized damages in mainline coatings to extend the lifespan of pipelines. Some coating products are specially designed to tolerate reduced surface conditions while providing the adequate corrosion protection performance. Due to easy mobilization and relatively inexpensive, power tool cleaning is commonly used in the field to prepare surfaces for small area repairs. During field coating work, adverse weather conditions are often encountered. However, little data were publicly available to support if the minimal surface recommended by the product data sheet (PDS) is also suitable for the coating applied under the minimum allowable temperature. In addition, the effect of the similar surface level produced by different power tools on the corrosion resistance of the same coating is rarely reported. This paper aims to address these gaps. Four commercially available coating products were selected to examine their potentials as patch repairs, including one liquid-applied epoxy coating, one butyl-based sealant product, and two viscoelastic coating products. Test samples were prepared using a rust grade C steel pipe section. Different power tools such as wire brush, rotary sander, flap disc, and bristle blaster were used to create SSPC-SP3, SSPC-SP11, and SSPC-SP15 surfaces. All four products were applied and cured at the minimum allowable temperatures specified in their respective PDS or recommended by the manufacturers. A 14-day cathodic disbondment (CD) test was employed to rule out the improper surfaces or power tools, and the next higher surface level was then considered as potentially suitable. The long-term performance characteristics of these coating products on the established minimal surfaces under the minimum allowable application temperatures were evaluated using the selected critical tests from CSA Z245.30 standards.
Picture for Study of Phase Distribution on Alloy UNS N07718 in Different Hardening Conditions and Its Relationship With Hydrogen Embrittlement Susceptibility
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Study of Phase Distribution on Alloy UNS N07718 in Different Hardening Conditions and Its Relationship With Hydrogen Embrittlement Susceptibility

Product Number: 51319-13025-SG
Author: Julia Botinha
Publication Date: 2019
$20.00
Picture for STUDY OF THE INHIBITIVE EFFECT OF NOVEL SCHIFF BASE ON CORROSION OF HCl ON MILD STEEL
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STUDY OF THE INHIBITIVE EFFECT OF NOVEL SCHIFF BASE ON CORROSION OF HCl ON MILD STEEL

Product Number: 51312-01478-SG
ISBN: 01478 2012 CP
Author: Smita M. Jauhari
Publication Date: 2012
$20.00
Picture for Study of Vapor Corrosion Inhibitors Built in to Corrosion Control Covers: Do VCIs Last the Life of the Covers?
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Study of Vapor Corrosion Inhibitors Built in to Corrosion Control Covers: Do VCIs Last the Life of the Covers?

Product Number: 51321-16175-SG
Author: Seckin Ozol / Na Qi
Publication Date: 2021
$20.00
Picture for 11403 Study on Effect of Phosphate Species on Green Rust Transformation
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Study on Effect of Phosphate Species on Green Rust Transformation in Steel in Marine Environment

Product Number: 51300-11403-SG
Author: Gadadhar Sahoo, Shun Fujieda, Kozo Shinoda and Shigeru Suzuki
Publication Date: 2011
$20.00
Picture for Study on Glycol Reboiler and Surge Vessel Corrosion in Glycol Regeneration Unit
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Study on Glycol Reboiler and Surge Vessel Corrosion in Glycol Regeneration Unit

Product Number: 51319-13289-SG
Author: Ali Akrouf
Publication Date: 2019
$20.00

Glycol systems are widely used in gas processing plants for the removal of contaminants such as moisture from the gas. Since the majority of the piping and vessels in these plants are fabricated from carbon steel there is a high potential for corrosion. This paper provides a brief overview of some of the major corrosion mechanisms associated with Glycol regeneration unit. In addition a case study from a Try-Ethylene Glycol (TEG) regeneration system is also discussed where localized corrosion was noticed in the Glycol reboiler and surge vessel. Booster Station facility receives gas from Gathering Center for further compression and removes moisture before being exported to the refinery. This is achieved by compression of gas in multiple stages with locally provided compression equipment and processed in glycol dehydration units to remove the moisture. Water vapor removal from the gas stream is achieved by contacting the wet gas counter-currently with lean (dry) TEG in the glycol contactor column. The rich glycol having water content is routed through a pre-heating coil flash tank filters and finally comes in the Glycol reboiler. Due to the high temperature in reboiler the glycol loses its ability to hold water. Separated water is vaporized and leaves through top of the still column. The regenerated glycol flows to the surge tank and from there it is pumped to Glycol absorber. During one of the Plant Maintenance shutdowns Glycol reboiler and surge vessel were opened for internal inspection and appreciable corrosion was noticed in the top sections of the vessels. A study was initiated to find out the probable causes of the deterioration. Corrosion products were collected for XRD analyses. Also chemical analysis of lean & rich Glycol samples taken from various streams was carried out. A corrosion pattern was established along the glycol regeneration circuit which revealed mainly the low pH of Rich Glycol due to possible decomposition reaction of glycol into organic acid. Presence of Iron sulfate and various forms of iron sulfide including Pyrite Greigite and Pyrhotite (also referred to as Black Powder Derivatives) all known to expedite localized corrosion and deterioration of the metals. This paper presents the findings based on the analysis of the corrosion products and glycol samples and discusses the possible corrosion mechanisms. Recommendations are also provided to ensure the integrity and reliability of these vessels for sustainable operation. This case history demonstrates the diverse nature of the causes of Glycol related corrosion in plants and the differing approaches that have to be taken to mitigate corrosion in Glycol regeneration equipment.