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3228 total products found.
Corrosion, perforated polymer lined pipelines, CO2, H2S, computational modelling, electrochemistry.
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Corrosion Prediction in Perforated Polymer Lined Pipelines (PLP) Used for Oil & Gas Transportation

Product Number: 51324-20954-SG
Author: Gaurav R. Joshi; Remy Mingant; Jean Kittel; Jitender Rai; Carol Taravel-Condat
Publication Date: 2024
$40.00

The perforated polymer-lined pipeline (PLP) is a rigid carbon steel pipeline with internal polymer liner for internal corrosion prevention. The liner is perforated to prevent liner collapse during depressurization. Although the perforations expose the carbon steel to the corrosion fluids within the bore of the pipeline, extensive small-scale and full-scale tests have demonstrated that corrosion at the bottom of each perforation is much less than the corrosion in an un-lined carbon steel pipeline. Based on experience gained on the evaluation and modelling of corrosion in the highly confined environments of flexible pipelines, we have developed a corrosion model to simulate carbon steel corrosion rates corresponding to the perforated PLP system geometry. Predictions from this model could help evaluate corrosion risks at and within perforated liner / steel interfaces. This paper presents an overview of the model and compares its predictions against a variety of experimental data that reproduce the conditions, the geometry, or both, found at the bottom of a PLP perforation. This 1D model considers diffusion and chemical reactions inside an inert hole and incorporates non-ideal thermodynamics (i.e., gas fugacity effects) to describe the aqueous solution chemistry. Electrochemical corrosion equations are compared with experimental data to support validation. This model could serve as a useful tool that complements qualification testing and help validate the PLP technology for a variety of field applications.

Picture for Nanolaminar Nickel-Cobalt Coatings: a Revolution in Wear and Corrosion Resistance
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Picture for Can Electrochemical Charging Replace Hydrogen Gas Charging During Hydrogen Embrittlement Testing?
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	Picture for Compatibility Study of HDPE Internal Lining in Carbon Steels for Polymer Injection and Mixing Applications
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Compatibility Study of HDPE Internal Lining in Carbon Steels for Polymer Injection and Mixing Applications

Product Number: 51324-20607-SG
Author: Ahmed Al Yahyaai; Amjad Al Kharusi; Bushra Al Hudar; Hilal Al Shuhumi; Mohammed Al Maqbali
Publication Date: 2024
$40.00
	Picture for Synthesis of Aminopropyl-modified Silica with Hydrophilic Branches Inhibitor for Corrosion Inhibition
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Synthesis of Aminopropyl-modified Silica with Hydrophilic Branches Inhibitor for Corrosion Inhibition

Product Number: 51324-20630-SG
Author: Norah Aljeaban; Ahmed Busaleh; Bader Alharbi; Tawfik A. Saleh
Publication Date: 2024
$40.00
Picture for Effect of Drying on Corrosion Mitigation of Hanford Transfer Lines
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Effect of Drying on Corrosion Mitigation of Hanford Transfer Lines

Product Number: 51324-20794-SG
Author: Pavan K. Shukla; Joshua Boerstler; Roderick E. Fuentes; Bruce J. Wiersma; Crystal Girardot
Publication Date: 2024
$40.00
Radioactive waste is stored in underground, carbon-steel double-shell tanks at the Department of Energy Hanford site. The waste is transferred between the tanks and other assets using the transfer lines spanning throughout the various tank farms at Hanford. The transfer lines consist of a pipe-in-pipe design, small diameter pipes, and are not piggable. Recent inspection data of the transfer lines have shown areas with corrosion on both interior of the encasements and exterior of the primary pipes, with nearly 50 percent wall loss on the primary pipes and nearly 25% wall loss on the encasement pipes due to pitting corrosion. The visual inspections of the transfer lines have shown presence of corrosion products near the pipeline risers and beyond. It has been hypothesized that the corrosion is predominantly due to the high humidity conditions and in some cases is driven by the presence of residual hydrotest water in the encasement and the associated contact with the safety significant primary pipe. Therefore, drying of the transfer lines could lead to corrosion mitigation. Experimental studies are being conducted to understand the effect of environmental conditions, especially, relative humidity and temperature, on transfer line grade carbon steel corrosion and on mitigating corrosion. The experimental conditions are selected based on the seasonal temperature changes, and relative humidity conditions ranging from 30 to 100 percent. The experimental data will be used as guidance for maintaining a dry environment that will help mitigate the transfer-line corrosion caused by the high humidity conditions.