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	Picture for Influence of the H2 Impurity on the Fatigue Crack Growth and Fracture in a Dense Phase CO2 Pipeline
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Influence of the H2 Impurity on the Fatigue Crack Growth and Fracture in a Dense Phase CO2 Pipeline

Product Number: 51324-20721-SG
Author: B Bezensek; S Hopkin; J Sonke; F Gui; C Taylor
Publication Date: 2024
$40.00
Transport of dense phase CO2 by pipelines needs to account for possible degradation mechanisms arising due to H2 impurity which can be present in (typically) the 0.75 ~ 1 mol% range depending on the specification used. H2 gas can affect fatigue and fracture properties even at low partial pressures and hence the integrity. In this study a complementary experimental and computational modeling program was undertaken. API 5L X65 grade material samples were used for comparable testing in pure H2 gas at low partial pressure H2 and in dense phase CO2 at 100 barg with H2 impurity added in a 2 mol% and 4 mol% increments (i.e. partial pressures of 2 barg and 4 barg). The test results show effect of the H2 impurity in the dense phase CO2 accelerated fatigue crack growth and reduced fracture toughness. These findings are supported by computational simulation using density functional theory and molecular dynamics. A scoping integrity assessment for a dense phase CO2 pipeline with H2 impurity at 2 mol% shows the measured accelerated fatigue crack growth only affects large pressure cycles (pressure range in excess of 70 bar for OD/WT pipelines of ~30). The fatigue life is significantly shortened compared to the pure CO2 pipeline and this is mainly driven by the reduced fracture toughness at low partial pressure H2. The fatigue damage is proportional to the maximum operating pressure (as it increases the pressure range). For a postulated 50-year design life a safe pipeline design window considering a range of conservative inputs (material properties, integrity operating window, geometry, postulated defect size etc.) a safe operating pressure of 2900 psig (200barg) was found for a new build pipeline using modern materials. For a repurposed vintage material pipeline the safe operating pressure was set at 2200 psig (150 barg). An ECA incorporating the deleterious effect of H2 should be conducted to confirm the above postulate unless the project falls within the limits of the conservative inputs (material properties, integrity operating window, geometry, postulated defect size etc.), from a fracture mechanics perspective, of the four case studies that form the basis of this overall study. Other impurities if exceeded their safe threshold may create water drop out and acid formation. It is imperative that the project specifications err on the side of caution and restrict the impurities to safe limits until further understanding of the complex interaction mechanisms is developed.
	Picture for Influence of the Soil Moisture Level and Differential Aeration Cell on the Corrosion Rate of Carbon Steel and Zinc Coated Steel
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Influence of the Soil Moisture Level and Differential Aeration Cell on the Corrosion Rate of Carbon Steel and Zinc Coated Steel

Product Number: 51324-20694-SG
Author: Erwan Diler; Philippe Verpoort; Souhail Amami; Ansbert De Cleene; Benoit Emo
Publication Date: 2024
$40.00
Picture for Influence Of The Surface Condition On The Pitting And SCC Resistance Of Alloy UNS N07718 Produced Via Selective Laser Melting
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Influence Of The Surface Condition On The Pitting And SCC Resistance Of Alloy UNS N07718 Produced Via Selective Laser Melting

Product Number: 51321-16949-SG
Author: Madison Woolridge; Christoph Wangenheim; Helmuth Sarmiento Klapper
Publication Date: 2021
$20.00
Picture for Influence of the UV Radiation on the Corrosion Resistance of the Carbon-Based Coatings for the Marine Industry
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Influence of the UV Radiation on the Corrosion Resistance of the Carbon-Based Coatings for the Marine Industry

Product Number: 51319-12950-SG
Author: Anastasiia Artemova
Publication Date: 2019
$20.00
Picture for Inhibited Erosion-Corrosion of Carbon Steel in Sweet Production with CaCO3 Versus Sand Particles
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Inhibited Erosion-Corrosion of Carbon Steel in Sweet Production with CaCO3 Versus Sand Particles

Product Number: 51319-13433-SG
Author: Anass Nassef
Publication Date: 2019
$20.00

In the oil and gas production industry carbon steel tubing and piping are susceptible to erosion-corrosion damage due to the erosive and corrosive nature of the flow. The combined effect of solid particle erosion and corrosion can increase the metal degradation rate while simultaneously decreasing the efficiency of corrosion protection systems including iron-carbonate scale formation and chemical inhibition. These combined effects can lead to higher corrosion rates surface pitting and material failure. Thus prediction of chemical inhibitor effectiveness when solid particles are being produced particularly important. Modeling this behavior is critical when the wells are deep or off-shore because coupon testing is impractical and replacement costs are high. Considerable research has been devoted to investigate the effect of sand erosion on the efficiency of corrosion inhibitors in sweet production/CO2 environments in presence of sand particles. However sand particles are not the only particles that occur during oil and gas production. Calcium carbonate (CaCO3) particles can also be produced during oil and gas production because the majority of oil and gas production in the world is from carbonate reservoirs where calcium carbonate (CaCO3) particles can enter into the flow of produced gas and oil. Currently little is known about the erosive effects of CaCO3 particles on the performance of corrosion inhibitors in CO2 environments. This paper describes experimental and modeling studies directed at understanding the influence of CaCO3 particles on the effectiveness of imidazoline-based inhibitor in reducing CO2 corrosion of carbon steel material. The performance of the inhibitor with CaCO3 particles is compared with the inhibitor performance for a flow containing sand particles. A phenomenological model based on Frumkin-type isotherm is presented as a technique for predicting inhibitor effectiveness for these flow conditions. Erosion-corrosion experiments were performed using flow loop set up with a direct impingement configuration in an iron carbonate forming environment. Electrochemical linear polarization resistance and weight loss methods were utilized to experimentally characterize erosion-corrosion rates for both types of solid particles.

Picture for Inhibition Of Calcium Carbonate Scale Formation In Water-Mono Ethylene Glycol Solutions By Water Soluble Polymers
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Inhibition Of Calcium Carbonate Scale Formation In Water-Mono Ethylene Glycol Solutions By Water Soluble Polymers

Product Number: 51321-16607-SG
Author: P.D. Natsi/ P.G. Koutsoukos
Publication Date: 2021
$20.00