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Picture for Materials Selection For Seawater Injection Service – Crevice Corrosion Testing Of Stainless Steels Under Controlled Dissolved Oxygen
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Materials Selection For Seawater Injection Service – Crevice Corrosion Testing Of Stainless Steels Under Controlled Dissolved Oxygen

Product Number: 51321-16527-SG
Author: K. J. Evans/ S. Chawla/ W. Huang
Publication Date: 2021
$20.00
Picture for Maximizing Materials Utility through a Next Life Optimization Process
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Maximizing Materials Utility through a Next Life Optimization Process

Product Number: 51324-20604-SG
Author: William Kovacs; Christopher David Taylor
Publication Date: 2024
$40.00
The carbon footprint of assets will increasingly be of importance to obtain beneficial, economic, social and environmental outcomes of design and engineering projects. Inclusion of a Next Life strategy at asset or product end-of-life can significantly reduce the greenhouse gas (GHG) emissions of First Life assets and Next Life reuses compared to the same uses made from virgin material or recycled content. Traditional engineering design and asset management often only plan for initial use and the management or maintenance strategies necessary to extend First Life, where the First Life is the primary engineering role of the asset. Critically missing from this picture are the costs and environmental impacts incurred throughout the asset or product lifecycle, especially associated with the end-of-life of an asset. A Next Life optimization process for these decisions is described herein that can aid in maximizing the overall Materials Sustainability and Materials Utility (i.e., longevity of fruitful usage) embedded in assets. It consists of appraisal, brainstorming, partnering and evaluation of beneficial impact for particular Next Life options allowing the benefits they can provide to First Life and Next Life opportunities. These benefits can include a reduction in carbon footprint over a lifecycle, cost savings related to GHG emissions, cost savings related to reused material/labor for Next Life assets, or other beneficial impact (even if increased financial cost). The process includes a qualitative conceptual assessment that can feed into a more detailed quantitative assessment for optimization of Next Life materials usage.
	Picture for MEA Triazine Contactor Optimization to Increase Efficiency and Reduce Fouling Potential
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MEA Triazine Contactor Optimization to Increase Efficiency and Reduce Fouling Potential

Product Number: 51324-20391-SG
Author: Willem-Louis Marais
Publication Date: 2024
$40.00
Liquid absorbents have been utilized for decades to remove impurities from produced natural gas. Throughout the last 15 years, monoethanolamine (MEA) triazine has become an industry-recognized name for the removal of sour gas (H2S). MEA triazine has one of the lowest cost profiles in terms of cost per mass of H2S removed and has obtained a commodity status. It is widely used in the oil and gas industry, both on production (upstream, midstream) and processing (downstream). MEA Triazine is typically applied via direct injection into flowlines or applied in contactor vessels (“scrubbers”, “towers”, “bubble columns”). The application type depends on numerous factors but in general, the application via contactor vessel is preferred due to its increased efficiency. However, due to the many different contactor configurations available, a wide range of efficiencies are achieved, ranging from 50 – 70%. MEA Triazine systems are also known to foul with acid-insoluble polymeric solids. This occurs when the MEA Triazine and its reaction products are not managed properly, or the system is not designed for the specific conditions. The spent material, commonly referred to as dithiazine, can form solids (amorphous dithiazine) in the contactor packing, post contactor separator, or in downstream pipelines if carry-over occurs. This paper aims to provide the reader guidance on how to optimize MEA Triazine contactor vessels to achieve maximum efficiency and to reduce or eliminate fouling. Optimization principles discussed will include contactor configurations, contactor modifications, and MEA Triazine properties and its effect on system performance. Increasing system efficiency and eliminating solids formation in these systems will have a direct impact on the user’s operating expense (OPEX). This is due to better scavenger utilization and a reduction in maintenance and downtime due to solids formation. A reduction in scope three emissions will also be achieved.
Picture for Measuring the Localized Corrosion Due to Carbonic Acid
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Measuring the Localized Corrosion Due to Carbonic Acid

Product Number: 51319-12923-SG
Author: Omar Yepez
Publication Date: 2019
$20.00

The mechanism of carbonic acid corrosion is of a paramount importance for the oil industry. This is because production of crude is always accompanied by CO2 and water. Carbonic acid localized corrosion is by far more important than general corrosion. This is because you just need one tiny rupture in the pipe to have a failure which will need to be addressed and repaired. Methods to determine localized corrosion are very few. In one method the electrochemical potential of the metal specimen is increased with time until the material fails which is detected as a large oxidation current. In another a large constant oxidative potential is imposed on the metal coupon then its temperature is increased until a high current is observed. In both the nature of the surface at corrosion potential is not preserved. Electrochemical noise has come to address this problems because this method does not perturb the surface of the metal and all its measurements occurs at open circuit potential. However this non-perturbative method has little quantitative value and the interpretation of the data obtained is still very difficult. For instance the noise current cannot be integrated to know the extension of the damage. This is because one does not know to what electrode the noise belongs. In this paper the localized carbonic acid corrosion of a carbon steel at corrosion potential was measured. This was performed by pulsing at the corrosion potential and changing the temperature of the test. Electrochemical impedance spectroscopy was also used in the same manner. In both methods the localized current was integrated and the localized damage was determined.Key words: Localized corrosion CO2 corrosion electrochemical methods.