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Picture for Mitigation Of Flange Face Corrosion During Plant Construction
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Mitigation Of Flange Face Corrosion During Plant Construction

Product Number: 51321-16742-SG
Author: Takahiro Tsuda; Nozomi Satake; Manabu Itoki
Publication Date: 2021
$20.00
Picture for Mitigation of Microbiologically Influenced Corrosion in Stagnant Fire Water Lines
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Mitigation of Microbiologically Influenced Corrosion in Stagnant Fire Water Lines

Product Number: MECC23-20008-SG
Author: Faisal Al-Refai; Abdulaziz Al-Beajan; Fahad Al-Qanaee; Anas Abdelmotelb; Vinoraj Selvaraj
Publication Date: 2023
$20.00

Utility water and fire water which is desalinated is supplied by Ministry of Electricity & Water (MEW) and stored in utility/fire water tank (70-T-0002). The process areas and the tanks are protected by desalinated water as fire water backed up by sea water and the buildings are protected completely by desalinated water. Buildings to be protected by desalinated fire water are fire station, maintenance & operation building, warehouse, workshop, laboratory, and administration building. DF water system used in buildings are stagnant and for the fire water in tanks are used frequently.
Picture for Mitigation Of Scaling Challenges For Long-Term Shut-In Wells Under Ultra-High Temperature
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Mitigation Of Scaling Challenges For Long-Term Shut-In Wells Under Ultra-High Temperature

Product Number: 51321-16995-SG
Author: Zhiwei (David) Yue; Megan Westerman; Ping Chen; Chunli Li; John Hazlewood
Publication Date: 2021
$20.00
Picture for Mitigation Of Scaling Potential Using Organophosphorus Phosphonates In High-Temperature And High-Hardness Carbonate Formations
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Mitigation Of Scaling Potential Using Organophosphorus Phosphonates In High-Temperature And High-Hardness Carbonate Formations

Product Number: 51322-17588-SG
Author: Jian Hou, Tao Chen, Ming Han, Mohammed Bataweel
Publication Date: 2022
$20.00

Scale is an adherent deposit of inorganic compounds precipitated from water onto surfaces. Most oilfield waters contain certain amounts of dissolved calcium, barium or strontium salts. The mineral scale can be formed by chemical reactions in the formation water itself, by mixing of formation water with injected seawater, or by mixing of the well streams of two incompatible oilfield waters. In carbonate reservoirs, when calcium is deposited as calcium sulfate or calcium carbonate scale, a loss of production and increased maintenance expenses can result. Therefore, effective mitigation of scaling potential is of importance to the oil producers.
Picture for Mitigation of Soil-Side Bottom Corrosion of Aboveground Storage Tanks Utilizing Volatile Corrosion
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Mitigation of Soil-Side Bottom Corrosion of Aboveground Storage Tanks Utilizing Volatile Corrosion

Product Number: 51317--9462-SG
ISBN: 9462 2017 CP
Author: Kelly Baker
Publication Date: 2017
$20.00

Electrical resistance probes monitor mitigation of corrosion. Data will be presented from multiple installations demonstrating the ability of volatile corrosion inhibitors to mitigate corrosion for soil-side bottoms of aboveground storage tanks.
Picture for Mitigation of Sour Corrosion Using Novel Fast Acting Hydrogen Sulfide Scavengers
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Mitigation of Sour Corrosion Using Novel Fast Acting Hydrogen Sulfide Scavengers

Product Number: 51317--9446-SG
ISBN: 9446 2017 CP
Author: Sunder Ramachandran
Publication Date: 2017
$20.00

A new experimental apparatus to evaluate H2S scavengers. Enables an assessment of scavenger efficiency and kinetics. Laboratory results are presented for a new, fast-acting H2S scavenger that is similar, but not identical, to previously described fast-acting H2S scavengers.
Picture for Mixed Metal Oxide Coated Titanium for Impressed Current Anodes Cathodic Protection
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Mixed Metal Oxide Coated Titanium for Impressed Current Anodes Cathodic Protection

Product Number: MECC23-20036-SG
Author: Talal Al-Zahrani; Abdullatif Al-Abdulhadi; Haitham Al-Jahani; Nayef Al-Anazi; Balasubramani Bakthavatchalu; Abdulrahman Al-Huwaiji
Publication Date: 2023
$20.00

Eliminating and mitigating corrosion is one of the major objectives that oil-and-gas industries are adopting to enhance and optimize the life of their assets. It is achieved by applying scientifically proven concepts that allows industries to with stand corrosion impacts, such as: cathodic protection. It is an electrochemical technique that controls a corrosion cycle by shifting the reaction and electrical potential of the metal surface, which requires protection, from anodic oxidized region to cathodic reduced region.
Picture for Mobile Application as a Tool to Ensure Effective Corrosion and Asset Integrity Management
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Mobile Application as a Tool to Ensure Effective Corrosion and Asset Integrity Management

Product Number: 51321-16353-SG
Author: Hajir Al Huraizi/Salim Al Harrasi/Monica Fernandez/Anwaar Al Kindi
Publication Date: 2021
$20.00
Picture for Modeling Abrasion-Corrosion in Horizontal Pipeline Slurry Flows
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Modeling Abrasion-Corrosion in Horizontal Pipeline Slurry Flows

Product Number: 51319-13125-SG
Author: Kofi Freeman Adane
Publication Date: 2019
$20.00

Slurry pipeline systems are used to process and transport mined ore and tailings in the oil and gas and mining industries. The handling processing and transporting of these slurries result in significant pipe wall material losses or wear. For the most widely used material carbon steel these losses are attributed to the combined effects of erosion/abrasion and corrosion due to the exposure of pipe wall materials to an aerated mixture of solids and liquids. In an attempt to mitigate this challenge some end-users such as mined oil sands operators have adopted polymer based pipe liner which basically only experiences erosion or abrasion damage. Models can be used as a predictive tool to optimize slurry design and processes material selection and/or even used as a tool for preventive maintenance. They are also being employed for technology assessment and product evaluation. These benefits are realized if the models are based on underlying mechanics or phenomena in the real systems. Unarguably there are a significant number of models for erosion-corrosion especially erosive wear. These models have a varying degree of accuracy which is partly due to the fact that most of them are based on some degree of empiricism and may lack accurate information on key parameters. Unfortunately models for wear which usually occurs in dense slurries are very limited despite most slurry applications fall under this category. As part of a broader wear model development project at our company this work focuses on validations of existing abrasive wear and/or abrasive-corrosion models. This work adopts computational fluid dynamic (CFD) as a tool to model abrasive wear and/or abrasion-corrosion in horizontal pipeline dense slurries. These CFD results will be compared with previously acquired wear data in our pilot-scale slurry flow loop for mild and dual-phase stainless steels pipe spools. The model performance will be presented and discussed with recommendations for future works.Key words: Wear; Pipeline; Slurry; Oil sands; Abrasion-corrosion; Flow Loop; CFD; modeling
Picture for Modeling and Experimental Insights of Sulfide Stress Cracking Corrosion Mechanism
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Modeling and Experimental Insights of Sulfide Stress Cracking Corrosion Mechanism

Product Number: 51317--9328-SG
ISBN: 9328 2017 CP
Author: Daniella Sales
Publication Date: 2017
$20.00

A model was built that describes stress field and hydrogen activity at the direct vicinity of a crack tip. A second model was based on the cohesive zone simulates the kinetic of a crack growth. Experiments using hydrogen permeation under stress on flat un-notched & notched specimens yielded data comparable to the simulations.
Picture for Modeling and Experiments of FeCO3 Scale Growth and Removal for Erosion-Corrosion Conditions
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Modeling and Experiments of FeCO3 Scale Growth and Removal for Erosion-Corrosion Conditions

Product Number: 51312-01132-SG
ISBN: 01132 2012 CP
Author: F. M. Al-Mutahar
Publication Date: 2012
$20.00
Picture for Modeling and Prediction of Pipeline External Corrosion
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Modeling and Prediction of Pipeline External Corrosion

Product Number: 51324-20704-SG
Author: Naim Dakwar; Sankara Papavinasam; Abdullah Hammoud
Publication Date: 2024
$40.00
External corrosion (EC) is still the leading cause of oil and gas transmission pipeline incidences. The primary source for understanding external corrosion risk is one of the interrelated parameters: EC rate, remaining wall thickness, or percentage wall loss. They may be obtained from five (5) sources: laboratory data (CLab), field operating conditions (CField), field above ground surveys (Csurveys), inline inspection (CILI), and field below ground inspection (CFBGM). • Laboratory data (CLab) and field operating data (CField) are “leading indicators” of localized pitting corrosion rate. • Field above ground surveys (Csurveys) are “current indicators”. • ILI (CILI) and field below ground inspection (CFBGM) are “past indicators”. The paper compares leading indicators CLab and CField with present condition indicator (CAbove) and trailing indicators (CILI, and CFBGM) of two (2) Saudi Aramco pipelines. This paper describes the success of the approach, lessons learned, and future improvements. How this approach is superior to other methods of prediction such as machine learning and simulation has been explained and how using the 5-M methodology as the based can accelerate the development of other approaches (artificial intelligence (AI) and simulation) has been described.
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