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14122 total products found.
Picture for Problems Related to the Slow Strain Rate Test Performance and the Specimen Characterization in Auste
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51317--9715-Problems Related to the Slow Strain Rate Test Performance and the Specimen Characterization in Austenitic Corrosion Resistant Alloy Tubes

Product Number: 51317--9715-SG
ISBN: 9715 2017 CP
Author: Pilar Esteban
Publication Date: 2017
$20.00

The specimen surface, effect of filling rate were examined. Characterization of the primary fracture surface and the gauge section of the tested specimens was done by scanning electron microscopy and subsequent classification according to the NACE TM0198 standard.
Picture for Development of Corrosion Severity Assessment Algorithms Using Environmental Monitoring Sensors in Naval Aviation Environments
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Development of Corrosion Severity Assessment Algorithms Using Environmental Monitoring Sensors in Naval Aviation Environments

Product Number: 51324-20663-SG
Author: Alexander Lilly; Steven Kopitzke; Ian Long
Publication Date: 2024
$40.00
Currently, Naval aircraft are inspected for corrosion based on Reliability Centered Maintenance analysis of component failure rates in a feedback loop scheme. Recently developed sensors allow for the measurement and recording of temperature, relative humidity, and solution conductivity in 30 minute intervals. These sensors were deployed collocated with corrosion witness coupons across two 1-year deployments spanning 26 naval aviation relevant locations. Features were engineered from the sensor data, and algorithms were trained to predict the mass loss observed on the collocated witness coupons. Using leave-one-out-cross-validation, the highest performing algorithms possessed an accuracy of 77% in the classification of site corrosion severity based on Aermet 100 mass loss, a landing gear high strength steel.
Picture for Synchrotron Based X-Ray Fluorescence Microscopy Confirms Copper in the Corrosion Products of Metals
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Synchrotron Based X-Ray Fluorescence Microscopy Confirms Copper in the Corrosion Products of Metals

Product Number: 51317--9017-SG
ISBN: 9017 2017 CP
Author: Samuel Zelinka
Publication Date: 2017
$20.00

X-ray fluorescence microscopy (XFM) maps of corrosion products removed from corroded fasteners that had been in contact with preservative treated wood clearly show the presence of copper and confirm the mechanism of corrosion in treated wood.
Picture for Effect of Alloying Elements on the Corrosion Behavior of Carbon Steel in CO2 Environments
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51318-10997-Effect of Alloying Elements on the Corrosion Behavior of Carbon Steel in CO2 Environments

Product Number: 51318-10997-SG
Author: Yoon-Seok Choi / Srdjan Nesic / Hwan-Gyo Jung
Publication Date: 2018
$20.00

The objective of the present study was to evaluate the effect of alloying elements (Cr, Mo and Cu) on the corrosion behavior of low carbon steel in CO2 environments. Six samples were prepared with varying Cr content from 0 to 2 wt.% and with added 0.5 wt.% of Mo and Cu.
Picture for Corrosion of Fire Sprinkler Piping in Untreated Pond Water under Nitrogen
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51318-10535-Corrosion of Fire Sprinkler Piping in Untreated Pond Water under Nitrogen

Product Number: 51318-10535-SG
Author: Paul Su / Blair Swinnerton
Publication Date: 2018
$20.00

This study used untreated pond water containing corrosive anions and MIC-causing bacteria as an accelerated testing environment to explore the feasibility of nitrogen as a deoxygenation gas to mitigate corrosion of sprinkler pipes.
Picture for Study of Akaganeite in Weathering Steel Corrosion Products and Distance From Ocean in South Florida
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51318-11337-Study of Akaganeite in Weathering Steel Corrosion Products and Distance From Ocean in South Florida

Product Number: 51318-11337-SG
Author: Mahmoud Madani / Richard D. Granata
Publication Date: 2018
$20.00

The corrosion products on samples from 31 stations (0.1 to 21 miles from the ocean) were analyzed using XRD to observe the intensities and peaks related to akaganeite, goethite, lepidocrocite and hematite products.
Picture for Localized Corrosion of Mild Steel under Iron Sulfide Layers in CO2/H2S Environment
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51318-10990-Localized Corrosion of Mild Steel under Iron Sulfide Layers in CO2/H2S Environment

Product Number: 51318-10990-SG
Author: Saba Navabzadeh Esmaeely / Gheorghe Bota / Bruce Brown / Srdjan Nesic
Publication Date: 2018
$20.00

Mild steel specimens (API 5L X65) were pretreated to form a pyrrhotite layer on the surface using high temperature sulfidation in oil, then exposed to a range of aqueous CO2 and H2S corrosion environments, leading to initiation of localized corrosion.

 
Picture for 07205 Corrosion of Stainless Steel in Sulfamic Acid Cleaning Solutions
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07205 Corrosion of Stainless Steel in Sulfamic Acid Cleaning Solutions

Product Number: 51300-07205-SG
ISBN: 07205 2007 CP
Author: Joseph R. Kish, Neville J. Stead, and Douglas L. Singbeil
Publication Date: 2007
$20.00

An investigation was conducted to characterize the corrosion behavior of Type 316L stainless steel (UNS S31603) in a sulphamic acid (NH2HSO3) cleaning solution.
Picture for High Temperature Corrosion And Stress Corrosion Investigations Of SS316 In Molten Nitrate Salt

High Temperature Corrosion And Stress Corrosion Investigations Of SS316 In Molten Nitrate Salt

Product Number: ED22-17168-SG
Author: Camilla A. Stitt, Andrew Brittan, George A. Young, Anne Demma, and Micah J. Hackett, Andrew Dong and Peter Hosemann
Publication Date: 2022
$20.00

Solar Salt has many desirable properties as an intermediate heat transfer fluid including low corrosion rates (<10 μm/yr) at temperatures (T) <600°C, high oxidizing power for capturing tritium, low melting point, and relatively low cost. However, higher temperatures (T > 600°C) and other factors e.g., high flow rates, can significantly increase corrosion rates.
Picture for 10354 Case Studies of Corrosion Failures in Oil Refineries
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10354 Case Studies of Corrosion Failures in Oil Refineries

Product Number: 51300-10354-SG
ISBN: 10354 2010 CP
Author: Gyoung Taek Kim, Hyun Sik Hwang, Sung Lyong Oh, Byong Mu Kim
Publication Date: 2010
$20.00

This paper describes three corrosion case histories caused by overconfidence and lack of thorough understanding of the corroding systems. 1. Exchanger tube failure. 2. Hydrogen induced cracking. 3. Inappropriate mixing of process streams.

 
Picture for Pitting corrosion of steam generator tubing alloys in chloride solutions with thiosulfate additions
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51318-10979-Pitting corrosion of steam generator tubing alloys in chloride solutions with thiosulfate additions

Product Number: 51318-10979-SG
Author: Abraham A. Becerra Araneda / Mariano A. Kappes / Martín A. Rodríguez / Ricardo M. Carranza
Publication Date: 2018
$20.00

Alloys UNS N06600, N06690 and N08800 are used for steam generator tubes. Pitting corrosion was studied in 0.1 to 1 M chloride solutions with additions of thiosulfate ranging from 10-4 M to 10-2 M, at room temperature. The alloys were tested in solution annealed and thermally aged conditions.
Picture for 02273 THE ROLE OF ACETATE IN CO2...
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02273 THE ROLE OF ACETATE IN CO2 CORROSION OF CARBON STEEL: HAS THE CHEMISTRY BEEN FORGOTTEN?

Product Number: 51300-02273-SG
ISBN: 02273 2002 CP
Author: Yannick Garsany, Derek Pletcher, and Bill Hedges
Publication Date: 2003
$20.00

The influence of acetate ion on the rate of corrosion of carbon steel (X65) in 3 % NaCl brine saturated with carbon dioxide has been investigated using voltammetry at a rotating disc electrode. The rate of corrosion can only be understood if it is recognised that the cathodic process in the steel corrosion is affected by acetic acid.
Picture for Effect of Crevice Former on the Crevice Corrosion of 316L Stainless Steel in Synthetic Tap Water
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Effect of Crevice Former on the Crevice Corrosion of 316L Stainless Steel in Synthetic Tap Water

Product Number: 51317--9412-SG
ISBN: 9412 2017 CP
Author: Seon-hong Kim
Publication Date: 2017
$20.00

To restrain the failure of plate heat exchanger in customer boiler working fluid, the effect of crevice former type on the corrosion behavior of Type 316L (UNS S31603) stainless steel plate was investigated using electrochemical methods and surface analysis in chloride-containing synthetic tap water.
Variability in Accelerated Corrosion Testing
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Variability in Accelerated Corrosion Testing

Product Number: 51220-276-SG
Author: N. Rakers, J. Begley, A. Mubarok
Publication Date: 2020
$20.00

Accelerated corrosion test methods are regularly utilized in coating industries to predict the performance of coatings in real life exposure. The performance of coatings in these accelerated tests is a key step in the product development cycle. It is essential to understand different factors that may introduce variability in the test result. 
Picture for Application of Artificial Intelligence in Corrosion Management
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Application of Artificial Intelligence in Corrosion Management

Product Number: 51324-20711-SG
Author: Mohd Aswadi Ton Alias; Nurul Asni Mohamed; M Iskandar Bakeri; Izzatdin A Aziz; M Hilmi Hasan
Publication Date: 2024
$40.00
Corrosion management system encompassing the various stages of an asset life starting from design, construction, through to operation and decommissioning remains the key focus in ensuring integrity and safe operation of the asset. Corrosion study is conducted during the initial design phase, followed by multiple reviews during the operational stage as part of the overall corrosion management process. These studies aim to identify all damage mechanisms that can be present, including both non-age-related and age-related mechanisms. Currently in the oil and gas industry, corrosion rate predictions for age-related mechanisms are generated via mathematical equations or correlations as outcome from laboratory testing and analyses which may not be representative of the actual operating condition. These predictions impose limitations with regards to utilizing inputs produced from big data. Application of artificial intelligence to predict corrosion rate offers advantages where real high frequency data streams from IoT sensors are analyzed via machine learning algorithm thus providing prediction based on historical experience of specific asset. Data preprocessing is an important step in machine learning that involves transforming raw data from various parameters so that issues owing to the incompleteness, inconsistency, and/or lack of appropriate representation of trends are resolved to arrive at a data set that is in an understandable format. Feature engineering will then be performed which analyze the parameter correlation to obtain the most suitable combination and the best features and data characteristics. For corrosion rate prediction, the supervised learning algorithm is applicable such as logistic regression, naive bayes, support vector machines, artificial neural networks, and random forests. The final step of the machine learning modelling is the model validation. The predicted corrosion rates will be verified with actual thickness measurement at site. To date, we have covered 30 process units which includes different trains, 120 corrosion groups selected from a total of about 3800 corrosion groups for the whole facility. 700 customized machine learning models were developed. Success is defined by best highest accuracy (>80%) with an optimum model run time. Recent validation has shown the ability to predict an anomaly in future trend which coincides with actual increase in corrosion rate.
Technical Paper: Petroleum-Based Corrosion Inhibitor
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Technical Paper: Petroleum-Based Corrosion Inhibitor

Product Number: 41206-268-SG
Author: James R. Mott
Publication Date: 2006
$20.00

The effects of corrosion are wide-spread and widely known.  From construction to transportation and everything in between corrosion is a result of environmental effects on the metals we use to build.  Corrosion may be controlled, however, through the use of inhibitors as an on-going treatment in order to effectively stall the act of corrosion.  
Picture for Corrosion of 13Cr Steel at the Cement/Casing Interface in CO2/H2S Environments at 4 85 and 200 °C
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51318-11015-Corrosion of 13Cr Steel at the Cement/Casing Interface in CO2/H2S Environments at 4 85 and 200 °C

Product Number: 51318-11015-SG
Author: Justin Beck / Ruishu Feng / Derek M. Hall / Aysel Buyuksagis / Serguei N. Lvov / Margaret Ziomek-Moroz
Publication Date: 2018
$20.00

A study investigated corrosion at the cement/casing interface for 13Cr casing steel. Scanning electron microscopy (SEM) and energy dispersive X-ray spectroscopy (EDS) found that corrosion increased with increasing temperature.
Picture for TM0171-Autoclave Corrosion Testing of Metals in High Temperature Water-HD1971
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TM0171-HD1971-SG Autoclave Corrosion Testing of Metals in High Temperature Water-HD1971

Product Number: 21203-HD1971
Author: NACE
Publication Date: 1971
$179.00

Laboratory method for determining the extent and the rate of uniform corrosion of metals in high temperature water or aqueous solutions at temperatures (> 212 F (100 C) & <~680 F (360 C))…Historical Document 1971
Picture for Electrochemical Noise - Ready for Corrosion Monitoring in Lab and Field
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51318-11614-Electrochemical Noise - Ready for Corrosion Monitoring in Lab and Field

Product Number: 51318-11614-SG
Author: Guenter Schmitt / Peter Schrems / Lars Kuhl
Publication Date: 2018
$20.00

Corrosion measurement and monitoring with correlation to corrosion rates can now be applied directly in the field with a new stand-alone hand-held potentiostat/galvanostat in combination with a new in-house diagnosis software of electrochemical current noise.

 
Corrosion Issues in Sweet and Sour Oil & Gas Wells
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Corrosion Issues In Sweet And Sour Oil & Gas Wells

Product Number: 51322-18150-SG
Author: Janardhan Rao Saithala, Amjad Kharusi, Boris Thomas, Al Toqi Hamood, Mohammed Ghafri, Muatasam Aulaqi, Manal Al Badwawi, Talal Nabhani, Nasser Behlani
Publication Date: 2022
$20.00

The unstable oil market demand in the petroleum industry, the oil financial crisis and the Covid-19 pandemic have pushed the Oil and Gas operators to look for optimized, cost effective and more reliable strategies of design and operation. Large part of CAPEX is invested in the well materials. Hence, materials of Oil and Gas wells should be selected to withstand both internal and external threats to ensure integrity and availability while maintaining on focus on affordability over the lifecycle.1 
Life-Cycle Cost Evaluation of Corrosion Mitigation Strategies in the Mining Industry
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Life-Cycle Cost Evaluation Of Corrosion Mitigation Strategies In Mining Industry

Product Number: 51322-18146-SG
Author: M. Naghizadeh, Y. Savguira, M. Fatakdawala
Publication Date: 2022
$20.00

An economic evaluation of a project plays a significant role in determining its feasibility. Corrosion is intrinsic to the operation of metallic assets, and the costs dedicated to its prevention and/or its consequences are unavoidable. Different corrosion strategies could be developed to address the project's needs while complying with relevant codes and standards. These various corrosion control strategies are characterized by inherently different capital expenditures (CAPEX) and operating expenses (OPEX). Careful analysis of the cost projections for each of the considered corrosion mitigation strategies is needed for project optimization and improvement of return on investment.  
Corrosion Control of CUI in a Refinery
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Corrosion Control of CUI in a Refinery

Product Number: 51217-053-SG
Author: Art MacKinnon
Publication Date: 2017
$20.00

This paper will explain how to find CUI (Corrosion under Insulation within a refinery through proper inspection and, damage mechanisms, avoiding premature structural failure due to corrosion.
Picture for Volatile Corrosion Inhibitor for Prevention of Black Powder in Sales Gas Pipelines
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51318-10962-Volatile Corrosion Inhibitor for Prevention of Black Powder in Sales Gas Pipelines

Product Number: 51318-10962-SG
Author: Z. Belarbi / B. George, N. / Moradighadi, D. / Young, S. / Nesic, M. Singer / R. P. Nogueira
Publication Date: 2018
$20.00

Black powder is a generic term used to describe entrained corrosion products that can accumulate in sales gas pipelines. This study was to evaluate the efficiency of model inhibitor compounds.
Picture for Interaction of H2S/CO2/O2 on Hydrogen Permeation of X70 Steel in Sour Humidity Corrosion Environment
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51316-7362-Interaction of H2S/CO2/O2 on Hydrogen Permeation of X70 Steel in Sour Humidity Corrosion Environment

Product Number: 51316-7362-SG
ISBN: 7362 2016 CP
Author: Wei Liu
Publication Date: 2016
$20.00

Corrosion performance of 3%Cr steel in CO2 and CO2-H2S environments was investigated using high temperature and high pressure autoclave. Corrosion scales were characterized by x-ray powder diffraction, scanning electron microscopy and energy-dispersive X-ray spectroscopy.
Picture for Remote, Visual Inspection And Digital Analysis For External Corrosion Assessment In Refining Unit Applications
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Remote, Visual Inspection And Digital Analysis For External Corrosion Assessment In Refining Unit Applications

Product Number: 51321-16542-SG
Author: Slawomir Kus/ Sridhar Srinivasan
Publication Date: 2021
$20.00
High Temperature Corrosion Resistance Of Alloy N07740 In Solar And Low Emission Ultrasupercritical Power Generation
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High Temperature Corrosion Resistance Of Alloy N07740 In Solar And Low Emission Ultrasupercritical Power Generation

Product Number: 51322-17945-SG
Author: Stephen McCoy, John deBarbadillo, Brian Baker, Mark Anderson
Publication Date: 2022
$20.00

In recent years, solar energy technology has received particular emphasis in the interest of reducing CO2 emissions.  Concentrated solar power (CSP) technology received an initial boost from the installation of nine parabolic trough-based electricity-generating systems totaling 354 megawatts of capacity in the 1980’s.  Solar One, operational in 1982 and supported by the DOE and an industrial consortium, illustrate utilization of a circulating heat transfer fluid to produce steam to drive a turbine generating electricity.  Solar Two in 1996 demonstrated energy storage so that solar power could be generated during the night.1  In the ensuing decades, additional capacity has increasingly been installed worldwide, comprised primarily of both parabolic trough and central tower CSP technologies,  As of 2019, global installed capacity totaled 6.2 GW, with an additional 21 GWh planned of installed thermal energy storage (TES) comprised primarily of molten salts.   
Picture for Effect of Thiosulfate on the Pitting Corrosion of Nickel Base Alloys in Chloride Solutions
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Effect of Thiosulfate on the Pitting Corrosion of Nickel Base Alloys in Chloride Solutions

Product Number: 51317--9036-SG
ISBN: 9036 2017 CP
Author: Mariano Kappes
Publication Date: 2017
$20.00

Pitting corrosion susceptibility of UNS N06600, UNS N06690 and UNS N08800 was studied in pure 1 M NaCl with and without Na2S2O3 additions. The alloys were tested in the as-received (AR), solution annealed (SA) and aged (SA + A) conditions.
Picture for RP0187-Design Considerations for Corrosion Control of Reinforcing Steel in Concrete-HD1990
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RP0187-1990, Design Considerations for Corrosion Control of Reinforcing Steel in Concrete

Product Number: 53063-HD1990
Author: NACE
Publication Date: 1009
$179.00

Controlling corrosion of proposed atmospherically exposed reinforced concrete structures. Causes of and control methods for the corrosion of reinforcing steel in Portland cement concrete structures. Historical Document 1990
Avoiding Corrosion in Desalination Plants

Avoiding Corrosion in Desalination Plants

Product Number: 37647-POD
ISBN: 978-1-57590-390-3
Author: Roger Francis
$147.00

This is a print-on-demand (POD) book that will be produced just for you in 2-5 days after your order. It should arrive at your door in about one to two weeks. However, due to supply chain and logistic challenges currently affecting the industry, it may take longer. Allow three weeks for international orders.

Over the past decade, the author, Roger Francis, has looked at some very expensive corrosion failures in desalination plants. Avoiding Corrosion in Desalination Plants explains how to avoid existing corrosion problems and how to avoid them in new builds.

This book looks at corrosion problems specific to multistage flash (MSF), multiple-effect distillation (MED), and seawater reverse osmosis (SWRO) desalination plants, describing their causes, some solutions, and the relative performance of various materials. It gives advice on procuring materials for desalination plants to avoid quality problems.

2019 NACE, 6 x 9" trim size, color, perfect bound, 214 pages
Picture for NACE SP0499-2022, Corrosion Control and Monitoring in Seawater Injection Systems
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NACE SP0499-2022, Corrosion Control and Monitoring in Seawater Injection Systems

Product Number: NACE SP0499-2022
Publication Date: 2022
$109.00

This AMPP standard practice provides guidance in controlling and monitoring for corrosion, bacteria, and water quality to corrosion engineers, field corrosion, production, technical, and operating personnel, and others involved in corrosion control of seawater injection systems. This standard includes descriptions of equipment and practices for controlling and monitoring corrosion in seawater injection systems. This standard does not cover all corrosion monitoring methods including but not limited to: Periodic External UT and Downhole inspection tools.
Combatting Localized Galvanic Corrosion at Bolted Connections in Gravity Sludge Thickeners and Clarifiers in Wastewater Treatment Plants
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Combatting Localized Galvanic Corrosion at Bolted Connections in Gravity Sludge Thickeners and Clarifiers in Wastewater Treatment Plants

Product Number: 51220-269-SG
Author: R. A. Nixon
Publication Date: 2020
$20.00

This paper will describe this commonplace corrosion problem associated with protective coating damage at dissimilar metal bolted connections and present a typical case history. The paper will go on to explain why slotted bolt holes are more susceptible to more aggressive corrosion damage than round bolt holes. In addition, the paper will present successful measures that can be taken to prevent this prevalent problem. 
Picture for Exploratory evaluation of interface effects of cathodic prevention in concrete
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51318-11581-Exploratory evaluation of interface effects of cathodic prevention in concrete

Product Number: 51318-11581-SG
Author: Krittin Rattakham / Alberto A. Sagüés
Publication Date: 2018
$20.00

Experiments on whether an intrinsic (predominantly interfacial effects of polarization) or an extrinsic (predominantly concentration changes due to polarization) mechanism may be dominant in the cathodic polarization of steel in concrete.
Picture for Corrosion Performance of L80-1Cr and L80-3Cr OCTG in High CO2 at Elevated Temperatures
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Corrosion Performance of L80-1Cr and L80-3Cr OCTG in High CO2 at Elevated Temperatures

Product Number: 51313-02753-SG
ISBN: 02753 2013 CP
Author: Amit Kumar
Publication Date: 2013
$20.00

Sweet corrosion of Oil Country Tubular Goods (OCTG) is a major concern in the oil and gas industry. This paper will present the experimental results and discuss the effects of temperature and Chromium content in OCTG on corrosion rate.
Corrosion Control in Petroleum Production, Third Edition

Corrosion Control in Petroleum Production, 3rd Edition

Product Number: 37646-POD
ISBN: 978-1-57590-389-7
Author: Robert J. Franco & Timothy Bieri
$148.00

This is a print-on-demand (POD) book that will be produced just for you in 2-5 days after your order. It should arrive at your door in about one to two weeks. However, due to supply chain and logistic challenges currently affecting the industry, it may take longer. Allow three weeks for international orders.

This greatly updated and expanded third edition of Corrosion Control in Petroleum Production is written for non-experts who have the responsibility for corrosion management of subsurface, surface, and subsea equipment used for producing and processing oil and natural gas.

The book provides an overview and reference on the different corrosion threats, the methods for controlling corrosion, and the establishment of a management system based on risk and continuous improvement.

The authors, Robert Franco and Tim Bieri, have distilled over 80 years of personal experience--as well as the experience from multiple reviewers and contributors--into one comprehensive reference.

Included are hundreds of photographs, figures, and tables to illustrate the practical aspects and essential theory of corrosion control and materials selection.

 2020 NACE, 536 pages, 6 x 9" trim size, perfect bound, color
Picture for Mitigation of Severe Pitting Corrosion Caused by MIC in a CDC Biofilm Reactor
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51317--9604-Mitigation of Severe Pitting Corrosion Caused by MIC in a CDC Biofilm Reactor

Product Number: 51317--9604-SG
ISBN: 9604 2017 CP
Author: Timothy Tidwell
Publication Date: 2017
$20.00

To study the effect of repeated biocide treatments to mitigate microbiologically influenced corrosion (MIC), we used a Center for Disease Control (CDC) biofilm reactor to generate and remediate corrosive biofilms on carbon steel coupons grown from a produced water sample from a salt water disposal (SWD).
Picture for Corrosion Control in Petroleum Production, Third Edition
Available for download

Corrosion Control in Petroleum Production, Third Edition

Product Number: 37646-pdf
ISBN: 978-1-57590-469-6
Author: Robert J. Franco & Timothy Bieri
Publication Date: 2020
$145.00

This greatly updated and expanded third edition of Corrosion Control in Petroleum Production is written for non-experts who have the responsibility for corrosion management of subsurface, surface, and subsea equipment used for producing and processing oil and natural gas. It provides an overview and reference on the different corrosion threats, the methods for controlling corrosion, and the establishment of a management system based on risk and continuous improvement.
Picture for Corrosion Control In Water Injection Pipelines
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Corrosion Control In Water Injection Pipelines

Product Number: 51322-17692-SG
Author: Jonathan Marsh
Publication Date: 2022
$20.00

Dubai Petroleum (the Operator) operates five offshore oil fields in the Emirate of Dubai (Fateh, South West Fateh, Falah, Jallilah and Rashid), in addition to various onshore gas production, storage, distribution and import facilities, and LNG import facilities. The assets within these offshore fields consist of approximately 80 platforms of various sizes, comprising central bridge linked processing facilities in Fateh and South West Fateh, and outlying normally unmanned wellhead production platforms. These platforms are linked by a network of over 150 subsea pipelines, of which over 30 are presently operational sea water injection pipelines.
Picture for Effect of Backing Gas Composition on Corrosion Behavior of Conventional Duplex Stainless Steel Weldments
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Effect of Backing Gas Composition on Corrosion Behavior of Conventional Duplex Stainless Steel Weldments

Product Number: 51321-16598-SG
Author: Ricardo Hernández Soto/ Abdullah M. Al-Rumaih
Publication Date: 2021
$20.00
Picture for Influence of Ultrasonic Nanocrystal Surface Modification on the Corrosion and Stress Corrosion Crack
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Influence of Ultrasonic Nanocrystal Surface Modification on the Corrosion and Stress Corrosion Cracking Behavior of Welded Joint in District Heating Pipe

Product Number: 51317--8953-SG
ISBN: 8953 2017 CP
Author: Yong-Sang Kim
Publication Date: 2017
$20.00

Stress corrosion cracking behavior measured by slow-strain rate tests with accelerated anodic & cathodic reactions. Results indicated the UNSM treatment has a significant effect on the corrosion condition. No effect appeared in the hydrogen embrittlement.
Picture for Cymbopogon citratus and Na2Cr2O7 Effects on Concrete Steel-rebar Corrosion in Industrial/Microbial Simulating-Environment
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51318-10808-Cymbopogon citratus and Na2Cr2O7 Effects on Concrete Steel-rebar Corrosion in Industrial/Microbial Simulating-Environment

Product Number: 51318-10808-SG
Author: Joshua Olusegun OKENIYI / Abimbola Patricia Idowu POPOOLA / Elizabeth Toyin Okeniyi
Publication Date: 2018
$20.00

Electrochemical measurements were obtained from steel-reinforced concrete samples immersed in 0.5 M H2SO4 medium, for simulating industrial/microbial environment, to assess the corrosion-inhibition effects of two admixtures.
Picture for Corrosion Risk Assessment Of Aging Plant In The Down Stream Petroleum Sector
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Corrosion Risk Assessment Of Aging Plant In The Down Stream Petroleum Sector

Product Number: 51322-17858-SG
Author: Muazu Mohammed
Publication Date: 2022
$20.00

This paper shares experiences and challenges of corrosion risk assessment in the down-stream petroleum industries and simplify ways of managing corrosion through effective corrosion assessment regime.
Picture for 10278 A Parametric Study of Sour Corrosion of Carbon Steel
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10278 A Parametric Study of Sour Corrosion of Carbon Steel

Product Number: 51300-10278-SG
ISBN: 10278 2010 CP
Author: Wei Sun, Dylan V. Pugh, Stephen N. Smith, Shiun Ling, Jorge L. Pacheco and Robert J. Franco
Publication Date: 2010
$20.00

A parametric study of sour corrosion was conducted and is presented in this paper to provide a better understanding of corrosion in sour gas environments. Various parameters that are known to affect the corrosion rate were evaluated and their impacts on corrosion rate are discussed.

 
Picture for Predicting Corrosion of Successive Feeds in Distilling Units - An Experimental Approach
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Predicting Corrosion of Successive Feeds in Distilling Units - An Experimental Approach

Product Number: 51324-20668-SG
Author: Gheorghe Bota; Ishan Patel; Peng Jin; David Young
Publication Date: 2024
$40.00
Cheap heavy crudes become attractive for oil refineries to increase their benefit margins but the corrosivity of heavy crudes compels the refinery engineers to blend them with the more expensive light sweet crudes. Crude oil blends with complex composition including organo-sulfur compounds, fatty acids, nitrogen and chlorine compounds become corrosive when processed at high temperatures due to these reactive species. Therefore, maintaining corrosion control is a constant effort in oil refineries, and it involves the use of dedicated corrosion models combined with specific experimental lab procedures and methods. This work is presenting the practical application of a lab testing procedure used for predicting the high temperature corrosivity of different crude fractions that were run successively for different time periods in a specific “flow-through” apparatus. The testing procedure consists of two distinct phases performed in the same apparatus, at the same temperature, and for different time durations. During the first phase of the test, scales are formed using a distilling fraction on metal samples and further, in the second test phase, these preformed scales on samples are exposed without interruption to a different distilling fraction. Thus, the two successive test phases, each using a different distilling fraction, are associated with the “changing feeds” in the distilling tower. Corrosive effects are evaluated by sample weight loss measured in successive fraction tests and in separate tests performed with each of the selected fractions. Experimental results are compared to predictions of a corrosion model for sulfidation and naphthenic acid corrosion.
Picture for Inhibiting Nucleation Corrosion in Liquid Hydrocarbons
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Inhibiting Nucleation Corrosion in Liquid Hydrocarbons

Product Number: 51324-21232-SG
Author: Moshood Adewale; Hitesh Bagaria; Nimeshkumar Patel; Tatiana Barbosa; Osvaldo Antonio Heredia Cancino
Publication Date: 2024
$40.00
Dewpoint corrosion is a well-known phenomenon in flue gas stacks and refinery overheads, where fine water droplets condense from the vapor upon cooling, and the acid gases in the vapors diffuse into water droplets to form a highly corrosive low pH liquid. We have identified a similar mechanism in hydrocarbon liquids, which we call as “nucleation corrosion” (C2023-19463). Liquid hydrocarbons often have dissolved water (DW), which does not promote corrosion even in the presence of corrosive species (e.g., organic acids, H2S). Upon cooling, the DW nucleates as nanometer-sized water droplets and acids present in the liquid partition into the water droplets decreasing pH to cause aggressive nucleation corrosion. In this study the methods to mitigate nucleation corrosion are investigated with an emphasis on studying the impact of different types of chemical inhibitors on this newly discovered mechanism. An interesting example of the impact of the test method on inhibitor selection is shown. Finally, a case study highlighting nucleation corrosion in a refinery distillation overhead reflux line is presented.
Introducing The Nation’s First Bachelor of Science Degree in Corrosion Engineering and the National Center for Education and Research on Corrosion and Materials Performance
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“Introducing The Nation’s First Bachelor of Science Degree in Corrosion Engineering and the National Center for Education and Research on Corrosion and Materials Performance

Product Number: 41211-627-SG
Author: Sue Louscher
Publication Date: 2011
$20.00

By establishing a holistic program that incorporates workforce training, the nation's first baccalaureate degree in Corrosion Engineering, and world-class research in corrosion and materials performance; The University of Akron (UA) is establishing a program that will create a pipeline of critical resources that will ensure that future investments in equipment and infrastructure revitalization are designed and implemented in a manner that minimizes the impact of corrosion and thus reduces the life-cycle cost to sustain those assets. 
Picture for Electrochemical Corrosion Analysis Of Stainless Steels In LALM Pyrolysis Bio-Oil With Organic Corrodents
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Electrochemical Corrosion Analysis Of Stainless Steels In LALM Pyrolysis Bio-Oil With Organic Corrodents

Product Number: 51322-17759-SG
Author: Jiheon Jun, Dino Sulejmanovic, James R. Keiser, Michael P. Brady, Michael D. Kass
Publication Date: 2022
$20.00

Biomass-derived pyrolysis oils (bio-oils) are recognized as a renewable energy source that could
aid in the reduction of fossil fuel use. Bio-oils exhibit higher corrosivity to common ferrous alloys because the oils contain organic acids and water. A series of corrosion studies were previously performed to determine the corrosion rates of ferrous alloys exposed in bio-oils for a quantitative evaluation of the material compatibility. The key information from these previous studies is that ferrous alloys with more Cr, Ni, and Mo are needed for compatibility with bio-oils.
Picture for Corrosion Behavior of Powder Metallurgical Cobalt-Based Alloys in Hydrochloric Acid
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51318-11155-Corrosion Behavior of Powder Metallurgical Cobalt-Based Alloys in Hydrochloric Acid

Product Number: 51318-11155-SG
Author: Jinhui Ding / Yuexiang Zhang
Publication Date: 2018
$20.00

Cobalt-based alloys containing Cr-Ni-Mo-W-Co ingredients were produced and their corrosion behavior in hydrochloric acid was investigated using potentiodynamic polarization (PDP) curves, electrochemical impedance spectroscopy (EIS) measurements and immersion corrosion tests.
Picture for Factors In Galvanic Corrosion Between Steel And Iron Sulfides In Acidic Solutions
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Factors In Galvanic Corrosion Between Steel And Iron Sulfides In Acidic Solutions

Product Number: 51322-17827-SG
Author: Payman Sharifi Abdar, Bruce Brown, Srdjan Nesic
Publication Date: 2022
$20.00

H2S corrosion, also known as sour corrosion, is one of the most researched types of metal degradation in oil and gas transmission pipelines requiring a wide range of environmental conditions and detailed surface analysis techniques. This is because localized or pitting corrosion is known to be the main type of corrosion failure in sour environments which caused 12% of all oilfield corrosion incidents according to a report from 1996. Therefore, control and reduction of this type of corrosion could prevent such failures in oil and gas industries, and significantly enhance asset integrity while reducing maintenance costs as well as eliminating environmental damage.

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