AMPP Store - Products tagged with 'oxygen'

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03269 Observations of Corrosion of Electric Resistance Welded Galvanized Steel Pipe in Domestic Potable Water

Product Number: 51300-03269-SG

ISBN: 03269 2003 CP

Author: Adrian J. Mac Nab

Publication Date: 2003

$20.00

Information from inspection and analysis of electric resistance welded galvanized steel pipe after service in residential water systems has resulted in a compilation of observations concerning the development and severity of corrosion leading to failure.

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07663 The Effect of Oxygenated Methanol on Corrosion in Sour Wet Gas Environments

Product Number: 51300-07663-SG

ISBN: 07663 2007 CP

Author: Neil Park, Sherif Maksoud, Lara Morello, and Jennifer E. Wong

Publication Date: 2007

$20.00

This paper studies the effect of oxygen in methanol on the structures and growth kinetics of iron sulfide scales. Gravimetric weight analysis was used to evaluate the corrosion mechanisms and rates. Scanning Electron Microscope/ Energy Dispersive X-ray Spectrometry (SEM/EDX), Optical Microscope and X-ray Diffraction (XRD) were used to analyze the scale.

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11120 Sulfur Corrosion Due To Oxygen Ingress

Product Number: 51300-11120-SG

ISBN: 2011 11120 CP

Author: Joseph Boivin and Scott Oliphant

Publication Date: 2011

$20.00

Case histories are presented where Oxygen ingress has led to Sulfur corrosion failures in pipelines and downhole equipment.

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51316-7188-Failure Analysis and Investigation Methods of Boiler Tubes Corrosion/Case Study

Product Number: 51316-7188-SG

ISBN: 7188 2016 CP

Author: hajatolah almasi

Publication Date: 2016

$20.00

The purpose of this study is to investigate the effect of amount of oxygen on corrosion rate of steam loop. Consequently, to eliminate failure, more effective steam quality monitoring concept is recommended.

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51318-11142-Weld preferential high temperature sulfidation

Product Number: 51318-11142-SG

Author: Matthieu Devallée / Xavier Roumeau / Francois Dupoiron

Publication Date: 2018

$20.00

Very different corrosion behavior was observed between adjacent welds. This paper describes the investigation to identify the corrosion mechanism, trying to understand the influence of filler metal composition and welding parameters.

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98417 TITANIUM AS REACTOR MATERIAL FOR SCWO APPLICATIONS.FIRST EXPERIMENTAL RESULTS

Product Number: 51300-98417-SG

ISBN: 98417 1998 CP

Author: N. Boukis, C. Friedrich, E. Dinjus

Publication Date: 1998

$20.00

Titanium does not show the required mechanical strength for high temperature high pressure applications and it can only be used to form liners for an SCWO apparatus. Therefore, pressure tubes made of alloy 625 were lined with titanium grade 2, Additionally corrosion tests with coupons made of titanium grades 2, 5, 7, 12 and P-C were performed.

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A Review Of Chloride Stress Corrosion Cracking Factors For Austenitic Stainless Steel

Product Number: 51322-17524-SG

Author: Sangeetha Rao

Publication Date: 2022

$20.00

This paper will identify and document how these different factors affect the susceptibility of austenitic stainless steel to Chloride-Stress Corrosion cracking based on a review of currently available literature. A review of current industry best practices and a review of how the Oxygen content, the pH and application of stress relief affects Chloride-Stress Corrosion Cracking will be documented and presented.

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Corrosion Of Wrought And Cast Ni-Fe-Cr-Mo Alloys In High-Temperature Brines And CO2-Rich Supercritical Phases With Oxygen And Hydrogen Sulfide

Product Number: 51322-17882-SG

Author: Manuel Marya

Publication Date: 2022

$20.00

Carbon dioxide capture, utilization, and storage (CCUS) is part of decarbonization solutions to reduce green-house gas emissions, as exemplified by the growing number of capital expenditure projects worldwide.^1-2 In CCUS, the carbon dioxide (CO₂) is consecutively (1) captured at origin, such as power plants and natural gas production sites, (2) separated from other gases and impurities, (3) compressed, (4) transported through pipelines, and finally (5) injected into a storage site such as deleted hydrocarbon wells, saline aquafers, coal beds, underground caverns, or seawater.^1,3 Since the 1970s, specifically the first commercial carbon dioxide flooding in the United States (known as SACROC), carbon dioxide sequestration has been largely discussed in the context of enhanced oil recovery (EOR), not in the newer context of Sustainability. Nonetheless, substantial experience has been drawn from EOR, including for the selection of the right and economical materials.⁴ As reflected by the literature, past materials test programs have rarely given any attention to downhole jewelry alloys compared to tubulars or surface-infrastructure alloys, and consequently the track records for such bar-stock alloys are either inexistent or not readily available. ^5-7 This lack of apparent return-on-experience represents a knowledge gap against the prospect of a safe greenhouse gas control method; needless to say, it also justifies the requirements for reliable well integrity monitoring solutions in carbon dioxide sequestration wells.^8-9

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Corrosion Risk Assessment for Reinjection of Aerated Condensate

Product Number: 51323-19023-SG

Author: Sigit Prabowo, Kelly Melia, Alice Young, Aimee Calibugan, Keith Lichti, Farrell Siega

Publication Date: 2023

$20.00

Nga Awa Purua geothermal power station (NAP) operates a conventional direct contact condenser with recirculating cooling water and forced air cooling towers. The power station is located at the Rotokawa Geothermal field, near Taupō in the North Island of New Zealand. The field supports two power stations: NAP, which was commissioned in 2010 with an installed capacity of 140 MW; and Rotokawa I, a binary power plant which has been in operation since 1997.

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CP of Steel in Soil: Temporospatial pH and Oxygen Variation as a Function of Soil Porosity

Product Number: 51321-16313-SG

Author: Federico Martinelli/Ueli Angst

Publication Date: 2021

$20.00

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Determination Of Oxygen Limits For Corrosion Resistant Alloys (Cras) In Oil & Gas Produced Water Based On Electrochemical Test Methods – Part 1

Product Number: 51322-17939-SG

Author: Roy Johnsen, Marie E. Edvardsen, Martin O. Hestvik, Cristian Torres, Jan Ivar Skar, Marion Duparc, Sven Morten Hesjevik

Publication Date: 2022

$20.00

Corrosion Resistant Alloys (CRAs) have been widely used in oil & gas process systems since the 1980s due to their excellent resistance towards uniform corrosion in aggressive environments such as seawater and produced water containing CO₂, organic acids and/or production chemicals. However, cases of localized corrosion in the form of pitting and crevice corrosion have regularly been observed. As an example, ISO⁽²⁾ 21457 limits the max. operating temperature to 20⁰C for 25 Cr super duplex stainless steel (UNS S32750/760) and 6-Mo austenittic stainless steels (UNS S31254) in chlorinated seawater systems, to avoid crevice corrosion.¹

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Determination Of Oxygen Limits For Corrosion Resistant Alloys (Cras) In Oil & Gas Produced Water Based On Electrochemical Test Methods – Part 2.

Product Number: 51322-17947-SG

Author: Marion Duparc, Roy Johnsen, Jan Ivar Skar, Tov Eivind Saxegaard

Publication Date: 2022

$20.00

Crevice corrosion is a geometrical-dependent type of localized attack that occurs in occluded regions where a stagnant and corrosive electrolyte is in contact with the surface of a passive metal^1,2. Crevices are present in all industrial designs and can lead to major failure since their detection is often challenging^3,4. Main strategies for the prevention and mitigation of crevice corrosion include design awareness and adequate materials selection⁵.

Products tagged with 'oxygen'

Association for Materials Protection and Performance