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14111 total products found.
Picture for Non-metallic Applications in Oil & Gas Industry
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Non-metallic Applications in Oil & Gas Industry

Product Number: MPWT19-14383
Author: Mohamed Al Ghosain, Ali Azman Faheem, Ullah Mohamed, Zohair Zaki
Publication Date: 2019
$0.00

Corrosion, either internal or external, along with other types of defects on pipelines eventually lead to leaks without proper treatment. This gives rise to several issues, including environmental and safety hazards, and in case of pipe leaks in a plant, a loss of the efficiency of the process or, ultimately, failure of the process. Replacing the corroded pipelines (piping) can be difficult, costly and time consuming especially for plant. A required shutdown causes major economic loss. Thus, instead of a replacement of the defected pipelines, the installation of online repair is a better option.
Repairs of pipelines include metallic and non-metallic repairs. Metallic repairs generally require welding or hot works which is not suitable for online repair of pipes containing hydrocarbons. In such cases the use of non-metallic composite repairs is the optimum solution. A non-metallic composite repair system is a system used to reinforce structures using a fiber equipped with a thermoset epoxy system. The epoxy system consists of a hardener and a resin which, after mixing, become solid through a polymerization reaction after a short duration of time, a process that is called curing. Depending on the temperature, the duration of time changes in an inverse relation. The higher the temperature, the smaller the duration of time needed for curing. This system can be used to reinforce pipelines with both external and internal corrosion and it can be used on Straight Pipes, Tees, Elbows, Flanges and weld joints. The repair system can also be installed online without the need for a shutdown in a short amount of time and a small requirement of labor intensity, making it cost effective. It is also environmentally friendly. In this paper we are going to present cases that were resolved by our company that demonstrate how successful these non-metallic composite repairs are and how diverse their applications can be
Picture for Industrial Coating Application (ICA) Module 4 - Liquid Coating Application_ALL

Industrial Coating Application (ICA) - Module 4: Liquid Coatings Application_ALL

Product Number: ICA Mod 4
$425.00
Picture for 97102 SCC MITIGATION STRATEGIES IN HOT
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97102 SCC MITIGATION STRATEGIES IN HOT WATER

Product Number: 51300-97102-SG
ISBN: 97102 1997 CP
Author: Peter L. Andresen
$20.00
CORROSION PREVENTION VIA GENERATION OF IRONMAGNESIUM PHOSPHATE DEPOSITION COATING
Available for download

CORROSION PREVENTION VIA GENERATION OF IRONMAGNESIUM PHOSPHATE DEPOSITION COATING

Product Number: 51218-167-SG
Author: Rebekah Wilson, Brooke Divan
Publication Date: 2018
$20.00

The DoD functions under a wide array of infrastructure to include, but not limited to, ships, tanks, combat vehicles and buildings. Due to the nature and need of the building materials, these are always at risk for corrosion, causing the infrastructure to literally crumble. This obviously puts Soldiers in harm’s way due to issues such as weapon misfiring and structural failures. 
Picture for Corrosion Investigations of Copper Alloys and Cast Stainless Steel Used for Drinking Water Applications
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Corrosion Investigations of Copper Alloys and Cast Stainless Steel Used for Drinking Water Applications

Product Number: 51324-20723-SG
Author: Luca Blanka Boncz; Jens Lykke Sørensen; Lotte Holmegaard; Morten Stendahl Jellesen
Publication Date: 2024
$40.00
Brass alloys are considered corrosion-resistant in potable water. However, chloride, disinfectants, and high flow rates were reported to weaken pipes, leading to leaks and damage. The degradation of copper alloys causes concern as metal ion release may affect water taste and human health in high concentrations. Therefore, materials with improved flow corrosion properties and increased corrosion resistance are needed. Failure investigations were performed on C52100 brass domestic water flowmeters by visual inspection, microstructural analysis with scanning electron microscope energy dispersive X-ray spectroscopy (SEM-EDS), and X-ray diffraction (XRD). The failure is mostly initiated by high local flow rates causing erosion corrosion attacks with dezincification. The corrosion behavior of C52100 (phosphor bronze), C89520 (Se-Bi brass), and S31600 (stainless steel) was investigated and compared to C27453 (brass) in drinking water with varying contents of chloride, ammonia, and chlorine by potentiodynamic polarization curves and long-term immersion tests. Furthermore, flowmeters (made of C27453 and C89520) were installed in a flow test setup to investigate flow induced conditions in a laboratory environment with aggressive drinking water. Immersion tests, flow tests, and potentiodynamic investigations show that brass corrodes at a higher rate than bronze, Se-Bi brass, and stainless steel in such environments.
Picture for 01577 PAINT AND COATING REMOVAL TECHNOLOGIES:
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01577 PAINT AND COATING REMOVAL TECHNOLOGIES: PAST, PRESENT AND FUTURE

Product Number: 51300-01577-SG
ISBN: 01577 2001 CP
Author: Vinod S. Agarwala, Krishnan Rajeshwar
$20.00
Picture for 00367 STRESS ASSISTED PIT AND FISSURE COALESCENCE
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00367 STRESS ASSISTED PIT AND FISSURE COALESCENCE DURING EARLY STAGES OF STRESS CORROSION CRACKING IN AI-Li-Cu ALLOY AA2096

Product Number: 51300-00367-SG
ISBN: 00367 2000 CP
Author: Brian J. Connolly and John R. Scully
$20.00
Picture for Performance of Organic Corrosion Inhibitors on Carbon Steels and High Alloys in 4M Hydrochloric Acid
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51315-5893-Performance of Organic Corrosion Inhibitors on Carbon Steels and High Alloys in 4M Hydrochloric Acid

Product Number: 51315-5893-SG
ISBN: 5893 2015 CP
Author: Evgeny Barmatov
Publication Date: 2015
$20.00
Picture for 08RTS02 Assessment of Corrosion Based Failure in Stainless Steel Containers Used for the Long-term S
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08RTS02 Assessment of Corrosion Based Failure in Stainless Steel Containers Used for the Long-term Storage of Plutonium Based Salts

Product Number: 51300-08RTS02-SG
ISBN: 08RTS02 2008 CP
Author: R. Lillard, D. Kolman, M. Hill, M. Prime, D. Veirs, L. Worl, and P. Zapp
Publication Date: 2008
$20.00
Picture for 09433 Corrosion Monitoring in Hanford Nuclear Waste Storage Tanks, Design and Data From the 241-AN-1
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09433 Corrosion Monitoring in Hanford Nuclear Waste Storage Tanks, Design and Data From the 241-AN-102 Multi-Probe Corrosion Monitoring System

Product Number: 51300-09433-SG
ISBN: 09433 2009 CP
Author: Alan R. Hagensen, Glenn L. Edgemon, Kayle D. Boomer, Vanessa S. Anda and Kelly G. Carothers
Publication Date: 2009
$20.00
Picture for 08638 Flow Dependancy of Sweet and Sour Corrosion of Carbon Steel Downhole Production Tubing in Khuf
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08638 Flow Dependancy of Sweet and Sour Corrosion of Carbon Steel Downhole Production Tubing in Khuff Gas Wells

Product Number: 51300-08638-SG
ISBN: 08638 2008 CP
Author: Ho Jin Choi and Hassan A. Al-Ajwad
Publication Date: 2008
$20.00
Picture for AMPP SP21484-2023, Splash Zone Site-Applied Wrap Corrosion Protection Systems
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AMPP SP21484-2023, Splash Zone Site-Applied Wrap Corrosion Protection Systems

Product Number: AMPP SP21484-2023
Publication Date: 2023
$109.00

This standard is for use by those responsible for the management of marine structures. They will be able to use it to establish the minimum requirements of the Site-Applied Wrap Corrosion Protection Systems they are considering for the protection of the submerged zone and splash zone of shore based marine metallic structures, either at the pointof new construction or during refurbishment or maintenance of existing structures. This standard is not intended to provide the minimum requirements for offshore oil and gas platforms and other similar structures of the offshore oil and gas industry. This standard may be used to provide the minimum requirements for estuarine, paludal, riverine, great lake structures or similar. The Site-Applied Wrap Corrosion Protection Systems in accordance with this standard are considered suitable for further protection by means of cathodic protection.
The Corrosion of Duplex Stainless Steels: A Practical Guide for Engineers

The Corrosion of Duplex Stainless Steels: A Practical Guide for Engineers

Product Number: 37636-POD
ISBN: 978-1-57590-369-9
Author: Roger Francos
$150.00

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.

In The Corrosion of Duplex Stainless Steels, author Roger Francis reviews various duplex alloy compositions, mechanical properties, and design stresses for vessels and pipes to various codes. He also covers the basics of welding duplex alloys, both to themselves and to other alloys, and their corrosion resistance.

Of most importance, the book looks at a variety of types of corrosion that may affect DSSs in service, presenting the available data and, in some cases, how to avoid problems.

2018 NACE, 256 pages, 8 x 10" trim size, color, perfect bound.

 

Corrosion of Duplex Stainless Steels

Download the free white paper summary of this title to see specific areas of focus and discussion

Picture for 03248 ENVIRONMENTAL EVALUATION OF A CADMIUM
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03248 ENVIRONMENTAL EVALUATION OF A CADMIUM REPLACEMENT COATING FOR USE IN A MARINE ENVIRONMENT

Product Number: 51300-03248-SG
ISBN: 03248 2003 CP
Author: David A. Shifler, Regis K. Conrad, Andrew D. Sheetz, Harry L. Archer, Jr.
Publication Date: 2003
$20.00

Because of its hardness, dimensional tolerance and resistance to hydrogen, cadmium plating has been used to protect steel components in marine environments.  However, Cadmium is thought to be toxic and a search is on for an alternative. In this paper,  cadmium and zinc-nickel plating/coating were compared in water immersion, temperature cycling, rain, humidity, and salt fog testing.
Cathodic Nanocoating Technology for Corrosion Control of Steel Structures
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Cathodic Nanocoating Technology for Corrosion Control of Steel Structures

Product Number: 41211-613-SG
Author: Todd Hawkins
Publication Date: 2011
$20.00

In 2000 the National Science Foundation estimated that the market for nanotechnology products will be over one trillion US dollars by 2015 and that the industry would employ over 200 million workers. These numbers have been subsequently quoted from funding applications to government policy documents, but at the halfway point many of the revolutionary and disruptive technologies predicted have failed to emerge. Indeed, seven years on from the inception of the National Nanotechnology Initiative, there appears to be little sign of a nanotechnology-based industry, although significant amounts of R&D are being undertaken by various industries. 
Picture for 97528 RAPID DETECTION OF MICROBIOLOGICALLY
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97528 RAPID DETECTION OF MICROBIOLOGICALLY INFLUENCED CORROSION IN SHIPBOARD EQUIPMENT BY ON-LINE MONITORING OF BIOFILM FORMATION

Product Number: 51300-97528-SG
ISBN: 97528 1997 CP
Author: George J. Licina, George Nekoksa
$20.00
Picture for 96436 ALLOYING EFFECTS ON DISSOLUTION RATE
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96436 ALLOYING EFFECTS ON DISSOLUTION RATE OF CREVICE CORROSION FOR AUSTENITIC STAINLESS STEELS IN 3% NaCl SOLUTION AT 80°C

Product Number: 51300-96436-SG
ISBN: 96436 1996 CP
Author: Peter Chen, Tadashi Shinohara, Shigeo Tsujikawa
$20.00
Picture for Recent Failures of 2205 Duplex Stainless Steel in FGD Scrubbers - Could They Have Been Avoided?
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51317--9747-Recent Failures of 2205 Duplex Stainless Steel in FGD Scrubbers - Could They Have Been Avoided?

Product Number: 51317--9747-SG
ISBN: 9747 2017 CP
Author: Bud Ross
Publication Date: 2017
$20.00

Over 5 years, 70 to 80 FGD scrubber units have exhibited corrosion problems. Many were after only a few months of service. This paper will provide an overview of readily available technical information in the published literature and past experience that could have been used to minimize corrosion problems in these FGD units.

 
Picture for 08254 External Pitting and Crevice Corrosion of 316L Stainless Steel Instrument Tubing in Marine Env
Available for download

08254 External Pitting and Crevice Corrosion of 316L Stainless Steel Instrument Tubing in Marine Environments and Proposed Solution

Product Number: 51300-08254-SG
ISBN: 08254 2008 CP
Author: A. Okeremi and M. Simon-Thomas
Publication Date: 2008
$20.00
Picture for 09512 Correlation of Electrochemical, ASTM Test and Metallographic Annalyses in the Corrosion Behavi
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09512 Correlation of Electrochemical, ASTM Test and Metallographic Annalyses in the Corrosion Behavior of 5XXX Aluminum Alloys

Product Number: 51300-09512-SG
ISBN: 09512 2009 CP
Author: Robert Ruedisueli and Elissa Bumiller
Publication Date: 2009
$20.00
Picture for Case History on the Selection of Materials in a Bulk Handling Chemical Facility at Partitioned Zone
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Case History on the Selection of Materials in a Bulk Handling Chemical Facility at Partitioned Zone

Product Number: 51317--8967-SG
ISBN: 8967 2017 CP
Author: Tariq Kamshad
Publication Date: 2017
$20.00

This paper reviews corrosion issues encountered as a result of using incompatible construction materials with production chemicals, which eventually lead to multiple failures.
Picture for High Temperature Stable Corrosion Inhibitor Development for Deepwater Applications
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High Temperature Stable Corrosion Inhibitor Development for Deepwater Applications

Product Number: 51321-16470-SG
Author: Larry Chen/Nihal Obeyesekere/Thusitha Wickramarachchi/Jonathan Wylde
Publication Date: 2021
$20.00
Picture for Mechanical, Microstructural And Corrosion Characterization Of Low Binder Containing WC-Co Grades Using A Binderjet Process
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Mechanical, Microstructural And Corrosion Characterization Of Low Binder Containing WC-Co Grades Using A Binderjet Process

Product Number: 51322-17583-SG
Author: Krutibas Panda, Ed Rusnica, Reece Goldsberry, Jerry Domingue, Paul Prichard, Zhuqing Wang
Publication Date: 2022
$20.00

Cemented carbides have been widely used to make parts for wear applications due to the excellent combination of hardness and toughness. Cemented carbides represent a group of composite materials containing hard metal carbides, such as tungsten carbide (WC), bonded by ductile metallic binder agents, such as cobalt (Co), nickel (Ni), or iron (Fe).1 By varying WC grain size, weight fraction of metallic binder, and processing parameters, a wider range of microstructure and mechanical properties can be achieved.
Picture for Evaluation of Impressed Current Cahtodically Protected API 650 Tank Bottoms in the Presence of Vapor
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51316-7600-Evaluation of Impressed Current Cahtodically Protected API 650 Tank Bottoms in the Presence of Vapor Phase Corrosion Inhibitors

Product Number: 51316-7600-SG
ISBN: 7600 2016 CP
Author: KHALIL ABED
Publication Date: 2016
$20.00
Picture for Incorporating Monte Carlo Analysis into a State-of-the-Art Corrosion Prediction System
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Incorporating Monte Carlo Analysis into a State-of-the-Art Corrosion Prediction System

Product Number: 51323-18910-SG
Author: Andrew Simm, Daniel Thomas, Gareth John, Steve Hodges
Publication Date: 2023
$20.00

Over the years there have been several different corrosion modelling software packages developed to provide predicted (estimated) corrosion rates for use in the oil & gas industries. Many are based on the original work of DeWaard & Milliams which provided a best-fit statistical model to corrosion rates measured in flow loop laboratory tests conducted at the IFE (Institutt For Energiteknikk) in Norway ; covering (initially) just partial pressure of CO2, temperature, liquid flow velocity and pH (typically as bicarbonate and dissolved CO2).
Picture for Corrosion Risk Assessment for Reinjection of Aerated Condensate
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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.
Picture for Comparison of Phosphate and 2-Aminoethanol on Scaling and Corrosion in a 10 MPa Class Boiler
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51313-02649-Comparison of Phosphate and 2-Aminoethanol on Scaling and Corrosion in a 10 MPa Class Boiler

Product Number: 51313-02649-SG
ISBN: 02649 2013 CP
Author: Hiroyasu Matsuda
Publication Date: 2013
$20.00
Picture for A Parametric Evaluation of Well Construction Corrosion-Resistant Alloys for Geological Carbon Sequestration
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A Parametric Evaluation of Well Construction Corrosion-Resistant Alloys for Geological Carbon Sequestration

Product Number: 51324-20582-SG
Author: Manuel Marya
Publication Date: 2024
$40.00
A parametric test program involving completion alloys in supercritical CO2 was conducted using both isothermal and non-isothermal cycles in the presence of contaminants (i.e., H2O, NO2, SO2, H2S, H2) above typical impurity limits for carbon capture and sequestration (CCS). The isothermal testing consisted of 4500 psi (310 bar) autoclave tests at 175°F (79°C) with the test materials in supercritical CO2, and optionally, in a NaCl-rich brine in equilibrium; the non-isothermal testing was similar, but included three consecutive cycles with 250°F (121°C) and 70°F (21°C) exposures. Up to ten corrosion-resistant alloys [i.e., 9Cr (UNS K90941), 13Cr (UNS S42000), S13Cr (ISO13680 (1) Type 13-5-2), 15Cr (proprietary), 17Cr (proprietary, 22Cr (UNS S32205), 25Cr (UNS S32750), G3 (UNS N06985), 925 (UNS N09925), 718 (UNS N07718), and 716 (UNS N07716)] were tested for weight loss, pitting, and crevice corrosion. The alloys, known to be more susceptible to environmentally-assisted cracking (EAC), were also evaluated for cracking with ppm-levels impurities (25-to-150 ppmv each), including hydrogen sulfide (H2S). Alloys 22Cr, 25Cr, and API (2) Spec. 6A and Std. 5CRA nickel-based alloys are generally found to be fit-for-service for subsurface CCS. In contrast, the alloys with 9-to-17 wt.% chromium tend to suffer from pitting, which when extensive, has been associated with a case of EAC. For the pitting-resistant alloys under test, neither EAC nor crevice corrosion created major new risks. The introduction of non-isothermal cycles to qualify alloys for CCS has successfully emphasized the dominant effects of condensates, otherwise under-represented, and is suggested for future material testing and qualification programs.
Picture for A Review on Residual Stresses in the Fabrication Domain: Evolution Mechanisms, Quantification Techniques and Treatment Methods
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A Review on Residual Stresses in the Fabrication Domain: Evolution Mechanisms, Quantification Techniques and Treatment Methods

Product Number: MPWT19-14359
Author: Rashed Alhajri, Fahad Alhindas, Yasser Alsubhi, Hatim Alhamdan
Publication Date: 2019
$0.00

Residual stresses are self-equilibrating stresses that exist in materials and structures at the absence of instantaneous application of external loadings. In industrial manufacturing and fabrication processes, such stresses can be prominent and may lead to premature failures if uncontrolled. Such failures can be manifested in many forms including stress corrosion cracking, fatigue cracking or brittle facture. This paper is devoted to providing a comprehensive review on residual stress in the manufacturing and fabrication domain with a greater emphasis on welding based residual stresses. Three residual stress evolution mechanisms will be evaluated covering deformation driven stresses during manufacturing, thermally driven during welding and surface modifications such as grinding, carburizing and plating. In welding processes, the residual stresses in the cooling cycle are characterized using Gleeble testing illustrating the stress profiles as a function of temperature. The effect of residual stresses in welded structures will be discussed covering fatigue performance, brittle fracture and effect on Stress Corrosion Cracking resistance. To ensure residual stresses are effectively measured and quantified, a total of nine (9) destructive, semi-destructive and non-destructive residual stress measurement techniques are evaluated. A comparison and evaluation of four (4) common residual stress mitigation techniques are also discussed covering Ultrasonic Impact Treatment, High Frequency Mechanical Impact, shot peening and Post-weld Heat Treatment. The review discussion extends to four (4) factors towards impacting the residual stress magnitude and distribution covering material properties, welding process and clamping and preheating during welding.
Picture for Evaluation of 316L and 2205 Steels Under Flow Effects in Caustic Environments
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Evaluation of 316L and 2205 Steels Under Flow Effects in Caustic Environments

Product Number: 51317--9158-SG
ISBN: 9158 2017 CP
Author: Bedi Aydin Baykal
Publication Date: 2017
$20.00

To better understand the mechanism of erosion-corrosion, electrochemical tests were performed on UNS G10180, UNS S31603 and UNS S32205, used in the construction of pulp/paper machinery components exposed to caustic environments.
Picture for 98028 WETTABILITY OF STEEL SURFACES AT
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98028 WETTABILITY OF STEEL SURFACES AT CO2 CORROSION CONDITIONS I. EFFECT OF SURFACE ACTIVE COMPOUNDS IN AQUEOUS AND HYDROCARBON MEDIA

Product Number: 51300-98028-SG
ISBN: 98028 1998 CP
Author: G. Schmitt, N. Stradmann
$20.00
Corrosion Management for a Sustainable Future

Corrosion Management for a Sustainable Future

Product Number: 37645-POD
ISBN: 978-1-57590-388-0
Author: Christopher Taylor, Andrea Sanchez Sours
$195.00

NEW!! The editors of Corrosion Management for a Sustainable Future, working in DNV’s Strategic Research and Innovation group at the time, examined facets of the materials lifecycle to help identify strategies that could be undertaken to mitigate the exponential increase in materials extraction and consumption that have characterized the rise of the modern world.

From this activity, a ‘materials stewardship’ strategy was formed, composed of the elements of dematerialization (doing more with less), durability (corrosion and risk management), design for multiple lifecycles, and diversion of waste (recycling and industrial symbiosis).

2022 AMPP, softbound, black & white, 280 pages
Picture for Good Fabrication Stage Practices to Mitigate Risks Associated with Wet H2S Caustic Amine Carbonate Corrosion and Cracking
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51318-10842-Good Fabrication Stage Practices to Mitigate Risks Associated with Wet H2S Caustic Amine Carbonate Corrosion and Cracking

Product Number: 51318-10842-SG
Author: Jigneshkumar J. Desai / Ashik S. Murthy / Cathleen Shargay
Publication Date: 2018
$20.00

Brief descriptions of the mechanisms of common types of corrosion attacks in petrochemical and refinery environments viz. Wet H2S, Caustic, Amine, Carbonate corrosion and cracking.
Picture for Electrochemical Corrosion Behavior of X70 Pipeline Steel in Wall Jet Zone under Jet Impingement at H
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51312-01270-Electrochemical Corrosion Behavior of X70 Pipeline Steel in Wall Jet Zone under Jet Impingement at H

Product Number: 51312-01270-SG
ISBN: 01270 2012 CP
Author: Wei Liu
Publication Date: 2012
$20.00
Picture for Mechanistic Correlations Between Single and Multicomponent Corrosion Inhibitor Blends for CO2 Corros
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Mechanistic Correlations Between Single and Multicomponent Corrosion Inhibitor Blends for CO2 Corrosion Control

Product Number: 51317--9190-SG
ISBN: 9190 2017 CP
Author: Carlos Menendez
Publication Date: 2017
$20.00

Mechanistic information was obtained employing such electrochemical techniques as linear polarization, electrochemical frequency modulation and potentiodynamic polarization while using a rotating cylinder electrode system under CO2 corrosion conditions.
Picture for 06473 Laboratory and Field Corrosion Performance
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06473 Laboratory and Field Corrosion Performance of a High Chromium Alloy for Protection of Waterwall Tubes from Corrosion in Low NOx Coal Fired Boilers

Product Number: 51300-06473-SG
ISBN: 06473 2006 CP
Author: Larry Paul, Gregg Clark, Michael Eckhardt
$20.00
Picture for Variances in Pipeline AC Interference Computational Modelling
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Variances in Pipeline AC Interference Computational Modelling

Product Number: 51319-12985-SG
Author: Gerald Haynes
Publication Date: 2019
$20.00

The AC interference between High Voltage AC (HVAC) power lines and pipelines has been modelled with various software programs all of which have a variety of input data which results in various results and outputs.Important aspects such as the soil resistivity along the pipeline route can have a significant impact on the pipelines coating resistance. This in turn affects both the computed AC voltages and current densities both of which can significantly affect personal safety and corrosion of the pipeline.Therefore the spacing between these field measurements along the pipeline route can have a significant effect on the pipeline integrity. Soil resistivity measurements collected every 1000ft versus every 5280ft (1 mile) can have a dire consequence on the corrosion results and the matter is exacerbated where these soil resistivity measurement values change significantly along the route. The accuracy of the soil resistivity field data relative to the actual routing (wetlands rivers low and high resistivity’s etc.) will also affect the correct placement of the AC Mitigation (grounding) as well as the resistance of the grounding which in turn has a cost implication to the asset owners and/or operators.Other aspects such as the power line LEF/EMF may also be used to “calibrate” the AC Interference especially where load data is absent.This paper addresses the critical importance of collecting adequate data for the AC Interference studies to prevent costly installations and to mitigate the incorrect positioning of AC Mitigation systems due to inadequate information.
Picture for 02519 SURFACE LAYERS ON ALLOYS 600 AND 690...
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02519 SURFACE LAYERS ON ALLOYS 600 AND 690 IN PWR PRIMARY WATER : POSSIBLE INFLUENCE ON STRESS CORROSION CRACK INITIATION

Product Number: 51300-02519-SG
ISBN: 02519 2002 CP
Author: J. PANTER, M. FOUCAULT, J.-M. CLOUE, P. COMBRADE, and B. VIGUIER, E. ANDRIEU
$20.00
Picture for 06173 INTEGRITY ASSESMENT AND MANAGEMENT OF A GAS
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06173 INTEGRITY ASSESMENT AND MANAGEMENT OF A GAS PRODUCTION LINE WITH INTERNAL CORROSION IN A MATURE FIELD

Product Number: 51300-06173-SG
ISBN: 06173 2006 CP
Author: Damodaran Raghu, Bert Pots, Mong-Hang Nguyen and David Amacker
$20.00
Picture for Corrosion Control and Integrity Management of Flare Gas Recovery Units
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Corrosion Control and Integrity Management of Flare Gas Recovery Units

Product Number: MECC23-20160-SG
Author: Mohamed M. Farah; Abdulaziz Al-Qahtani; Ibrahim Zahrani
Publication Date: 2023
$20.00

Gas flaring is often a frequent occurrence in the oil and gas industry, where significant unrecovered gas is flared to the atmosphere with wide ranging negative environmental implications such as increased greenhouse emission, and other pollutants that have negative health implications on local populations. However, recent environmental awareness, drive to lower emission and economic benefits associated with flare gas recovery has seen a shift in flaring practice. The recovery of flared gas reduces noise and thermal radiation, operating and maintenance costs, air pollution and gas emission and reduces fuel gas and steam consumption.
Picture for Numerical Exploration of a Comprehensive Mechanistic CO2 Corrosion Model Part II: Influence of Hydrodynamics and Bulk pH
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Numerical Exploration of a Comprehensive Mechanistic CO2 Corrosion Model Part II: Influence of Hydrodynamics and Bulk pH

Product Number: 51323-19305-SG
Author: Michael Jones, Gregory de Boer, Richard Woollam, Joshua Owen and Richard Barker
Publication Date: 2023
$20.00

It is well known that the hydrodynamics of fluid flow directly influences the corrosion process, as shown
in various experiments utilizing rotating electrodes and flow loops to measure corrosion within
turbulent flow. However, when fluid is flowing through a pipe, there is a phenomenon known as the ‘noslip
condition’ which causes the velocity of the fluid to tend to zero as it reaches the wall. For straight
pipe flow, this follows the ‘universal law of the wall’ (Figure 1) which separates flow into 3 domains: fully
turbulent flow, the buffer layer, and the viscous sublayer (also known as the boundary layer) which is the
being modelled here.
Picture for 96447 ALLOY SELECTION METHODOLOGY AND EXPERIENCES
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96447 ALLOY SELECTION METHODOLOGY AND EXPERIENCES OF THE FGD INDUSTRY IN SOLVING COMPLEX CORROSION PROBLEMS: THE LAST 25 YEARS

Product Number: 51300-96447-SG
ISBN: 96447 1996 CP
Author: D.C. Agarwal
$20.00
Picture for ICCP System for Internal Protection of Monopiles for Offshore Wind Farms
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51318-11120-ICCP System for Internal Protection of Monopiles for Offshore Wind Farms

Product Number: 51318-11120-SG
Author: Torsten Krebs
Publication Date: 2018
$20.00

A solution to significantly reduce the internal corrosion of internal areas of offshore monopiles using a highly sophisticated ICCP system. Other technical, electrochemical and installation challenges in of such an ICCP system in confined spaces.

 
Picture for 01368 MEASURING CORROSION RATE OF TYPE 304
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01368 MEASURING CORROSION RATE OF TYPE 304 STAINLESS STEEL IN SUBCRITICAL AND SUPERCRITICAL AQUEOUS SOLUTIONS VIA ELECTROCHEMICAL NOISE ANALYSIS

Product Number: 51300-01368-SG
ISBN: 01368 2001 CP
Author: D.D. Macdonald, X.Y. Zhou, S.N. Lvov, X.J. Wei, and L. G. Benning
$20.00
Picture for Validation of an Optimized qPCR Workflow for MIC Risk Identification and Oilfield Microbial Monitoring
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Validation of an Optimized qPCR Workflow for MIC Risk Identification and Oilfield Microbial Monitoring

Product Number: MECC23-20130-SG
Author: Iain McCulloch; Michael Whitman; Danika Nicoletti; Greg Howard; Neil Sharma; Amy Manning
Publication Date: 2023
$20.00

Microbiologically influenced corrosion (MIC) is a key risk to oil and gas infrastructure and confers great cost to asset owners. The AMPP 2021 IMPACT Canada study, which analyzed the energy, manufacturing, and mining sectors, shows the cost of corrosion in Canada is roughly $51.9 billion per year. To break this down further, MIC is estimated to make up roughly 20% of all corrosion which is roughly $10.4 billion in Canada alone, each year.
Picture for On-Line Real-Time Corrosion Monitoring Techniques Under Co2 - Brine Environment – Comparative Study
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On-Line Real-Time Corrosion Monitoring Techniques Under Co2 - Brine Environment – Comparative Study

Product Number: 51317--9040-SG
ISBN: 9040 2017 CP
Author: Hui Li
Publication Date: 2017
$20.00

 Injection water/brine handling systems are important elements of the oil & gas field operations. This comparative study offers insights relevant to accuracy, sensitivity and responsiveness of different corrosion monitoring techniques in brine environment.

 
Picture for Case Study on Corrosion under Coating Sleeves after Strain Gauges Installed on Pipeline in Alberta
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51316-7709-Case Study on Corrosion under Coating Sleeves after Strain Gauges Installed on Pipeline in Alberta

Product Number: 51316-7709-SG
ISBN: 7709 2016 CP
Author: Michael Crutchley
Publication Date: 2016
$20.00
Picture for 04565 Influence of the Identity of Surface Films
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04565 Influence of the Identity of Surface Films on Stress Corrosion Cracking of 304 Stainless Steel in BWRs and Alloy 600 in PWRs

Product Number: 51300-04565-SG
ISBN: 04565 2004 CP
Author: Todd Mintz, Christopher M. Kumai, and Thomas M. Devine, University of California Berkeley
$20.00

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