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14122 total products found.
Picture for Coatings + Proceedings 2021-ALL Papers
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(Coating Formulation) Corrosion Resistance Comparison of Zinc-Rich Epoxy With Reduced Zinc Levels

Product Number: 46-COAT_DEC21
Author: Mary Roley
Publication Date: 2021
$20.00

Zinc-rich coatings have long been known to provide excellent corrosion resistance in highly corrosive environments, in general,inorganic zincs for new construction and organic zincs for maintenance. A recent trend has been toward zinc-rich coatings with reduced levels of zinc dust. An SSPC committee formed to revise SSPC Paint 29, Zinc Dust Sacrificial Primer, Performance Based, to reference performance only, removing reference to minimum zinc dust level.
Picture for 98482 “The Effect of Surface Iron Contamination
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98482 “The Effect of Surface Iron Contamination on the Corrosion Resistance of Alloys in Simulated FGD Environments”

Product Number: 51300-98482-SG
ISBN: 98482 1998 CP
Author: William L Silence, Paul Crook, Jeffrey R. Dillman, F.G. Hodge
$20.00
Picture for UNDER DEPOSIT CORROSION (UDC) IN THE OIL AND GAS INDUSTRY: A REVIEW OF MECHANISMS TESTING AND MITIG
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51312-01379-UNDER DEPOSIT CORROSION (UDC) IN THE OIL AND GAS INDUSTRY: A REVIEW OF MECHANISMS TESTING AND MITIG

Product Number: 51312-01379-SG
ISBN: 01379 2012 CP
Author: Jose Vera
Publication Date: 2012
$20.00
Picture for 98113 EFFECT OF CHROMIUM AND MOLYBDENUM ON
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98113 EFFECT OF CHROMIUM AND MOLYBDENUM ON CORROSION RESISTANCE OF SUPER 13CR MARTENSITIC STAINLESS STEEL IN CO2 ENVIRONMENT

Product Number: 51300-98113-SG
ISBN: 98113 1998 CP
Author: Hisashi Amaya, Kunio Kondo, Hiroyuki Hirata, Masakatsu Ueda, Tomoki Mori
$20.00
Picture for Effect of Chloride Content on The Corrosion Behavior of Ferritic and Austenitic Steels in Molten Sol
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51316-7494-Effect of Chloride Content on The Corrosion Behavior of Ferritic and Austenitic Steels in Molten Solar Salts

Product Number: 51316-7494-SG
ISBN: 7494 2016 CP
Author: Ali Soleimani Dorcheh
Publication Date: 2016
$20.00
Picture for A Review of Experimental Techniques Used for Corrosion Testing in Dense Phase CO2 with Flue Gas Impu
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51314-4383-A Review of Experimental Techniques Used for Corrosion Testing in Dense Phase CO2 with Flue Gas Impurities

Product Number: 51314-4383-SG
ISBN: 4383 2014 CP
Author: Arne Dugstad
Publication Date: 2014
$20.00
Picture for Oxidation Assessment and Impact of Pre-oxidation on Hot Corrosion Behavior of Fe- and Ni-based Alloys
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Oxidation Assessment and Impact of Pre-oxidation on Hot Corrosion Behavior of Fe- and Ni-based Alloys

Product Number: 51324-20991-SG
Author: Haofei Sun; Chentao He; Jing Liu
Publication Date: 2024
$40.00
In this study, we first validated the oxidation performance of Alloy 800 (Fe-based alloy) and 625 (Ni-based alloy) within the temperature range of 700-1000 °C. After 24 hours of oxidation at 1000°C in air, the mass gain is measured as 2.53 and 1.86 mg/cm2 for Alloy 800 and 625, respectively, with their increase rates approximately reaching 6 times compared with those at 900 °C. The main oxidation scale in both two alloys is identified as a Cr2O3 layer with minor NiCr2O4 from 800-1000 °C. A crucial facet of this investigation involved subjecting the alloys to pre-oxidation treatment at 1000 °C for 24 hours, resulting in reduced mass gain during subsequent hot corrosion evaluations with NaCl/Na2SO4 salts at 900°C, particularly noticeable in Alloy 800, where a dense oxidation layer formed. However, cross-sections of both two alloys show a deep penetration by Na and O. These findings reveal the limited protective role of the Cr2O3 layer in augmenting resistance to hot corrosion while offering valuable insights into materials' performance in high-temperature environments and industrial applications.
Picture for Can Micelles Be Used To Expedite And Enhance Laboratory Qualification Testing?
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Can Micelles Be Used To Expedite And Enhance Laboratory Qualification Testing?

Product Number: 51322-17824-SG
Author: Scott Rankin, Andy Osnowski, Emma Perfect
Publication Date: 2022
$20.00

The prevention of internal corrosion remains a significant challenge during the production of oil and gas. The use of film forming corrosion inhibitors is an important and cost-effective means of protecting assets from corrosion. These chemicals operate by forming a protective layer between the corrosive species present in the produced fluids and the pipe surface.
Picture for Underdeposit Corrosion: Investigating Kinetics within Deposits-Covered Artificial Pits
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51318-11055-Underdeposit Corrosion: Investigating Kinetics within Deposits-Covered Artificial Pits

Product Number: 51318-11055-SG
Author: Ahmed Shamso / Nick Laycock / Aboubakr Abdullah / Mary Ryan
Publication Date: 2018
$20.00

In this work, both planar electrode and 1-­dimensional (1D) artificial pit experiments were performed The effects of deposit chemistry and morphology on the electrochemical dissolution behavior are discussed in terms of a transport-­controlled model for pit propagation.

 
Picture for 04678 Effects of Yield Strength, Corrosion
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04678 Effects of Yield Strength, Corrosion Potential, Composition and Stress Intensity Factor in SCC of Stainless Steels

Product Number: 51300-04678-SG
ISBN: 04678 2004 CP
Author: Peter L. Andresen and Martin M. Morra, GE Global Research Center; William R. Catlin, General Electri
$20.00
Picture for Evaluating the Role of SO? and O? on the Corrosion of X65 in Water-Containing Supercritical CO? Envi
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51315-5832-Evaluating the Role of SO? and O? on the Corrosion of X65 in Water-Containing Supercritical CO? Environments

Product Number: 51315-5832-SG
ISBN: 5832 2015 CP
Author: Yong Hua
Publication Date: 2015
$20.00
Picture for Silica Solubility in High Enthalpy Water up to 440°C in the Presence of NaCl
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Silica Solubility in High Enthalpy Water up to 440°C in the Presence of NaCl

Product Number: 51324-21029-SG
Author: Morten Tjelta; Sissel Opsahl Viig
Publication Date: 2024
$40.00
In geothermal energy production, precipitation/scaling and potential plugging of wells is one of the major threats to flow assurance. Mitigation strategies should be considered at the design stage, but to do so knowledge about solubility across a relevant space of temperature, pressure and fluid composition is needed. In hot fluids, silica scaling is often found to be the major concern. Predictive models available in literature give good agreement with experimental values in the region where data are available, but there is limited data available at high temperatures and low pressures, in particular in the presence of salt. This work describes an experimental setup designed to carry out solubility experiments up to 500 °C and 400 bar. A main feature of the setup is the ability to dilute the sample fluid in the hot zone in order to avoid precipitation during sampling. Illustrations are given for how existing phase relations can be used to guide the execution of such high-pressure high-temperature experiments. Results of silica solubility experiments in the presence of NaCl up to 440 °C at 150-350 bar are presented. This work includes data at the steam side pseudocritical line (critical density isochor) where limited data is available in the literature. The experimental concept, with hot zone dilution to avoid precipitation during sampling, can be used to obtain fluid samples as a function of time. Although utilized in the current work for solubility experiments it should be equally applicable to corrosion studies.
Picture for Field Testing of Self-Healing Metallic Coatings for Internal Corrosion Protection of Natural Gas Pipelines
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Field Testing of Self-Healing Metallic Coatings for Internal Corrosion Protection of Natural Gas Pipelines

Product Number: 51323-18857-SG
Author: Zineb Belarbi, Ömer N. Doğan, Patrick Carr, Richard E. Chinn, Julius Samson
Publication Date: 2023
$20.00

Natural gas pipelines are subject to internal corrosion. Internal corrosion of steel pipelines can cause natural gas leakage, leading to wasted energy, explosion hazards, and methane emissions. The U.S. Department of Transport reported numerous case histories of corrosion problems and failures in wet gas pipelines. The National Energy Technology Laboratory (NETL) performed an incident survey from 2010 through 2018 and found that 112 (12%) of these incidents in the U.S. transmission lines were caused by internal corrosion.
Picture for Erosion and Corrosion Assessment of Type 304L Stainless Steel Jumper Removed from Nuclear Waste Transfer Service
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Erosion and Corrosion Assessment of Type 304L Stainless Steel Jumper Removed from Nuclear Waste Transfer Service

Product Number: 51324-20634-SG
Author: Sheewa X. Feng; Jason S. Page
Publication Date: 2024
$40.00
A pipe connection assembly (jumper), fabricated from Type 304L stainless steel, was used to transfer nuclear waste from one tank to other tanks on the Hanford Site. After serving as the routing connection for approximately 11 million liters of tank waste over approximately 11 months, the jumper was removed from service and examined to determine any erosion, pitting, cracking, or other forms of degradation to the jumper. Ultrasonic transducer measurements for wall thickness before and after service at the same selected locations show that there was no measurable wall loss, and no erosion patterns were observed. After the ultrasonic transducer measurement, the jumper section was cut open to expose the inner surface for detailed examination by optical microscopy and scanning electron microscopy. The straight pipe sections at both upstream and downstream locations looked pristine, while discoloring was observed at the two welds, in the heat-affected zone, and in nearby regions joining the elbow and straight pipes. There was no erosion, pitting corrosion, or flow-induced corrosion, nor were there other corrosion mechanisms in evidence except for a crack-like feature observed at the boundary of the base metal and weld. Material etching didn't show alignment of the crack with grain boundaries. Degree of sensitization measurement shows that the weld and heat-affected zone, including the neighboring base, was only slightly sensitized during the manufacturing process. The results suggest that there is very low likelihood that the crack-like feature observed from the weld cross section was the result of stress corrosion cracking. Overall, the jumper performed well during the waste transfer process.
Picture for Evaluating the impact of different families of scale inhibitors on corrosion inhibitor performance
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51318-11505-Evaluating the impact of different families of scale inhibitors on corrosion inhibitor performance

Product Number: 51318-11505-SG
Author: Ana Ferrer / Yolanda De-Abreu / Carol Roach
Publication Date: 2018
$20.00

How different families of scale inhibitors impact corrosion inhibitors performance in the presence of each other. Fundamental properties of both chemistries and how their interaction can be understood at the molecular level.
Picture for 03376 MAKING CREDIBLE CORROSION MEASUREMENTS-
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03376 MAKING CREDIBLE CORROSION MEASUREMENTS - REAL CORROSION, REAL TIME

Product Number: 51300-03376-SG
ISBN: 03376 2003 CP
Author: Dawn C. Eden, Michael S. Cayard, Joseph D. Kintz, Robert A .Schrecengost, Bernard P. Breen, Edward K
$20.00
Picture for 97396 TRANSFERRING CORROSION KNOWLEDGE TO
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97396 TRANSFERRING CORROSION KNOWLEDGE TO COMPUTERS: MODELS FOR PREDICTING CORROSION

Product Number: 51300-97396-SG
ISBN: 97396 1997 CP
Author: Tero J. Hakkarainen
$20.00
Picture for Characterization of Corrosion Inhibitor With Contact Angle Measurement
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Characterization of Corrosion Inhibitor With Contact Angle Measurement

Product Number: 51321-16287-SG
Author: Susumu HIRANO/Ayano YASUI/ Hirotaka MIZUKAMI/Toshiyuki SUNABA
Publication Date: 2021
$20.00
Picture for Corrosion Studies Of An Additive Manufactured Alpha-Beta Ti Alloy
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Corrosion Studies Of An Additive Manufactured Alpha-Beta Ti Alloy

Product Number: 51321-16874-SG
Author: Kishore Venkatesan; Dimitri Conjan; Darren Fraser; David Ritchie; Sri Lathabai
Publication Date: 2021
$20.00
Picture for Effect of Ni on Sulfide Stress Cracking and Stress Grooving in Carbon Steel - Part 1: Constant-load (Dead-weight) Test
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Effect of Ni on Sulfide Stress Cracking and Stress Grooving in Carbon Steel - Part 1: Constant-load (Dead-weight) Test

Product Number: 51324-20715-SG
Author: Taishi Fujishiro; Taro Muraki; Nobuyuki Ishikawa; Daichi Izumi; Takuya Hara
Publication Date: 2024
$40.00
Sulfide stress cracking (SSC) occurs in steel exposed to sour environments. Ni promotes the formation of a crack-like corrosion morphology (so-called stress groove or fissure), which accelerates the SSC; however, the mechanisms underlying fissure formation and growth are not fully understood. In this study, the effects of Ni on SSC and fissures were investigated. Constant-load tests were conducted at various potentials using TS 800 MPa grade steel with and without 1 % Ni addition. The fissures were formed near the corrosion potential on adding Ni. Anodic or cathodic polarization promoted SSC, suggesting that SSC was affected by both active path corrosion (APC) and hydrogen embrittlement (HE) mechanisms. In addition, the fissure shapes and crystal orientations of the microstructure were analyzed to classify the fissures as dissolution (corrosion) or mechanical cracking. Further, characteristic grooves promoted by Ni were confirmed to be APC.
Investigating Specimen Preparation and Cleaning Variables Influencing the NACE TM0208-2018 Jar Test Performance
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Investigating Specimen Preparation and Cleaning Variables Influencing the NACE TM0208-2018 Jar Test Performance

Product Number: 51322-17985-SG
Author: Mitchell Fillbach, Mikel Roe, Daniel Neuburger, Barbara Nygaard, Mahin Shahlari
Publication Date: 2022
$20.00

The NACE TM0208-2018 Jar Test remains an industry-wide recognized standard for evaluating the vapor-inhibiting ability (VIA) of raw materials and finished products to provide off-contact corrosion protection of steel surfaces1. It is particularly useful for comparing the efficacy of different VCI chemistries, as well as for monitoring performance consistency between productions of VCI functionalized materials. 
Picture for Effect of Pre-pits on Localized Corrosion and Sulfide Stress Cracking Resistance of Duplex Stainless Steel UNS S32205 in Upstream Production Environments
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Effect of Pre-pits on Localized Corrosion and Sulfide Stress Cracking Resistance of Duplex Stainless Steel UNS S32205 in Upstream Production Environments

Product Number: 51324-21031-SG
Author: Guru Prasad Sundararajan; V.T. Aruna; Marc E. Wilms; Navashree Surendran
Publication Date: 2024
$40.00
Components in upstream Oil and Gas production such as flowlines, storage vessels or injector pipelines which are made of duplex stainless steel UNS S32205 can undergo localized corrosion such as pitting or crevice corrosion when exposed to oxygen during shutdowns or turn arounds. Such unintended exposure to oxygen is related to poor maintenance or improper preservation and would normally require replacement of equipment. Further use of such pitted components can be considered but requires re-assessment of the pre-corroded material. Open-circuit Potential (OCP) and repassivation potentials (Erp) were measured on UNS S32205 in simulated flowline brines containing 150,000 mg/L Cl- at 110oC with pCO2 of 4.1 bara. The effect of pre-pits on bare and girth welded UNS S32205 was determined by creating artificial pits at OCP under oxygenated brine conditions and then switching the gaseous environment to sweet (CO2) conditions with continuous OCP monitoring. It was found that in oxygen-free CO2 production environments, existing pits did not grow. Sulfide Stress Cracking (SSC) resistance of pre-pitted solution annealed UNS S32205 specimens was determined through Slow Strain Rate Testing (SSRT) and Ripple Load Testing (RLT) at 90oC in concentrated chloride solutions. An electrochemical method was applied to create a single pit on the gauge surface. Comparison of SSRT and RLT results showed that SSRT is too aggressive for determining the pH2S limits. RLT of both pristine and pre-pitted UNS S32205 in concentrated chlorides with up to 0.3 bara pH2S did not show rupture, while selective attack of the ferrite phase was found (pit-depth < 30µm). RLT of notched UNS S32205 specimens were compared to that of pre-pitted specimens. Implications of these results on the limits recommended in ISO15156 / NACE MR0175 are discussed.
Picture for Long-Term Performance of HLP Solution for Mildly Sour HIC Testing
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Long-Term Performance of HLP Solution for Mildly Sour HIC Testing

Product Number: 51317--9129-SG
ISBN: 9129 2017 CP
Author: Daisuke Mizuno
Publication Date: 2017
$20.00

Applicability of High Strength Line Pipe solution has been evaluated by conducting 30-day Hydrogen Induced Cracking (HIC) tests. Reproducibility of corrosion loss and HIC damage was investigated in comparison with those of the conventional solution, specified by NACE TM0284-2016, Solution C.
Picture for Impacts of Impurities SO2 and H2S on Corrosion of sc-CO2 Pipe Steels
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51318-11481-Impacts of Impurities SO2 and H2S on Corrosion of sc-CO2 Pipe Steels

Product Number: 51318-11481-SG
Author: Yimin Zeng / Kaiyang Li / Jingli Lao / Muhammad Arafin
Publication Date: 2018
$20.00

This paper re-examines most public and in-house corrosion data on the effects of six typical impurities to advance the fundamental understanding of how pipeline steels corrode in sc-CO2 environments and identify knowledge gaps for further investigations.
Picture for Use of Large Standoff Magnetometry in Pipeline Integrity Investigations
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Use of Large Standoff Magnetometry in Pipeline Integrity Investigations

Product Number: 51320-14475-SG
Author: C. Onuoha, E. Pozniak, S. McDonnell, V. Shankar, T. Lich, M. Jawed
Publication Date: 2020
$20.00

Large standoff magnetometry (LSM), a novel screening technology, has shown strong industry relevance in several pipeline integrity investigations. LSM is used to detect changes in the magnetic field of a pipeline due to changes in the magnetic susceptibility of steel. These changes are known as inverse magnetostriction (a.k.a. the Villari effect) and occur when a ferromagnetic material (steel) is subjected to mechanical stress, such as the presence of stress on the wall of a pipeline. Geometric anomalies (ovalities, dents, wrinkles), hoop stress, ground and slope movement, bend strain, thermal expansion, cracks, and material defects are examples of potential sources of stress that LSM can detect from aboveground.  

This paper summarizes the use of LSM as a complimentary tool in several pipeline integrity assessments conducted on oil and gas pipelines, in this case, to pinpoint a lost inline inspection pig and to identify dents, cracks, buckles, slope movement, casing ends, unknown valve locations and other pipeline integrity and direct assessment applications. Ongoing development programs and lessons learnt from practical, real-life projects and validations of the technology are presented to demonstrate the effectiveness of LSM for pipeline integrity investigations. 
Picture for 07096 Effect of Variation of Local pH on Stress Corrosion Cracking of Stainless Steels in High Conce
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07096 Effect of Variation of Local pH on Stress Corrosion Cracking of Stainless Steels in High Concentration Brines

Product Number: 51300-07096-SG
ISBN: 07096 2007 CP
Author: Hisashi Amaya, Masakatsu Ueda, Masayuki Sagara, and Kazuhiko Noda
Publication Date: 2007
$20.00
Picture for 00650 A COMPARISON OF CORROSION PROPERTIES BETWEEN
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00650 A COMPARISON OF CORROSION PROPERTIES BETWEEN LEADED BRASS AND UNLEADED BRASSES CONTAINING BISMUTH IN POTABLE WATER SYSTEMS

Product Number: 51300-00650-SG
ISBN: 00650 2000 CP
Author: Jung-Gu Kim, O-Hyun Kwon
$20.00
Picture for A New, Highly Stable Corrosion Resistant Alloy For Severe Oil & Gas And CPI Environments
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A New, Highly Stable Corrosion Resistant Alloy For Severe Oil & Gas And CPI Environments

Product Number: 51321-16555-SG
Author: David S. Bergstrom/ Nacéra Sabrina Meck/ John J. Dunn
Publication Date: 2021
$20.00
Picture for 97036 EVALUATION OF THE CORROSION
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97036 EVALUATION OF THE CORROSION RESISTANCE OF HIGH NITROGEN CONTAINING STAINLESS STEELS IN CHLORIDE AND H2S/CO2 ENVIRONMENTS

Product Number: 51300-97036-SG
ISBN: 97036 1997 CP
Author: Jean-Pierre Audouard, Michel Verneau
$20.00
Picture for 98061 PREVENTING SCALE DEPOSITION IN OIL
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98061 PREVENTING SCALE DEPOSITION IN OIL PRODUCTION FACILITIES: AN INDUSTRY REVIEW

Product Number: 51300-98061-SG
ISBN: 98061 1998 CP
Author: Charles J. Hinrichsen
$20.00
Picture for Effect Of Inhibitor Component On Inhibitor Efficiency - Inhibitor Types And Intensifier-
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Effect Of Inhibitor Component On Inhibitor Efficiency - Inhibitor Types And Intensifier-

Product Number: 51322-17791-SG
Author: Hirotaka Mizukami, Ayano Yasui, Tatsuya Sei, Takashi Ito, Susumu Hirano, Toshiyuki Sunaba, Akiyoshi Kimura, Reiko Ikeda, Mitsuru Uno
Publication Date: 2022
$20.00

A lot of oil and gas facilities face corrosion problems because the production fluid contains some corrosive components represented by CO2. Generally, corrosion inhibitors are used in order to mitigate corrosion problems of tubing and pipeline. Imidazoline is known as one of the active ingredients of corrosion inhibitors and widely used in the oil and gas industries. However, imidazoline-type inhibitor is easily hydrolyzed to amide if water mixes into it.
Picture for Proactive Corrosion Management for Dead-legs
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Proactive Corrosion Management for Dead-legs

Product Number: 51319-13290-SG
Author: Mohammed Al Shahrani
Publication Date: 2019
$20.00

Identifying dead-legs and their related corrosion issues continues to be a challenge in the process industry.This paper presents a comprehensive program for managing corrosion in dead-legs. A three-step methodology is adopted focusing on identification control and monitoring. The identification step entails a comprehensive No Flow/ Low Flow (NFLF) survey. The survey revealed dead-legs in locations where stagnation of oily water containing dissolved carbon dioxide hydrogen sulfide and possibly oxygen at the center bottom portion of pipes associated with stabilization units and NGL compression trains at hydrocarbon operating facility. Consequently the stagnant flow condition significantly contributed to a severe wall thinning that was confirmed by using appropriate Non-Destructive Testing (NDT) technology such as Ultrasonic Testing (UT). The encountered risk was 60% metal loss from the base metal of the defective dead-legs.This corrosion was controlled by establishing a flushing program that is implemented by operation and monitored by inspection team. Additionally for low-flow locations a minimum velocity of 1m/s was maintained where possible. In the last step the effectiveness of the program was monitored by conducting full UT-Scanning every three years and then trending the corrosion rates.Key words: dead-legs management system No Flow/ Low Flow (NFLF) survey Ultrasonic Testing (UT) monitoring strategy
Picture for NACE SP0403-2023
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NACE SP0403-2023, Avoiding Caustic Stress Corrosion Cracking of Refinery Equipment and Piping

Product Number: NACE SP0403-2023
Publication Date: 2023
$109.00

This standard practice is intended to provide guidance to those designing, fabricating, and/or maintaining refinery equipment and piping that are exposed to caustic environments.

Caustic is used in many petroleum refinery applications in a wide range of concentrations and temperatures.  Caustic stress corrosion cracking (SCC) of carbon steel (CS) equipment has been reported in industry since the 1930s, e.g., in riveted steam boilers.  NACE has published guidance for handling sodium hydroxide (NaOH) in the form of a “Caustic Service Chart” since at least the mid-1960s.
Picture for Installed UT Sensors for Continuous Corrosion Monitoring: Better Understanding How Process Changes Influence Corrosion Rates
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Installed UT Sensors for Continuous Corrosion Monitoring: Better Understanding How Process Changes Influence Corrosion Rates

Product Number: 51321-16228-SG
Author: Mitchell Gribi
Publication Date: 2021
$20.00
Picture for High Performance Solutions for the Mitigation or Elimination of Corrosion Under Insulation (CUI)
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High Performance Solutions for the Mitigation or Elimination of Corrosion Under Insulation (CUI)

Product Number: MECC23-20243-SG
Author: Neil Wilds
Publication Date: 2023
$20.00

Corrosion under insulation represents a real threat not just to the assets used in heavy industry / Oil & Gas but also to life. This has been demonstrated through the years with millions of dollars of lost assets/production and unfortunately injuries and deaths. For this reason there have been many documents which have providing guidance not only for design of equipment against CUI but also the pre-qualification/testing of coating systems.
Picture for 05037 Life-Cycle Cost Comparisons of Corrosion
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05037 Life-Cycle Cost Comparisons of Corrosion Protection Methods for Ductile Iron Pipe

Product Number: 51300-05037-SG
ISBN: 05037 2005 CP
Author: David H. Kroon, Corrpro Companies Inc.
Publication Date: 2005
$20.00

Numerous studies and papers have addressed the need and technical merits of various external corrosion protection scenarios for ductile iron pipe. Most recently, a Design Decision Model was developed to select the optimum method of corrosion protection, considering both the likelihood and consequence of failure.

 
Picture for Current Understanding of Corrosion Mechanisms Due to H?S in Oil and Gas Production Environments
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51315-5485-Current Understanding of Corrosion Mechanisms Due to H?S in Oil and Gas Production Environments

Product Number: 51315-5485-SG
ISBN: 5485 2015 CP
Author: Stephen Smith
Publication Date: 2015
$0.00
Picture for Effect of chlorination on corrosion of 90-10 Cu-Ni alloy for ballast water system
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51318-11418-Effect of chlorination on corrosion of 90-10 Cu-Ni alloy for ballast water system

Product Number: 51318-11418-SG
Author: Geunsu Jung / Byoung Young Yoon / Jae Kwang Lee / Chae-Seon Lim
Publication Date: 2018
$20.00

Biofouling and corrosion issues were investigated with experimental methods. 90-10 Cu-Ni samples were prepared and immersed in bottled seawater with various chlorination levels for up to 6 months.
Picture for Corrosion Performances of Modified Grade-Duplex Stainless Steel for Line Pipe Usage in Slightly Sour
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51315-5703-Corrosion Performances of Modified Grade-Duplex Stainless Steel for Line Pipe Usage in Slightly Sour Environment

Product Number: 51315-5703-SG
ISBN: 5703 2015 CP
Author: Masayuki Sagara
Publication Date: 2015
$0.00
Picture for Effect of Surfactants on Inhibition Performance of Corrosion Inhibitors
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Effect of Surfactants on Inhibition Performance of Corrosion Inhibitors

Product Number: 51319-13448-SG
Author: Hejian Sun
Publication Date: 2019
$20.00

Oil and gas industry has gathered extensive and positive experience of applying corrosion inhibitor to control carbon steel corrosion in CO2 and H2S environment. Occasionally asset failures caused by corrosion are observed due to a wrong corrosion inhibitor applied. In many cases overuse or wrongly use of surfactants in a commercial corrosion inhibitor package has attributed to these asset failures. In this paper comprehensive evaluation was conducted to determine what surfactant can enhance corrosion inhibition of different imidazolines. The results show that the water dispersibility of corrosion inhibitor molecules was increased greatly by applying correct surfactants. Some surfactants improve the partition property of inhibitors in aqueous phase. It therefore improves the corrosion inhibition performance. The inhibition performance was measured by both general corrosion inhibition and localized corrosion inhibition. 
Thinning of Inlet Piping to Reactor Effluent Air Condenser [REAC] Of Gas Oil Hydrotreating Unit - Case Study
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Thinning Of Inlet Piping To Reactor Effluent Air Condenser [REAC] Of Gas Oil Hydrotreating Unit - Case Study

Product Number: 51322-18007-SG
Author: Sudharsanan Soundararajan
Publication Date: 2022
$20.00

Gas Oil Hydrotreating Unit uses a catalytic hydrotreating process employing a selective catalyst and a hydrogen-rich gas stream to decompose organic sulfur, oxygen and nitrogen compounds contained in the feed. The products of these reactions are the contaminant free hydrocarbon, along with H2S and NH3. Other Treating reactions include halide removal and aromatic saturation. Reactor effluent is cooled in series of Combined Feed Exchangers followed by REAC for product separation. The reactor effluent system is prone for corrosion and fouling due to salting of NH4HS and NH4Cl. Most of the failure analysis studies and literature available in public domain regarding reactor effluent corrosion deals with the corrosion in the REAC and its outlet piping.
Picture for 98276 SELECTION OF CORROSION INHIBITORS
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98276 SELECTION OF CORROSION INHIBITORS TO CONTROL MICROBIOLOGICALLY INFLUENCED CORROSION

Product Number: 51300-98276-SG
ISBN: 98276 1998 CP
Author: Rupi Prasad
$20.00
Picture for Corrosion-Induced Hydrogen Entry to Steel and a Risk of Hydrogen Embrittlement
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Corrosion-Induced Hydrogen Entry to Steel and a Risk of Hydrogen Embrittlement

Product Number: 51323-19560-SG
Author: Darya Rudomilova, Gerald H. Luckeneder, Tomáš Prošek, Josef Faderl, Andreas Muhr
Publication Date: 2023
$20.00

Hydrogen embrittlement is a process that results in a decrease of the ductility of metals as a result of absorbed hydrogen. Advanced high-strength steels used in the automotive industry are materials that are considered prone to hydrogen embrittlement. Hydrogen can enter the material during steelmaking or processing steps, such as pickling, cleaning, phosphating, and electroplating.
Picture for NACE SP0113-2023, Pipeline Integrity Management: Methods Selection and Implementation
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NACE SP0113-2023, Pipeline Integrity Management: Methods Selection and Implementation

Product Number: NACE SP0113-2023
Publication Date: 2023
$109.00

This standard practice provides guidance on selecting and implementing the Pipeline Integrity Management (PIM) methods (i.e., technologies and processes) to assess and to mitigate threats to pipeline integrity. Predominant threats to pipeline integrity are external corrosion (EC), internal corrosion (IC), stress corrosion cracking (SCC), mechanical damage (first, second, and third party or vandalism), equipment malfunctioning, manufacturing anomalies, construction anomalies, incorrect operations, weather-related, and external forces. The standard is focused on the “selection” and “implementation” of methods and best practices to manage pipeline integrity, but not necessarily on defining all aspects of PIM programs. 
Picture for Swarm S2 - A Wireless, Multi-Channel Ultrasonic Corrosion and Erosion Monitoring Tool
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Swarm S2 - A Wireless, Multi-Channel Ultrasonic Corrosion and Erosion Monitoring Tool

Product Number: 51324-21238-SG
Author: Ali Fatemi
Publication Date: 2024
$40.00
A new EX certified (explosion proof) ultrasonic monitoring tool for integrity management of onshore assets which are subject to corrosion and erosion is presented in this paper. This tool makes it possible to wirelessly perform monitoring with a battery or solar power driven datalogger unit connected to one or several ultrasonic sensors. With internal processing of data in the datalogger, internal storage and wireless communication, the system provides the end user with real-time wall thickness data with micrometer accuracy. Up-to-date data can be directly sent to the control system for review by the decision makers. The datalogger has a modular design which consists of a main body for processing and storing data, a bottom part for transducer connection and a top part for communication. This gives a wide range of possibilities based on the number and type of transducers required and type of communication preferences. We will present different configurations of this product and will show the results of an installation in field and discuss thickness and wall loss data.
Picture for 08642 Practical Applications of Internal Corrosion Predictive Modeling (ICPM) in 2 or 3 Phase Sour P
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08642 Practical Applications of Internal Corrosion Predictive Modeling (ICPM) in 2 or 3 Phase Sour Petroleum Pipelines: Model Validation

Product Number: 51300-08642-SG
ISBN: 08642 2008 CP
Author: Patrick J. Teevens and Keith Sand
Publication Date: 2008
$20.00
Picture for Stainless steel rebar for marine environment: a study of galvanic corrosion with carbon steel rebar used in the same concrete structure
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51318-11312-Stainless steel rebar for marine environment: a study of galvanic corrosion with carbon steel rebar used in the same concrete structure

Product Number: 51318-11312-SG
Author: Juliana Lopes Cardoso / Adriana de Araujo / Mayara Stecanella Pacheco / Jose Luis Serra Ribeiro / Zehbour Panossian
Publication Date: 2018
$20.00

This work aims at comparing a performance of the UNS(1) S32304 lean-duplex stainless steel rebars in electrical contact with carbon steel rebars, both embedded in concrete subjected to a chloride ion contamination.
Picture for 06637 VAPOR SPACE AND LIQUID/AIR INTERFACE
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06637 VAPOR SPACE AND LIQUID/AIR INTERFACE CORROSION OF LOW CARBON STEEL IN COMPLEX RADIOACTIVE HIGH LEVEL RADIOACTIVE WASTE

Product Number: 51300-06637-SG
ISBN: 06637 2006 CP
Author: Karthik H. Subramanian, Bruce J. Wiersma
$20.00

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